Knowledge · Damage mechanisms
How metals degrade,
and how to tell them apart.
100 categorised metal damage and failure mechanisms — each with a concise review, an original conceptual diagram, and source-qualified context.
Every mechanism keeps its original review fields and an original conceptual diagram. Photographs are being sourced separately; each will carry its source, licence, date and a credibility tier (80 = TWI/ASNT/ASME/ASTM/API/EPRI/peer-reviewed & recognised standards; 70 = Wikipedia/Wikimedia; 50 = other inspection & case sources; 20 = general web).
What the failure statistics actually say
These are investigation-cohort percentages with their own denominators — they describe the cases each organisation examined, not a worldwide incidence rate. They are not additive.
Oil, gas & maritime
DNV • published 2020 · More than 1,000 investigated component failures
Fatigue leads the reported mechanism classes in this investigation cohort.
Referral case series, not a random sample of operating assets. Exact n is not disclosed. Only the reported percentages are plotted.
Alberta pipelines
AER • 2025 failures · 229 pipeline failures (leaks or ruptures)
Internal corrosion is the leading reported category in this pipeline population.
Regulatory failure categories mix mechanisms, component labels and construction deficiencies. Rounded percentages; not all categories are shown.
Rolling bearings
SKF • published 2022 · Identified bearing failure modes in SKF investigations
Abrasive wear leads the reported bearing modes; 16% is surface-initiated fatigue, not all rolling-contact fatigue.
Sample size is not disclosed. These are shares of investigated damage modes, not probabilities that an installed bearing will fail.
Helicopter components
Davies et al. • 2013 · Failures in a 30-year AgustaWestland investigation review
Fatigue dominates this manufacturer-specific review, not necessarily other equipment populations.
Approximately 55%; exact n is unavailable in the accessible text. A selected component-investigation cohort, not a fatal-accident or fleet-wide failure rate.
DM-001Uniform aqueous corrosionAqueous & localized corrosion · General metal loss
Mechanism pathway
Service conditions
Conductive water; oxidant or reducible species; no single acid required
Physical processes
- Anodic metal dissolution
- Coupled cathodic reaction over the wetted surface
Observable damage
Broad thinning; rust or scale; weight loss
Possible failure mode
Perforation or pressure rupture
- Other names
- General corrosion; general wastage
- Industries / exposed sectors
- Water; chemical processing; marine; utilities
- Typically affected parts
- Tank walls; piping; exposed wetted surfaces
- Susceptible materials
- Iron and steel; other susceptible metals require environment-specific assessment
- Required chemicals / environment
- Conductive water; oxidant or reducible species; no single acid required
- Influencing parameters
- pH; temperature; oxygen; salinity; wetting time
- Physical explanation (1–3 processes)
- Anodic metal dissolution
- Coupled cathodic reaction over the wetted surface
- Signs and symptoms
- Broad thinning; rust or scale; weight loss
- Prevention / slowing the damage
- Keep surfaces dry where practical; use suitable barriers and engineered cathodic protection
- Typical failure outcome
- Perforation or pressure rupture
- Possible consequences
- Release; contamination; reduced load capacity
- Can be mistaken for
- Erosion-corrosion; oxidation; localized corrosion
- How to distinguish it
- Map thickness over a grid; identify electrolyte and products; separate general loss from isolated pits
- How often is it seen?
- No representative subtype-specific incidence was identified in the reviewed sources. This is a data gap, not evidence of rarity.
- Historical case / verification status
- No mechanism-attributed catastrophe was verified in the sources reviewed; this does not mean none has occurred.
Photographs — 5 needed (real-life, not diagrams)
Macro / field view
Close-up or micrograph
Cross-section
In-service failure
Distinguishing feature
Sources
- 80 TWI — What is Corrosion? Definition and Prevention — Technical reference (accessed 2026-09-08)
- 80 PHMSA — Fact Sheet: Corrosion — Regulatory technical/statistical reference (accessed 2026-09-08)
- 70 AMPP — Forms of Corrosion — Technical reference (accessed 2026-09-08)
Educational synthesis, not a diagnosis or repair instruction. Confirm the actual alloy, environment, loading and damage before selecting mitigation. Generic signs are not unique proof of a mechanism.
DM-002Atmospheric corrosionAqueous & localized corrosion · Thin-film corrosion
Mechanism pathway
Service conditions
Atmospheric moisture and deposited marine salts
Physical processes
- Thin electrolyte films enable electrochemical attack
- Wet/dry cycling concentrates contaminants
Observable damage
Rust; coating undercutting; section loss
Possible failure mode
Structural fracture or collapse after sufficient section loss
- Other names
- Weathering corrosion; atmospheric rusting
- Industries / exposed sectors
- Infrastructure; transport; marine; storage
- Typically affected parts
- Exposed bridge steel and comparable outdoor steelwork
- Susceptible materials
- Mild steel; painted or thermally sprayed aluminium-coated steel
- Required chemicals / environment
- Atmospheric moisture and deposited marine salts
- Influencing parameters
- Sheltering; orientation; coastal distance; salt deposition and weather
- Physical explanation (1–3 processes)
- Thin electrolyte films enable electrochemical attack
- Wet/dry cycling concentrates contaminants
- Signs and symptoms
- Rust; coating undercutting; section loss
- Prevention / slowing the damage
- Drainage; durable coatings; wash salt deposits; select exposure-appropriate alloys
- Typical failure outcome
- Structural fracture or collapse after sufficient section loss
- Possible consequences
- Reduced structural capacity; falling components
- Can be mistaken for
- CUI; filiform corrosion; soil corrosion
- How to distinguish it
- Establish exposure and wetting pattern; inspect coating and sheltered surfaces
- How often is it seen?
- No representative subtype-specific incidence was identified in the reviewed sources. This is a data gap, not evidence of rarity.
- Historical case / verification status
- No mechanism-attributed catastrophe was verified in the sources reviewed; this does not mean none has occurred.
Photographs — 5 needed (real-life, not diagrams)
Macro / field view
Close-up or micrograph
Cross-section
In-service failure
Distinguishing feature
Sources
- 80 Bullard, S.J., Holcomb, G.R. & Matthes, S.A. (2002). Atmospheric Corrosion of Steel and Coated Steel in Coastal Environments. CORROSION 2002, paper 02216. — Primary field-study abstract (accessed 2026-09-08)
- 80 TWI — What is Corrosion? Definition and Prevention — Technical reference (accessed 2026-09-08)
Educational synthesis, not a diagnosis or repair instruction. Confirm the actual alloy, environment, loading and damage before selecting mitigation. Generic signs are not unique proof of a mechanism.
DM-003Soil corrosionAqueous & localized corrosion · Buried-electrolyte corrosion
Mechanism pathway
Service conditions
Moist soil electrolyte; oxygen gradients; microbes may contribute
Physical processes
- Unequal soil exposure creates coupled anodic and cathodic regions
Observable damage
External pits; coating disbondment; thinning at soil transitions
Possible failure mode
Leak or rupture
- Other names
- Buried external corrosion
- Industries / exposed sectors
- Pipelines; water; foundations; power
- Typically affected parts
- Buried steel pipes, piles and reinforced infrastructure
- Susceptible materials
- Carbon steel; cast iron; metallic coatings
- Required chemicals / environment
- Moist soil electrolyte; oxygen gradients; microbes may contribute
- Influencing parameters
- Soil resistivity; moisture; pH; drainage; coating condition
- Physical explanation (1–3 processes)
- Unequal soil exposure creates coupled anodic and cathodic regions
- Signs and symptoms
- External pits; coating disbondment; thinning at soil transitions
- Prevention / slowing the damage
- Coating plus monitored cathodic protection; drainage; compatible backfill
- Typical failure outcome
- Leak or rupture
- Possible consequences
- Soil/water contamination; supply interruption
- Can be mistaken for
- MIC; stray-current corrosion; graphitic corrosion
- How to distinguish it
- Excavation evidence; soil/CP surveys; morphology and metallography; do not diagnose from resistivity alone
- How often is it seen?
- No representative subtype-specific incidence was identified in the reviewed sources. This is a data gap, not evidence of rarity.
- Historical case / verification status
- No mechanism-attributed catastrophe was verified in the sources reviewed; this does not mean none has occurred.
Photographs — 5 needed (real-life, not diagrams)
Macro / field view
Close-up or micrograph
Cross-section
In-service failure
Distinguishing feature
Sources
- 80 National Academies — Corrosion of Buried Steel at New and In-Service Infrastructure, chapter 6 — Scientific consensus report (accessed 2026-09-08)
- 80 PHMSA — Fact Sheet: External Corrosion — Regulatory technical reference (accessed 2026-09-08)
- 70 AMPP — Cathodic Protection for Corrosion Control — Technical reference (accessed 2026-09-08)
Educational synthesis, not a diagnosis or repair instruction. Confirm the actual alloy, environment, loading and damage before selecting mitigation. Generic signs are not unique proof of a mechanism.
DM-004Galvanic corrosionAqueous & localized corrosion · Electrically coupled corrosion
Mechanism pathway
Service conditions
Shared electrolyte and electrical continuity are necessary
Physical processes
- Electrical coupling drives anodic dissolution of the less noble member
Observable damage
Preferential attack beside dissimilar-metal contact
Possible failure mode
Local perforation; joint failure
- Other names
- Bimetallic corrosion; dissimilar-metal corrosion
- Industries / exposed sectors
- Marine; aerospace; utilities; process plants
- Typically affected parts
- Mixed-metal joints; fasteners; exchanger tubesheets
- Susceptible materials
- A less noble metal coupled to a more noble conductive surface
- Required chemicals / environment
- Shared electrolyte and electrical continuity are necessary
- Influencing parameters
- Relative electrochemical potential; exposed anode-to-cathode area; continuity of protection
- Physical explanation (1–3 processes)
- Electrical coupling drives anodic dissolution of the less noble member
- Signs and symptoms
- Preferential attack beside dissimilar-metal contact
- Prevention / slowing the damage
- Electrically isolate joints; compatible alloys; coat both members appropriately; avoid small-anode/large-cathode geometry
- Typical failure outcome
- Local perforation; joint failure
- Possible consequences
- Leak; loss of attachment
- Can be mistaken for
- Crevice corrosion; selective leaching
- How to distinguish it
- Confirm electrical continuity, electrolyte and polarity; compare attack on both coupled metals
- How often is it seen?
- No representative subtype-specific incidence was identified in the reviewed sources. This is a data gap, not evidence of rarity.
- Historical case / verification status
- No mechanism-attributed catastrophe was verified in the sources reviewed; this does not mean none has occurred.
Photographs — 5 needed (real-life, not diagrams)
Macro / field view
Close-up or micrograph
Cross-section
In-service failure
Distinguishing feature
Sources
- 80 TWI — What is Galvanic Corrosion and How Can it be Prevented? — Technical reference (accessed 2026-09-08)
- 80 Al-Mazeedi, H.A., Al-Farhan, A., Tanoli, N. & Abraham, L. (2019). A Study of Galvanic Corrosion in Stagnant Ammonium Bisulfide Solution. International Journal of Corrosion, 1325169, 9 pages. — Primary experimental paper (accessed 2026-09-08)
Educational synthesis, not a diagnosis or repair instruction. Confirm the actual alloy, environment, loading and damage before selecting mitigation. Generic signs are not unique proof of a mechanism.
DM-005Pitting corrosionAqueous & localized corrosion · Localized passive-film breakdown
Mechanism pathway
Service conditions
Electrolyte plus film-destabilizing chemistry; chloride common, not mandatory
Physical processes
- Local failure of passivity permits concentrated attack into the metal
Observable damage
Deep isolated cavities; small openings may hide large subsurface pits
Possible failure mode
Pinhole leak; rupture of a severely weakened section
- Other names
- Localized penetration; pit attack
- Industries / exposed sectors
- Chemical; marine; food; water
- Typically affected parts
- Chemical tanks and other wetted alloy equipment
- Susceptible materials
- Passivating alloys; the verified case concerns 316Ti stainless steel
- Required chemicals / environment
- Electrolyte plus film-destabilizing chemistry; chloride common, not mandatory
- Influencing parameters
- Temperature; potential; halides; surface finish; stagnation
- Physical explanation (1–3 processes)
- Local failure of passivity permits concentrated attack into the metal
- Signs and symptoms
- Deep isolated cavities; small openings may hide large subsurface pits
- Prevention / slowing the damage
- Control halides/deposits; select resistant alloys; passivate appropriately; inspect locally
- Typical failure outcome
- Pinhole leak; rupture of a severely weakened section
- Possible consequences
- Containment loss; hidden strength reduction; pits may initiate subsequent fatigue or SCC
- Can be mistaken for
- MIC; crevice corrosion; erosion craters
- How to distinguish it
- Measure pit depth and distribution; cross-section; analyse deposits and chemistry; morphology alone is insufficient
- How often is it seen?
- No representative subtype-specific incidence was identified in the reviewed sources. This is a data gap, not evidence of rarity.
- Historical case / verification status
- No mechanism-attributed catastrophe was verified in the sources reviewed; this does not mean none has occurred.
Photographs — 5 needed (real-life, not diagrams)
Macro / field view
Close-up or micrograph
Cross-section
In-service failure
Distinguishing feature
Sources
- 80 ASTM G46-21 — Examination and Evaluation of Pitting Corrosion — Official public standard scope (accessed 2026-09-08)
- 80 ASTM G48-25 — Pitting and Crevice Corrosion Resistance of Stainless Steels and Related Alloys by Use of Ferric Chloride Solution — Official public standard scope (accessed 2026-09-08)
- 80 TWI — Tank corrosion investigation — Primary case investigation (accessed 2026-09-08)
Educational synthesis, not a diagnosis or repair instruction. Confirm the actual alloy, environment, loading and damage before selecting mitigation. Generic signs are not unique proof of a mechanism.
DM-006Crevice corrosionAqueous & localized corrosion · Shielded localized attack
Mechanism pathway
Service conditions
Conductive liquid trapped in a restrictive gap; chlorides often aggravate
Physical processes
- Oxygen depletion inside a crevice
- Acidification and ion concentration destabilize passivity
Observable damage
Attack under gaskets or overlaps; intact adjacent open surface
Possible failure mode
Perforation; joint leakage
- Other names
- Occluded-cell corrosion
- Industries / exposed sectors
- Marine; chemical; water; desalination
- Typically affected parts
- Gaskets, washers, threads, lap joints and clamps
- Susceptible materials
- Stainless steels; aluminium; other passivating alloys
- Required chemicals / environment
- Conductive liquid trapped in a restrictive gap; chlorides often aggravate
- Influencing parameters
- Gap geometry; temperature; stagnation; oxygen access
- Physical explanation (1–3 processes)
- Oxygen depletion inside a crevice
- Acidification and ion concentration destabilize passivity
- Signs and symptoms
- Attack under gaskets or overlaps; intact adjacent open surface
- Prevention / slowing the damage
- Eliminate crevices; seal-weld where suitable; resistant alloys; clean deposits
- Typical failure outcome
- Perforation; joint leakage
- Possible consequences
- Release; loss of sealing/support
- Can be mistaken for
- Pitting; under-deposit corrosion
- How to distinguish it
- Demonstrate correspondence with the physical gap; section the joint and map the attack
- How often is it seen?
- No representative subtype-specific incidence was identified in the reviewed sources. This is a data gap, not evidence of rarity.
- Historical case / verification status
- No mechanism-attributed catastrophe was verified in the sources reviewed; this does not mean none has occurred.
Photographs — 5 needed (real-life, not diagrams)
Macro / field view
Close-up or micrograph
Cross-section
In-service failure
Distinguishing feature
Sources
- 70 AMPP — Crevice Corrosion — Technical reference (accessed 2026-09-08)
- 80 TWI — Lab Scale Corrosion Testing for Heat Exchangers (2019) — Primary testing summary (accessed 2026-09-08)
- 80 ASTM G48-25 — Pitting and Crevice Corrosion Resistance of Stainless Steels and Related Alloys by Use of Ferric Chloride Solution — Official public standard scope (accessed 2026-09-08)
Educational synthesis, not a diagnosis or repair instruction. Confirm the actual alloy, environment, loading and damage before selecting mitigation. Generic signs are not unique proof of a mechanism.
DM-007Under-deposit corrosionAqueous & localized corrosion · Deposit-created microenvironment
Mechanism pathway
Service conditions
Wetted deposits; corrosive species may concentrate beneath them
Physical processes
- Boiling beneath porous deposits can concentrate aggressive dissolved species
Observable damage
Local wall loss beneath deposits
Possible failure mode
Leak or local rupture
- Other names
- Deposit-associated localized corrosion
- Industries / exposed sectors
- Boilers; cooling water; oil/gas; chemical
- Typically affected parts
- Tube surfaces; low-flow pipe sections; tank bottoms
- Susceptible materials
- Carbon steel; low-alloy and stainless steels
- Required chemicals / environment
- Wetted deposits; corrosive species may concentrate beneath them
- Influencing parameters
- Deposit porosity; heat flux; flow; bulk and local chemistry
- Physical explanation (1–3 processes)
- Boiling beneath porous deposits can concentrate aggressive dissolved species
- Signs and symptoms
- Local wall loss beneath deposits
- Prevention / slowing the damage
- Control fouling and water chemistry; maintain flow; qualified cleaning
- Typical failure outcome
- Leak or local rupture
- Possible consequences
- Tube failure; process cross-contamination
- Can be mistaken for
- MIC; caustic gouging; oxygen pitting
- How to distinguish it
- Preserve deposits; analyse layers and local conditions; distinguish the specific chemical driver
- How often is it seen?
- Alberta, 2025: 19% of internal-corrosion pipeline failures were assigned to this mechanism. Denominator: internal-corrosion failures, NOT all 229 pipeline failures or all industries. No representative worldwide rate identified.
- Historical case / verification status
- No mechanism-attributed catastrophe was verified in the sources reviewed; this does not mean none has occurred.
Photographs — 5 needed (real-life, not diagrams)
Macro / field view
Close-up or micrograph
Cross-section
In-service failure
Distinguishing feature
Sources
- 50 Veolia Water Technologies — Water Handbook, chapter 11: Preboiler and Boiler Corrosion Control — Manufacturer technical handbook (accessed 2026-09-08)
- 80 PHMSA — Fact Sheet: Internal Corrosion — Regulatory technical reference (accessed 2026-09-08)
- 80 Alberta Energy Regulator — Pipeline Performance: Industry Performance Metrics, 2025 — Regulatory failure statistics (accessed 2026-09-08)
Educational synthesis, not a diagnosis or repair instruction. Confirm the actual alloy, environment, loading and damage before selecting mitigation. Generic signs are not unique proof of a mechanism.
DM-008Corrosion under insulationAqueous & localized corrosion · Hidden external attack
Mechanism pathway
Service conditions
Water ingress; salts can intensify damage
Physical processes
- Wet insulation retains an electrolyte against metal
- Concentration during drying intensifies localized attack
Observable damage
Rust staining; damaged jackets; concealed thinning
Possible failure mode
Leak or rupture
- Other names
- CUI; external corrosion under insulation
- Industries / exposed sectors
- Refining; chemical; power; offshore
- Typically affected parts
- Insulated piping; vessels; supports; penetrations
- Susceptible materials
- Carbon/low-alloy steel; stainless steel can develop chloride SCC
- Required chemicals / environment
- Water ingress; salts can intensify damage
- Influencing parameters
- Wetting/drying; temperature cycles; jacket integrity; drainage
- Physical explanation (1–3 processes)
- Wet insulation retains an electrolyte against metal
- Concentration during drying intensifies localized attack
- Signs and symptoms
- Rust staining; damaged jackets; concealed thinning
- Prevention / slowing the damage
- Maintain an engineered moisture barrier and inspect concealed surfaces; TSA coatings have been studied for CUI mitigation
- Typical failure outcome
- Leak or rupture
- Possible consequences
- Unexpected loss of containment; difficult inspection
- Can be mistaken for
- Atmospheric corrosion; external chloride SCC; soil attack
- How to distinguish it
- Inspect beneath insulation; thickness mapping; distinguish metal loss from cracking in stainless steel
- How often is it seen?
- No representative subtype-specific incidence was identified in the reviewed sources. This is a data gap, not evidence of rarity.
- Historical case / verification status
- No mechanism-attributed catastrophe was verified in the sources reviewed; this does not mean none has occurred.
Photographs — 5 needed (real-life, not diagrams)
Macro / field view
Close-up or micrograph
Cross-section
In-service failure
Distinguishing feature
Sources
- 80 Begg, H. — Evaluation of a New Corrosion Under Insulation Test Method. TWI Report Summary 1097/2018. — Primary research summary (accessed 2026-09-08)
- 80 TWI — Corrosion Under Insulation at Seminar (13 March 2020) — Technical reference (accessed 2026-09-08)
- 80 TWI — Research into corrosion under insulation (20 February 2019) — Technical reference (accessed 2026-09-08)
Educational synthesis, not a diagnosis or repair instruction. Confirm the actual alloy, environment, loading and damage before selecting mitigation. Generic signs are not unique proof of a mechanism.
DM-009Microbiologically influenced corrosionAqueous & localized corrosion · Biologically influenced electrochemistry
Mechanism pathway
Service conditions
Microbial activity in a compatible wet environment; nutrient and redox conditions vary
Physical processes
- Microbial activity changes local corrosion reactions and chemistry
Observable damage
Localized attack under biofilms; deposits; sometimes tubercles
Possible failure mode
Pinhole leak or rupture
- Other names
- MIC; biocorrosion
- Industries / exposed sectors
- Water, wastewater, marine and hydrocarbon/process systems
- Typically affected parts
- Deadlegs; tanks; pipelines; heat exchangers
- Susceptible materials
- Steels; stainless steels; copper and aluminium alloys
- Required chemicals / environment
- Microbial activity in a compatible wet environment; nutrient and redox conditions vary
- Influencing parameters
- Biofilm; stagnation; temperature; redox conditions; treatment history
- Physical explanation (1–3 processes)
- Microbial activity changes local corrosion reactions and chemistry
- Signs and symptoms
- Localized attack under biofilms; deposits; sometimes tubercles
- Prevention / slowing the damage
- Control biofilms and deposits; suitable treatment; flow management; compatible materials
- Typical failure outcome
- Pinhole leak or rupture
- Possible consequences
- Contamination; release; downtime
- Can be mistaken for
- Abiotic pitting; under-deposit attack; sulfide corrosion
- How to distinguish it
- Combine microbiology, chemistry, metallography and operations evidence; finding microbes alone does not prove MIC
- How often is it seen?
- Alberta, 2025: 7% of internal-corrosion pipeline failures were assigned to this mechanism. Denominator: internal-corrosion failures, NOT all 229 pipeline failures or all industries. No representative worldwide rate identified.
- Historical case / verification status
- No mechanism-attributed catastrophe was verified in the sources reviewed; this does not mean none has occurred.
Photographs — 5 needed (real-life, not diagrams)
Macro / field view
Close-up or micrograph
Cross-section
In-service failure
Distinguishing feature
Sources
- 70 AMPP — Microbiologically Influenced Corrosion (MIC) — Technical reference (accessed 2026-09-08)
- 80 Little, B.J. & Lee, J.S. (2006). Diagnosing Microbiologically Influenced Corrosion: A State-of-the-Art Review. CORROSION 62(11), 1006–1017. — Research abstract (accessed 2026-09-08)
- 80 Alberta Energy Regulator — Pipeline Performance: Industry Performance Metrics, 2025 — Regulatory failure statistics (accessed 2026-09-08)
Educational synthesis, not a diagnosis or repair instruction. Confirm the actual alloy, environment, loading and damage before selecting mitigation. Generic signs are not unique proof of a mechanism.
DM-010DC stray-current corrosionAqueous & localized corrosion · Electrical interference
Mechanism pathway
Service conditions
Electrolyte and unintended DC current path
Physical processes
- Metal dissolves where conventional current leaves the structure into the electrolyte
Observable damage
Concentrated external pits; time-varying structure-to-soil potentials
Possible failure mode
Perforation or rupture
- Other names
- Electrolytic corrosion; stray direct-current attack
- Industries / exposed sectors
- Pipelines and infrastructure near DC transit or other current sources
- Typically affected parts
- Buried steel pipes, tanks and electrically continuous piles
- Susceptible materials
- Conductive metals exposed to an electrolyte
- Required chemicals / environment
- Electrolyte and unintended DC current path
- Influencing parameters
- Current magnitude/direction; coating holidays; rail-return design
- Physical explanation (1–3 processes)
- Metal dissolves where conventional current leaves the structure into the electrolyte
- Signs and symptoms
- Concentrated external pits; time-varying structure-to-soil potentials
- Prevention / slowing the damage
- Identify current source; engineered drainage/bonding; insulation; coordinated CP
- Typical failure outcome
- Perforation or rupture
- Possible consequences
- Leak; shortened asset life
- Can be mistaken for
- Soil corrosion; AC corrosion; galvanic corrosion
- How to distinguish it
- Time-synchronized potential/current surveys linked to source operation; locate current-discharge areas
- How often is it seen?
- No representative subtype-specific incidence was identified in the reviewed sources. This is a data gap, not evidence of rarity.
- Historical case / verification status
- No mechanism-attributed catastrophe was verified in the sources reviewed; this does not mean none has occurred.
Photographs — 5 needed (real-life, not diagrams)
Macro / field view
Close-up or micrograph
Cross-section
In-service failure
Distinguishing feature
Sources
- 80 The Electrochemical Origin of Internal Stray Currents (2020). Materials Performance 59(9), 26. — Primary technical article (accessed 2026-09-08)
- 70 AMPP — Cathodic Protection for Corrosion Control — Technical reference (accessed 2026-09-08)
- 80 PHMSA — Fact Sheet: External Corrosion — Regulatory technical reference (accessed 2026-09-08)
- 80 National Academies — Corrosion of Buried Steel at New and In-Service Infrastructure, chapter 6 — Scientific consensus report (accessed 2026-09-08)
Educational synthesis, not a diagnosis or repair instruction. Confirm the actual alloy, environment, loading and damage before selecting mitigation. Generic signs are not unique proof of a mechanism.
DM-011AC-induced corrosionAqueous & localized corrosion · Electrical interference
Mechanism pathway
Service conditions
Soil electrolyte plus induced/conducted AC
Physical processes
- Proposed explanations include nonlinear electrochemical rectification and cyclic changes to surface films; no single model explains all AC corrosion.
Observable damage
Severe localized loss at small coating defects
Possible failure mode
Pinhole leak or rupture
- Other names
- Alternating-current corrosion
- Industries / exposed sectors
- Pipelines beside AC power lines or rail systems
- Typically affected parts
- Coating holidays on buried steel pipelines
- Susceptible materials
- Cathodically protected carbon steel
- Required chemicals / environment
- Soil electrolyte plus induced/conducted AC
- Influencing parameters
- AC/DC current density; holiday size; soil chemistry; CP level
- Physical explanation (1–3 processes)
- Proposed explanations include nonlinear electrochemical rectification and cyclic changes to surface films; no single model explains all AC corrosion.
- Signs and symptoms
- Severe localized loss at small coating defects
- Prevention / slowing the damage
- AC-interference assessment; engineered grounding/decoupling; monitor coupons and CP
- Typical failure outcome
- Pinhole leak or rupture
- Possible consequences
- Pipeline release; electrical safety hazard may coexist
- Can be mistaken for
- DC corrosion; ordinary external corrosion
- How to distinguish it
- Measure AC and DC current/potential, coupon loss and coating defects; adequate CP potential alone does not exclude AC damage
- How often is it seen?
- No representative subtype-specific incidence was identified in the reviewed sources. This is a data gap, not evidence of rarity.
- Historical case / verification status
- No mechanism-attributed catastrophe was verified in the sources reviewed; this does not mean none has occurred.
Photographs — 5 needed (real-life, not diagrams)
Macro / field view
Close-up or micrograph
Cross-section
In-service failure
Distinguishing feature
Sources
- 80 The AC Corrosion Mechanisms and Models: A Review. CORROSION 76(2), 188 (2020). — Research abstract (accessed 2026-09-08)
- 80 Hosokawa, Y. et al. (2004). Alternating-Current Corrosion Risk Arising from Alternating-Current-Powered Rail Transit Systems. CORROSION 60(4), 408–413. — Primary field-study abstract (accessed 2026-09-08)
Educational synthesis, not a diagnosis or repair instruction. Confirm the actual alloy, environment, loading and damage before selecting mitigation. Generic signs are not unique proof of a mechanism.
DM-012Intergranular corrosionAqueous & localized corrosion · Grain-boundary selective attack
Mechanism pathway
Service conditions
Corrosive electrolyte compatible with the depleted/segregated boundary region
Physical processes
- Boundary segregation or precipitation creates locally susceptible regions
- Selective boundary dissolution can detach otherwise intact grains
Observable damage
Boundary attack, grain loss and reduced mechanical integrity
Possible failure mode
Leak or brittle-appearing separation
- Other names
- IGC; intercrystalline corrosion
- Industries / exposed sectors
- Chemical; aerospace; heat treatment; food
- Typically affected parts
- Sensitized weld HAZ; heat-exchanger tubes; alloy sheet
- Susceptible materials
- Susceptible stainless steels and aluminium alloys
- Required chemicals / environment
- Corrosive electrolyte compatible with the depleted/segregated boundary region
- Influencing parameters
- Thermal history; sensitization; chemistry; temperature
- Physical explanation (1–3 processes)
- Boundary segregation or precipitation creates locally susceptible regions
- Selective boundary dissolution can detach otherwise intact grains
- Signs and symptoms
- Boundary attack, grain loss and reduced mechanical integrity
- Prevention / slowing the damage
- Control alloy composition and thermal exposure; appropriate solution treatment; validated corrosion testing
- Typical failure outcome
- Leak or brittle-appearing separation
- Possible consequences
- Unexpected loss of ductility and containment
- Can be mistaken for
- SCC; liquation cracking; exfoliation
- How to distinguish it
- Metallographic boundary attack plus sensitization/chemistry evidence; assess whether tensile stress was essential
- How often is it seen?
- No representative subtype-specific incidence was identified in the reviewed sources. This is a data gap, not evidence of rarity.
- Historical case / verification status
- No mechanism-attributed catastrophe was verified in the sources reviewed; this does not mean none has occurred.
Photographs — 5 needed (real-life, not diagrams)
Macro / field view
Close-up or micrograph
Cross-section
In-service failure
Distinguishing feature
Sources
- 70 AMPP — Intergranular Corrosion — Technical reference (accessed 2026-09-08)
- 80 TWI — Embrittlement of austenitic steel welds at high temperature — Technical reference (accessed 2026-09-08)
Educational synthesis, not a diagnosis or repair instruction. Confirm the actual alloy, environment, loading and damage before selecting mitigation. Generic signs are not unique proof of a mechanism.
DM-013Exfoliation corrosionAqueous & localized corrosion · Advanced intergranular corrosion
Mechanism pathway
Service conditions
Corrosive moisture, often chloride-bearing
Physical processes
- Intergranular attack follows elongated grain paths
- Expanding corrosion products lift surface layers
Observable damage
Leaf-like lifting; bulging; delamination
Possible failure mode
Component separation or fracture after section degradation
- Other names
- EXCO; layer lifting
- Industries / exposed sectors
- Aerospace; transport; marine
- Typically affected parts
- Heavily worked aluminium sections, especially exposed end grains at edges or holes
- Susceptible materials
- Susceptible high-strength aluminium with flattened, elongated grains
- Required chemicals / environment
- Corrosive moisture, often chloride-bearing
- Influencing parameters
- Grain orientation; temper; residual stress; salt wetting
- Physical explanation (1–3 processes)
- Intergranular attack follows elongated grain paths
- Expanding corrosion products lift surface layers
- Signs and symptoms
- Leaf-like lifting; bulging; delamination
- Prevention / slowing the damage
- Resistant temper/alloy; coatings and sealants; drainage; inspect lap joints
- Typical failure outcome
- Component separation or fracture after section degradation
- Possible consequences
- Reduced structural capacity
- Can be mistaken for
- Lamination defects; blistering; general IGC
- How to distinguish it
- Cross-section shows corrosion along elongated grain boundaries and wedging products, not a clean manufacturing interface
- How often is it seen?
- No representative subtype-specific incidence was identified in the reviewed sources. This is a data gap, not evidence of rarity.
- Historical case / verification status
- No mechanism-attributed catastrophe was verified in the sources reviewed; this does not mean none has occurred.
Photographs — 5 needed (real-life, not diagrams)
Macro / field view
Close-up or micrograph
Cross-section
In-service failure
Distinguishing feature
Sources
- 70 AMPP — Exfoliation — Technical reference (accessed 2026-09-08)
- 80 TWI — Weldability of materials: aluminium alloys, Job Knowledge 21 — Technical reference (accessed 2026-09-08)
Educational synthesis, not a diagnosis or repair instruction. Confirm the actual alloy, environment, loading and damage before selecting mitigation. Generic signs are not unique proof of a mechanism.
DM-014DezincificationAqueous & localized corrosion · Dealloying
Mechanism pathway
Service conditions
Aqueous electrolyte; chemistry determines susceptibility
Physical processes
- Net zinc loss produces a copper-rich porous layer; dissolution and copper redeposition can contribute.
Observable damage
Porous copper-rich layers or localized plugs; strength loss
Possible failure mode
Leak; brittle-appearing fitting break
- Other names
- Selective zinc leaching from brass
- Industries / exposed sectors
- Water; plumbing; marine; process
- Typically affected parts
- Brass valves; fittings; tubes; fasteners
- Susceptible materials
- Susceptible copper-zinc alloys
- Required chemicals / environment
- Aqueous electrolyte; chemistry determines susceptibility
- Influencing parameters
- Temperature; stagnation; chloride; pH; alloy phase balance
- Physical explanation (1–3 processes)
- Net zinc loss produces a copper-rich porous layer; dissolution and copper redeposition can contribute.
- Signs and symptoms
- Porous copper-rich layers or localized plugs; strength loss
- Prevention / slowing the damage
- Dezincification-resistant brass; water chemistry control; suitable alternative alloy
- Typical failure outcome
- Leak; brittle-appearing fitting break
- Possible consequences
- Flooding; loss of isolation
- Can be mistaken for
- General brass corrosion; ammonia SCC
- How to distinguish it
- Cross-section and elemental analysis show zinc depletion/porosity rather than a stress-driven crack
- How often is it seen?
- No representative subtype-specific incidence was identified in the reviewed sources. This is a data gap, not evidence of rarity.
- Historical case / verification status
- No mechanism-attributed catastrophe was verified in the sources reviewed; this does not mean none has occurred.
Photographs — 5 needed (real-life, not diagrams)
Macro / field view
Close-up or micrograph
Cross-section
In-service failure
Distinguishing feature
Sources
- 70 AMPP — Dealloying (selective leaching) — Technical reference (accessed 2026-09-08)
- CUterms
Educational synthesis, not a diagnosis or repair instruction. Confirm the actual alloy, environment, loading and damage before selecting mitigation. Generic signs are not unique proof of a mechanism.
DM-015Graphitic corrosion of cast ironAqueous & localized corrosion · Dealloying
Mechanism pathway
Service conditions
Corrosive water or moist soil
Physical processes
- Iron dissolves around the pre-existing graphite network
- Graphite and corrosion products preserve shape while strength falls
Observable damage
Soft dark surface; original shape despite severe weakening
Possible failure mode
Crushing; brittle break; leakage
- Other names
- Graphitic selective leaching; graphitic corrosion
- Industries / exposed sectors
- Water; wastewater; buried services
- Typically affected parts
- Cast-iron mains; valves; pump bodies
- Susceptible materials
- Graphite-containing cast iron, especially grey iron
- Required chemicals / environment
- Corrosive water or moist soil
- Influencing parameters
- Time; soil/water chemistry; graphite morphology
- Physical explanation (1–3 processes)
- Iron dissolves around the pre-existing graphite network
- Graphite and corrosion products preserve shape while strength falls
- Signs and symptoms
- Soft dark surface; original shape despite severe weakening
- Prevention / slowing the damage
- Protective linings/coatings; appropriate CP; condition assessment and replacement
- Typical failure outcome
- Crushing; brittle break; leakage
- Possible consequences
- Sudden main break; flooding
- Can be mistaken for
- Thermal graphitization: a different metallurgical process
- How to distinguish it
- Metallography reveals removed iron around pre-existing graphite; thermal graphitization instead precipitates new graphite in steel
- How often is it seen?
- No representative subtype-specific incidence was identified in the reviewed sources. This is a data gap, not evidence of rarity.
- Historical case / verification status
- No mechanism-attributed catastrophe was verified in the sources reviewed; this does not mean none has occurred.
Photographs — 5 needed (real-life, not diagrams)
Macro / field view
Close-up or micrograph
Cross-section
In-service failure
Distinguishing feature
Sources
- 70 AMPP — Dealloying (selective leaching) — Technical reference (accessed 2026-09-08)
- 80 TWI — What is graphitisation? — Technical reference (accessed 2026-09-08)
Educational synthesis, not a diagnosis or repair instruction. Confirm the actual alloy, environment, loading and damage before selecting mitigation. Generic signs are not unique proof of a mechanism.
DM-016DenickelificationAqueous & localized corrosion · Dealloying
Mechanism pathway
Service conditions
Corrosive process condensate; particular deposited/hot-spot environments
Physical processes
- Preferential nickel loss creates a copper-rich weakened layer
Observable damage
Porosity; local wall loss; copper-rich residue
Possible failure mode
Tube leak or rupture
- Other names
- Selective nickel leaching
- Industries / exposed sectors
- Refining; heat exchange; marine systems
- Typically affected parts
- Copper-nickel condenser tubes at deposit-associated hot spots
- Susceptible materials
- Susceptible copper-nickel alloys, including 70/30 Cu-Ni
- Required chemicals / environment
- Corrosive process condensate; particular deposited/hot-spot environments
- Influencing parameters
- Temperature differences; deposits; local chemistry; thermal coupling
- Physical explanation (1–3 processes)
- Preferential nickel loss creates a copper-rich weakened layer
- Signs and symptoms
- Porosity; local wall loss; copper-rich residue
- Prevention / slowing the damage
- Address deposits, hot spots and stagnant regions within an approved operating programme
- Typical failure outcome
- Tube leak or rupture
- Possible consequences
- Cross-contamination; process outage
- Can be mistaken for
- Dezincification; general Cu-Ni corrosion
- How to distinguish it
- Elemental mapping confirms nickel depletion, not zinc loss; correlate with temperature/deposit pattern
- How often is it seen?
- No representative subtype-specific incidence was identified in the reviewed sources. This is a data gap, not evidence of rarity.
- Historical case / verification status
- No mechanism-attributed catastrophe was verified in the sources reviewed; this does not mean none has occurred.
Photographs — 5 needed (real-life, not diagrams)
Macro / field view
Close-up or micrograph
Cross-section
In-service failure
Distinguishing feature
Sources
- 70 Copper Development Association — Copper-nickel: corrosion resistance and antifouling — Technical reference (accessed 2026-09-08)
- CUterms
Educational synthesis, not a diagnosis or repair instruction. Confirm the actual alloy, environment, loading and damage before selecting mitigation. Generic signs are not unique proof of a mechanism.
DM-017Filiform corrosionAqueous & localized corrosion · Coating-underfilm attack
Mechanism pathway
Service conditions
Moisture penetrates a breached or permeable surface coating
Physical processes
- An active filament head advances under the coating
- Differential aeration separates head and trailing products
Observable damage
Thread-like tracks below paint; cosmetic blistering
Possible failure mode
Coating disbondment or cosmetic rejection; structural failure is not inevitable
- Other names
- Underfilm filamentary corrosion
- Industries / exposed sectors
- Automotive; aerospace; coated products
- Typically affected parts
- Painted aluminium, steel or magnesium sheet
- Susceptible materials
- Coated reactive metals
- Required chemicals / environment
- Moisture penetrates a breached or permeable surface coating
- Influencing parameters
- Coating defects, moisture permeability and adhesion
- Physical explanation (1–3 processes)
- An active filament head advances under the coating
- Differential aeration separates head and trailing products
- Signs and symptoms
- Thread-like tracks below paint; cosmetic blistering
- Prevention / slowing the damage
- Use a well-adhered coating with appropriate resistance to water-vapour transmission
- Typical failure outcome
- Coating disbondment or cosmetic rejection; structural failure is not inevitable
- Possible consequences
- Appearance degradation; reduced coating protection
- Can be mistaken for
- General underfilm corrosion; scratch marks; fungal growth
- How to distinguish it
- Lift coating locally and examine corrosion filaments and metal attack; do not identify from paint pattern alone
- How often is it seen?
- No representative subtype-specific incidence was identified in the reviewed sources. This is a data gap, not evidence of rarity.
- Historical case / verification status
- No mechanism-attributed catastrophe was verified in the sources reviewed; this does not mean none has occurred.
Photographs — 5 needed (real-life, not diagrams)
Macro / field view
Close-up or micrograph
Cross-section
In-service failure
Distinguishing feature
Sources
- 70 AMPP — Filiform Corrosion (page title: Fillform Corrosion) — Technical reference (accessed 2026-09-08)
- 80 Van Loo, M. et al. (1953). Filiform Corrosion. CORROSION 9(8), 277–283. — Primary research abstract (accessed 2026-09-08)
Educational synthesis, not a diagnosis or repair instruction. Confirm the actual alloy, environment, loading and damage before selecting mitigation. Generic signs are not unique proof of a mechanism.
DM-018Carbon dioxide corrosionProcess-specific aqueous corrosion · Acid-gas aqueous corrosion
Mechanism pathway
Service conditions
Free water and dissolved CO2; impurities can change behaviour
Physical processes
- Dissolved CO2 establishes an acidic aqueous environment
- Iron dissolution competes with protective carbonate-scale formation
Observable damage
General thinning; local pits or mesa-like attack
Possible failure mode
Leak or rupture
- Other names
- CO2 corrosion; sweet corrosion
- Industries / exposed sectors
- Oil and gas production and wet CO2-containing process streams
- Typically affected parts
- Wet pipelines; production tubing; vessels
- Susceptible materials
- Carbon and low-alloy steels
- Required chemicals / environment
- Free water and dissolved CO2; impurities can change behaviour
- Influencing parameters
- CO2 and other gas composition; water chemistry; operating conditions; material
- Physical explanation (1–3 processes)
- Dissolved CO2 establishes an acidic aqueous environment
- Iron dissolution competes with protective carbonate-scale formation
- Signs and symptoms
- General thinning; local pits or mesa-like attack
- Prevention / slowing the damage
- Manage water and impurities; validated inhibitors; resistant materials; monitor scale/flow
- Typical failure outcome
- Leak or rupture
- Possible consequences
- Hydrocarbon/CO2 release; shutdown
- Can be mistaken for
- Wet H2S corrosion; oxygen corrosion; erosion-corrosion
- How to distinguish it
- Analyse gas/liquid and carbonate scale; morphology alone does not identify CO2
- How often is it seen?
- Alberta, 2025: 6% of internal-corrosion pipeline failures were assigned to this mechanism. Denominator: internal-corrosion failures, NOT all 229 pipeline failures or all industries. No representative worldwide rate identified.
- Historical case / verification status
- No mechanism-attributed catastrophe was verified in the sources reviewed; this does not mean none has occurred.
Photographs — 5 needed (real-life, not diagrams)
Macro / field view
Close-up or micrograph
Cross-section
In-service failure
Distinguishing feature
Sources
- 80 TWI — CO2 Corrosion — Technical reference (accessed 2026-09-08)
- 80 TWI — Selection of Materials for High Pressure CO2 Transport — Technical research paper (accessed 2026-09-08)
- 80 PHMSA — Fact Sheet: Internal Corrosion — Regulatory technical reference (accessed 2026-09-08)
- 80 Alberta Energy Regulator — Pipeline Performance: Industry Performance Metrics, 2025 — Regulatory failure statistics (accessed 2026-09-08)
Educational synthesis, not a diagnosis or repair instruction. Confirm the actual alloy, environment, loading and damage before selecting mitigation. Generic signs are not unique proof of a mechanism.
DM-019Wet hydrogen sulfide corrosionProcess-specific aqueous corrosion · Acid-gas aqueous corrosion
Mechanism pathway
Service conditions
Water and H2S
Physical processes
- Iron dissolution forms iron-sulfide products
- Film damage or unstable scales permit continued attack
Observable damage
Black sulfide deposits; thinning or pitting
Possible failure mode
Leak or rupture
- Other names
- Sour corrosion; aqueous H2S metal loss
- Industries / exposed sectors
- Sour oil/gas and associated process equipment
- Typically affected parts
- Pipelines; separators; sour-water piping
- Susceptible materials
- Carbon/low-alloy steel; other alloys depending on environment
- Required chemicals / environment
- Water and H2S
- Influencing parameters
- pH; H2S activity; temperature; flow; sulfide-film stability
- Physical explanation (1–3 processes)
- Iron dissolution forms iron-sulfide products
- Film damage or unstable scales permit continued attack
- Signs and symptoms
- Black sulfide deposits; thinning or pitting
- Prevention / slowing the damage
- Sour-service materials; chemistry and flow control; suitable inhibition; monitoring
- Typical failure outcome
- Leak or rupture
- Possible consequences
- Toxic H2S release; outage
- Can be mistaken for
- Sulfidation; SSC; HIC; CO2 corrosion
- How to distinguish it
- Prove wet service and metal loss; test separately for hydrogen-assisted cracking; black scale alone is not diagnostic
- How often is it seen?
- No representative subtype-specific incidence was identified in the reviewed sources. This is a data gap, not evidence of rarity.
- Historical case / verification status
- No mechanism-attributed catastrophe was verified in the sources reviewed; this does not mean none has occurred.
Photographs — 5 needed (real-life, not diagrams)
Macro / field view
Close-up or micrograph
Cross-section
In-service failure
Distinguishing feature
Sources
- 80 TWI — Sour Testing — Technical reference (accessed 2026-09-08)
- 80 Al-Mazeedi, H.A., Al-Farhan, A., Tanoli, N. & Abraham, L. (2019). A Study of Galvanic Corrosion in Stagnant Ammonium Bisulfide Solution. International Journal of Corrosion, 1325169, 9 pages. — Primary experimental paper (accessed 2026-09-08)
- 80 PHMSA — Fact Sheet: Internal Corrosion — Regulatory technical reference (accessed 2026-09-08)
Educational synthesis, not a diagnosis or repair instruction. Confirm the actual alloy, environment, loading and damage before selecting mitigation. Generic signs are not unique proof of a mechanism.
DM-020Hydrochloric acid corrosionProcess-specific aqueous corrosion · Mineral-acid corrosion
Mechanism pathway
Service conditions
Aqueous hydrochloric acid
Physical processes
- Acid-driven electrochemical dissolution consumes susceptible metal
Observable damage
Rapid thinning; rough etched surfaces; localized attack
Possible failure mode
Leak; local rupture
- Other names
- HCl attack; hydrochloric-acid dewpoint corrosion
- Industries / exposed sectors
- Chemical processing
- Typically affected parts
- Overhead condensers; piping; acid tanks
- Susceptible materials
- Carbon steel; many stainless grades; alloy resistance depends on concentration
- Required chemicals / environment
- Aqueous hydrochloric acid
- Influencing parameters
- Acid concentration; temperature; oxidizing impurities
- Physical explanation (1–3 processes)
- Acid-driven electrochemical dissolution consumes susceptible metal
- Signs and symptoms
- Rapid thinning; rough etched surfaces; localized attack
- Prevention / slowing the damage
- Control chloride sources and condensate chemistry; engineered wash/neutralization; qualified alloy selection
- Typical failure outcome
- Leak; local rupture
- Possible consequences
- Acid exposure; process contamination
- Can be mistaken for
- NH4Cl corrosion; other acid attack
- How to distinguish it
- Sample initial condensate and deposits; determine chloride, acidity and temperature history
- How often is it seen?
- No representative subtype-specific incidence was identified in the reviewed sources. This is a data gap, not evidence of rarity.
- Historical case / verification status
- No mechanism-attributed catastrophe was verified in the sources reviewed; this does not mean none has occurred.
Photographs — 5 needed (real-life, not diagrams)
Macro / field view
Close-up or micrograph
Cross-section
In-service failure
Distinguishing feature
Sources
- 50 Haynes International — Corrosive Environments — Manufacturer technical guide (accessed 2026-09-08)
- 50 Haynes International — HASTELLOY HYBRID-BC1 alloy — Primary manufacturer test data (accessed 2026-09-08)
- 80 TWI — Corrosion in Petrochemical and Refinery Industries (27 June 2022) — Technical reference (accessed 2026-09-08)
Educational synthesis, not a diagnosis or repair instruction. Confirm the actual alloy, environment, loading and damage before selecting mitigation. Generic signs are not unique proof of a mechanism.
DM-021Sulfuric acid corrosionProcess-specific aqueous corrosion · Mineral-acid corrosion
Mechanism pathway
Service conditions
Sulfuric acid with water; oxidants/impurities modify attack
Physical processes
- Acidic electrochemical attack depends on alloy and the stability of protective surface films
Observable damage
Thinning; etched surfaces; local erosion-corrosion
Possible failure mode
Leak; rupture
- Other names
- H2SO4 attack
- Industries / exposed sectors
- Fertilizer; chemical; mineral processing; batteries
- Typically affected parts
- Acid tanks; pumps; piping; exchangers
- Susceptible materials
- Steel and corrosion-resistant alloys, depending strongly on acid concentration
- Required chemicals / environment
- Sulfuric acid with water; oxidants/impurities modify attack
- Influencing parameters
- Acid concentration, temperature, impurities and flow
- Physical explanation (1–3 processes)
- Acidic electrochemical attack depends on alloy and the stability of protective surface films
- Signs and symptoms
- Thinning; etched surfaces; local erosion-corrosion
- Prevention / slowing the damage
- Select alloy/lining for the actual concentration-temperature envelope; prevent unintended dilution
- Typical failure outcome
- Leak; rupture
- Possible consequences
- Acid burns; environmental release
- Can be mistaken for
- Acid-dewpoint corrosion; HCl attack
- How to distinguish it
- Analyse acid concentration and impurities; reconstruct dilution/temperature excursions
- How often is it seen?
- No representative subtype-specific incidence was identified in the reviewed sources. This is a data gap, not evidence of rarity.
- Historical case / verification status
- No mechanism-attributed catastrophe was verified in the sources reviewed; this does not mean none has occurred.
Photographs — 5 needed (real-life, not diagrams)
Macro / field view
Close-up or micrograph
Cross-section
In-service failure
Distinguishing feature
Sources
- 50 Haynes International — Corrosive Environments — Manufacturer technical guide (accessed 2026-09-08)
- 50 Haynes International — HASTELLOY HYBRID-BC1 alloy — Primary manufacturer test data (accessed 2026-09-08)
Educational synthesis, not a diagnosis or repair instruction. Confirm the actual alloy, environment, loading and damage before selecting mitigation. Generic signs are not unique proof of a mechanism.
DM-022Hydrofluoric acid corrosionProcess-specific aqueous corrosion · Mineral-acid corrosion
Mechanism pathway
Service conditions
HF-containing service; water and contaminants change severity
Physical processes
- Metal dissolution and fluoride-film formation compete
- Local film instability accelerates metal loss
Observable damage
Thinning; scale; isolated highly corroded components
Possible failure mode
Leak or rupture
- Other names
- HF corrosion
- Industries / exposed sectors
- Refinery alkylation; fluorochemical processing
- Typically affected parts
- HF-alkylation piping, including elbows
- Susceptible materials
- Carbon-steel components; residual copper/nickel chemistry matters
- Required chemicals / environment
- HF-containing service; water and contaminants change severity
- Influencing parameters
- Component composition and actual HF-service conditions
- Physical explanation (1–3 processes)
- Metal dissolution and fluoride-film formation compete
- Local film instability accelerates metal loss
- Signs and symptoms
- Thinning; scale; isolated highly corroded components
- Prevention / slowing the damage
- Strict chemistry/material control; component-level inspection; engineered containment and isolation
- Typical failure outcome
- Leak or rupture
- Possible consequences
- Highly toxic release; fire if hydrocarbons are present
- Can be mistaken for
- HCl corrosion; localized erosion; weld-related attack
- How to distinguish it
- Verify HF duty, water history and component chemistry; thickness-map individual fittings
- How often is it seen?
- No representative subtype-specific incidence was identified in the reviewed sources. This is a data gap, not evidence of rarity.
- Historical case / verification status
- Philadelphia Energy Solutions, 21 June 2019: a severely corroded HF-service elbow ruptured, causing explosions/fire and an HF release. CSB linked accelerated corrosion to component chemistry.
Photographs — 5 needed (real-life, not diagrams)
Macro / field view
Close-up or micrograph
Cross-section
In-service failure
Distinguishing feature
Sources
- 80 US Chemical Safety Board (2022) — Final report into 2019 PES fire and explosion in Philadelphia — Primary accident investigation (accessed 2026-09-08)
- 50 Haynes International — Corrosive Environments — Manufacturer technical guide (accessed 2026-09-08)
Educational synthesis, not a diagnosis or repair instruction. Confirm the actual alloy, environment, loading and damage before selecting mitigation. Generic signs are not unique proof of a mechanism.
DM-023Phosphoric acid corrosionProcess-specific aqueous corrosion · Mineral-acid corrosion
Mechanism pathway
Service conditions
Aqueous phosphoric acid with process-dependent sulfate, metal-ion, fluoride and chloride impurities
Physical processes
- Acid dissolution attacks insufficiently resistant alloys
- Impurities can destabilize passive films
Observable damage
General loss; pits or preferential weld attack
Possible failure mode
Leak or rupture
- Other names
- H3PO4 attack
- Industries / exposed sectors
- Fertilizer; phosphates; chemical processing
- Typically affected parts
- Fertilizer-grade phosphoric-acid evaporator tubing and related process equipment
- Susceptible materials
- Steels; stainless and nickel alloys depending on purity
- Required chemicals / environment
- Aqueous phosphoric acid with process-dependent sulfate, metal-ion, fluoride and chloride impurities
- Influencing parameters
- Acid concentration, temperature, impurity content and deposits
- Physical explanation (1–3 processes)
- Acid dissolution attacks insufficiently resistant alloys
- Impurities can destabilize passive films
- Signs and symptoms
- General loss; pits or preferential weld attack
- Prevention / slowing the damage
- Select against actual wet-process acid, not reagent-acid data alone; control impurities and flow
- Typical failure outcome
- Leak or rupture
- Possible consequences
- Acid/slurry release; production loss
- Can be mistaken for
- Slurry erosion; HCl/HF corrosion
- How to distinguish it
- Analyse acid impurities and solids; compare shielded and impinged areas; inspect weld/base metal
- How often is it seen?
- No representative subtype-specific incidence was identified in the reviewed sources. This is a data gap, not evidence of rarity.
- Historical case / verification status
- No mechanism-attributed catastrophe was verified in the sources reviewed; this does not mean none has occurred.
Photographs — 5 needed (real-life, not diagrams)
Macro / field view
Close-up or micrograph
Cross-section
In-service failure
Distinguishing feature
Sources
- 80 Lizlovs, E.A. (1969). Corrosion Behavior of Types 304 and 316 Stainless Steels in Hot 85% Phosphoric Acid. CORROSION 25(9), 389–393. — Primary research abstract (accessed 2026-09-08)
- 50 Haynes International — HASTELLOY G-35 alloy — Primary manufacturer test data (accessed 2026-09-08)
Educational synthesis, not a diagnosis or repair instruction. Confirm the actual alloy, environment, loading and damage before selecting mitigation. Generic signs are not unique proof of a mechanism.
DM-024Caustic corrosionProcess-specific aqueous corrosion · Concentrated-alkali corrosion
Mechanism pathway
Service conditions
Locally concentrated sodium hydroxide in boiler water
Physical processes
- Concentrated caustic dissolves protective magnetite, exposing steel to continued metal loss
Observable damage
Irregular gouges or thinning
Possible failure mode
Tube leak or rupture
- Other names
- Caustic gouging; alkaline metal loss
- Industries / exposed sectors
- Boilers; refining; chemical; pulp
- Typically affected parts
- Boiler tubes under deposits; caustic piping; evaporators
- Susceptible materials
- Carbon/low-alloy steels; susceptible stainless alloys
- Required chemicals / environment
- Locally concentrated sodium hydroxide in boiler water
- Influencing parameters
- Local concentration; temperature; deposits; heat flux; dryout
- Physical explanation (1–3 processes)
- Concentrated caustic dissolves protective magnetite, exposing steel to continued metal loss
- Signs and symptoms
- Irregular gouges or thinning
- Prevention / slowing the damage
- Prevent caustic concentration/dryout; control deposits and chemistry; suitable materials
- Typical failure outcome
- Tube leak or rupture
- Possible consequences
- Hot fluid release; outage
- Can be mistaken for
- Caustic SCC; acid phosphate corrosion; FAC
- How to distinguish it
- Metallography distinguishes wall loss from stress-driven cracks; analyse deposit chemistry and heat-flux pattern
- How often is it seen?
- No representative subtype-specific incidence was identified in the reviewed sources. This is a data gap, not evidence of rarity.
- Historical case / verification status
- No mechanism-attributed catastrophe was verified in the sources reviewed; this does not mean none has occurred.
Photographs — 5 needed (real-life, not diagrams)
Macro / field view
Close-up or micrograph
Cross-section
In-service failure
Distinguishing feature
Sources
- 50 Veolia Water Technologies — Water Handbook, chapter 11: Preboiler and Boiler Corrosion Control — Manufacturer technical handbook (accessed 2026-09-08)
- 50 Veolia Water Technologies — Water Handbook, chapter 14: Boiler System Failures — Manufacturer technical handbook (accessed 2026-09-08)
Educational synthesis, not a diagnosis or repair instruction. Confirm the actual alloy, environment, loading and damage before selecting mitigation. Generic signs are not unique proof of a mechanism.
DM-025Amine-unit corrosionProcess-specific aqueous corrosion · Solvent-system corrosion
Mechanism pathway
Service conditions
Aqueous amine with acid gases/degradation products; heat-stable salts can aggravate
Physical processes
- Heat-stable salts can increase solution corrosiveness; the effect depends on salt identity and concentration
Observable damage
Metal loss; morphology must be confirmed for the actual solvent
Possible failure mode
Leak or equipment rupture
- Other names
- Amine corrosion; acid-gas treating corrosion
- Industries / exposed sectors
- Gas sweetening; refining; carbon capture
- Typically affected parts
- Regenerators; reboilers; rich-amine lines; exchangers
- Susceptible materials
- Carbon steel and304 stainless steel in the verified MEA study; alloy response is chemistry-dependent
- Required chemicals / environment
- Aqueous amine with acid gases/degradation products; heat-stable salts can aggravate
- Influencing parameters
- Temperature and acid-gas composition; solvent and heat-stable-salt composition
- Physical explanation (1–3 processes)
- Heat-stable salts can increase solution corrosiveness; the effect depends on salt identity and concentration
- Signs and symptoms
- Metal loss; morphology must be confirmed for the actual solvent
- Prevention / slowing the damage
- Control solvent quality and heat-stable salts; oxygen exclusion where appropriate; flow and material review
- Typical failure outcome
- Leak or equipment rupture
- Possible consequences
- Toxic/flammable release; solvent contamination
- Can be mistaken for
- Amine SCC; wet H2S corrosion; CO2 corrosion
- How to distinguish it
- Analyse solvent, gas loading and salts; distinguish cracks from metal loss
- How often is it seen?
- No representative subtype-specific incidence was identified in the reviewed sources. This is a data gap, not evidence of rarity.
- Historical case / verification status
- No mechanism-attributed catastrophe was verified in the sources reviewed; this does not mean none has occurred.
Photographs — 5 needed (real-life, not diagrams)
Macro / field view
Close-up or micrograph
Cross-section
In-service failure
Distinguishing feature
Sources
- 80 Tanthapanichakoon, W., Veawab, A. & McGarvey, B. (2006). Electrochemical Investigation on the Effect of Heat-stable Salts on Corrosion in CO2 Capture Plants Using Aqueous Solution of MEA. Industrial & Engineering Chemistry Research 45(8), 2586–2593. — Primary experimental paper (accessed 2026-09-08)
- 80 Javidi, Ghassemi & Lalehparvar (2017). Amine corrosion and cracking of API 5L X52 in diethanolamine service. Corrosion Engineering, Science and Technology 52(7). — Primary investigation (accessed 2026-09-08)
Educational synthesis, not a diagnosis or repair instruction. Confirm the actual alloy, environment, loading and damage before selecting mitigation. Generic signs are not unique proof of a mechanism.
DM-026Ammonium bisulfide corrosionProcess-specific aqueous corrosion · Sour-water salt corrosion
Mechanism pathway
Service conditions
Water containing ammonia and hydrogen sulfide/bisulfide species
Physical processes
- Electrochemical iron loss accompanies formation of sulfide-containing corrosion products
Observable damage
Rapid thinning; localized grooves; sulfide products
Possible failure mode
Leak or rupture
- Other names
- NH4HS corrosion; ammonium hydrosulfide corrosion
- Industries / exposed sectors
- Hydroprocessing; refining; sour-water stripping
- Typically affected parts
- Sour-water ammonia-rectifier heat-exchanger nozzle in the verified case
- Susceptible materials
- Carbon steel in the verified nozzle investigation
- Required chemicals / environment
- Water containing ammonia and hydrogen sulfide/bisulfide species
- Influencing parameters
- Salt concentration; temperature; turbulence; velocity; wash-water distribution
- Physical explanation (1–3 processes)
- Electrochemical iron loss accompanies formation of sulfide-containing corrosion products
- Signs and symptoms
- Rapid thinning; localized grooves; sulfide products
- Prevention / slowing the damage
- Engineered water-wash distribution; concentration/flow control; appropriate materials and thickness mapping
- Typical failure outcome
- Leak or rupture
- Possible consequences
- Toxic/flammable release; exchanger outage
- Can be mistaken for
- Wet H2S corrosion; erosion-corrosion; NH4Cl attack
- How to distinguish it
- Analyse NH4HS-related chemistry, products and flow locations; check for concurrent HIC
- How often is it seen?
- No representative subtype-specific incidence was identified in the reviewed sources. This is a data gap, not evidence of rarity.
- Historical case / verification status
- Published 2026 refinery case: metallurgical/electrochemical investigation attributed sour-water exchanger damage to NH4HS-related corrosion. A fatal/offsite catastrophe was not established in that paper.
Photographs — 5 needed (real-life, not diagrams)
Macro / field view
Close-up or micrograph
Cross-section
In-service failure
Distinguishing feature
Sources
- 80 Al-Mazeedi, H.A., Al-Farhan, A., Tanoli, N. & Abraham, L. (2019). A Study of Galvanic Corrosion in Stagnant Ammonium Bisulfide Solution. International Journal of Corrosion, 1325169, 9 pages. — Primary experimental paper (accessed 2026-09-08)
- 80 Nicacio, J.A.P., de Freitas Cunha Lins, V. & de Arruda Santos, L. (2026). Failure Analysis of a Heat Exchanger in the Sour Water Unit of an Oil Refinery due to Ammonium Bisulfide Corrosion. Journal of Failure Analysis and Prevention 26, 559–570. — Primary failure investigation (accessed 2026-09-08)
Educational synthesis, not a diagnosis or repair instruction. Confirm the actual alloy, environment, loading and damage before selecting mitigation. Generic signs are not unique proof of a mechanism.
DM-027Ammonium chloride corrosionProcess-specific aqueous corrosion · Hygroscopic-salt corrosion
Mechanism pathway
Service conditions
Solid ammonium chloride deposits that absorb environmental moisture
Physical processes
- Hygroscopic salt wetting establishes a concentrated corrosive environment
Observable damage
Localized thinning beneath salt; pits; plugging
Possible failure mode
Leak or rupture
- Other names
- NH4Cl salt corrosion
- Industries / exposed sectors
- Refining; hydroprocessing
- Typically affected parts
- Hydroprocessing reactor-effluent equipment exposed to NH4Cl deposits
- Susceptible materials
- Carbon steel and susceptible stainless/alloy materials; response differs by material
- Required chemicals / environment
- Solid ammonium chloride deposits that absorb environmental moisture
- Influencing parameters
- Relative humidity, temperature and alloy
- Physical explanation (1–3 processes)
- Hygroscopic salt wetting establishes a concentrated corrosive environment
- Signs and symptoms
- Localized thinning beneath salt; pits; plugging
- Prevention / slowing the damage
- Limit salt precursors; engineered water washing; avoid dry salt accumulation; inspect deposition zones
- Typical failure outcome
- Leak or rupture
- Possible consequences
- Toxic/flammable release; blockage
- Can be mistaken for
- HCl dewpoint corrosion; NH4HS corrosion
- How to distinguish it
- Identify chloride-rich salt and wetting conditions; distinguish first-condensate attack from hygroscopic salt wetting
- How often is it seen?
- No representative subtype-specific incidence was identified in the reviewed sources. This is a data gap, not evidence of rarity.
- Historical case / verification status
- No mechanism-attributed catastrophe was verified in the sources reviewed; this does not mean none has occurred.
Photographs — 5 needed (real-life, not diagrams)
Macro / field view
Close-up or micrograph
Cross-section
In-service failure
Distinguishing feature
Sources
- 80 Toba, K., Suzuki, T., Kawano, K. & Sakai, J. (2011). Effect of Relative Humidity on Ammonium Chloride Corrosion in Refineries. CORROSION. — Primary experimental paper (accessed 2026-09-08)
- 80 TWI — Corrosion in Petrochemical and Refinery Industries (27 June 2022) — Technical reference (accessed 2026-09-08)
Educational synthesis, not a diagnosis or repair instruction. Confirm the actual alloy, environment, loading and damage before selecting mitigation. Generic signs are not unique proof of a mechanism.
DM-028Flue-gas acid-dewpoint corrosionProcess-specific aqueous corrosion · Condensate corrosion
Mechanism pathway
Service conditions
Sulfur oxides and water in sulfur-bearing-fuel combustion gas
Physical processes
- Acid condenses on sufficiently cold surfaces
- Liquid acid consumes exposed metal
Observable damage
Cold-end thinning; rust/acid deposits; perforation
Possible failure mode
Perforation; duct leakage or collapse
- Other names
- Cold-end corrosion; sulfuric-acid dewpoint corrosion
- Industries / exposed sectors
- Power; boilers; furnaces; incineration
- Typically affected parts
- Air heaters; economizers; ducts; stacks
- Susceptible materials
- Carbon/low-alloy steels; unsuitable linings/alloys
- Required chemicals / environment
- Sulfur oxides and water in sulfur-bearing-fuel combustion gas
- Influencing parameters
- Metal temperature relative to actual acid dewpoint; fuel chemistry; deposits
- Physical explanation (1–3 processes)
- Acid condenses on sufficiently cold surfaces
- Liquid acid consumes exposed metal
- Signs and symptoms
- Cold-end thinning; rust/acid deposits; perforation
- Prevention / slowing the damage
- Control cold spots and combustion chemistry; suitable coatings/materials; drainage
- Typical failure outcome
- Perforation; duct leakage or collapse
- Possible consequences
- Flue-gas escape; efficiency loss; outage
- Can be mistaken for
- Atmospheric corrosion; high-temperature hot corrosion
- How to distinguish it
- Compare surface temperature with measured/composition-based acid dew point and examine acidic condensate
- How often is it seen?
- No representative subtype-specific incidence was identified in the reviewed sources. This is a data gap, not evidence of rarity.
- Historical case / verification status
- No mechanism-attributed catastrophe was verified in the sources reviewed; this does not mean none has occurred.
Photographs — 5 needed (real-life, not diagrams)
Macro / field view
Close-up or micrograph
Cross-section
In-service failure
Distinguishing feature
Sources
- 50 Veolia Water Technologies — Water Handbook, chapter 22: Cold-End Deposition and Corrosion Control — Manufacturer technical handbook (accessed 2026-09-08)
- 50 Haynes International — Corrosive Environments — Manufacturer technical guide (accessed 2026-09-08)
Educational synthesis, not a diagnosis or repair instruction. Confirm the actual alloy, environment, loading and damage before selecting mitigation. Generic signs are not unique proof of a mechanism.
DM-029Oxygen pitting in boiler/feedwater systemsProcess-specific aqueous corrosion · Oxidant-driven localized corrosion
Mechanism pathway
Service conditions
Dissolved oxygen in water
Physical processes
- Cathodic oxygen reduction supports anodic iron dissolution
Observable damage
Localized pits, sometimes beneath oxide caps
Possible failure mode
Tube or pipe leak
- Other names
- Dissolved-oxygen attack; oxygen corrosion
- Industries / exposed sectors
- Power; industrial steam; district heating
- Typically affected parts
- Feedwater lines, economizers and boiler tubes
- Susceptible materials
- Carbon/low-alloy steels
- Required chemicals / environment
- Dissolved oxygen in water
- Influencing parameters
- Oxygen ingress; stagnation; temperature; pH; deposits
- Physical explanation (1–3 processes)
- Cathodic oxygen reduction supports anodic iron dissolution
- Signs and symptoms
- Localized pits, sometimes beneath oxide caps
- Prevention / slowing the damage
- Control unintended oxygen ingress and use a plant-specific operating and layup programme
- Typical failure outcome
- Tube or pipe leak
- Possible consequences
- Steam/water release; shutdown
- Can be mistaken for
- MIC; chloride pitting; under-deposit corrosion
- How to distinguish it
- Correlate oxygen/layup records, pit/deposit chemistry and biological evidence; tubercles alone do not establish MIC
- How often is it seen?
- No representative subtype-specific incidence was identified in the reviewed sources. This is a data gap, not evidence of rarity.
- Historical case / verification status
- No mechanism-attributed catastrophe was verified in the sources reviewed; this does not mean none has occurred.
Photographs — 5 needed (real-life, not diagrams)
Macro / field view
Close-up or micrograph
Cross-section
In-service failure
Distinguishing feature
Sources
- 50 Veolia Water Technologies — Water Handbook, chapter 11: Preboiler and Boiler Corrosion Control — Manufacturer technical handbook (accessed 2026-09-08)
- 50 Veolia Water Technologies — Water Handbook, chapter 14: Boiler System Failures — Manufacturer technical handbook (accessed 2026-09-08)
Educational synthesis, not a diagnosis or repair instruction. Confirm the actual alloy, environment, loading and damage before selecting mitigation. Generic signs are not unique proof of a mechanism.
DM-030Acid phosphate corrosionProcess-specific aqueous corrosion · Deposit-related boiler corrosion
Mechanism pathway
Service conditions
Locally concentrated acidic phosphate beneath deposits
Physical processes
- Deposits and local phosphate chemistry dissolve the protective magnetite layer
Observable damage
Gouging under adherent deposits; maricite may identify the reaction products
Possible failure mode
Tube leakage or rupture
- Other names
- APC; acid-phosphate boiler-tube attack
- Industries / exposed sectors
- Power; industrial boilers
- Typically affected parts
- Deposited boiler waterwalls and HRSG evaporator tubes
- Susceptible materials
- Carbon and low-alloy boiler steels
- Required chemicals / environment
- Locally concentrated acidic phosphate beneath deposits
- Influencing parameters
- Phosphate treatment history; local Na:P balance; hideout; heat flux
- Physical explanation (1–3 processes)
- Deposits and local phosphate chemistry dissolve the protective magnetite layer
- Signs and symptoms
- Gouging under adherent deposits; maricite may identify the reaction products
- Prevention / slowing the damage
- Qualified boiler chemistry programme; avoid inappropriate phosphate dosing; manage deposits
- Typical failure outcome
- Tube leakage or rupture
- Possible consequences
- Forced outage; hot-fluid release
- Can be mistaken for
- Caustic gouging; oxygen pitting; boiler hydrogen damage
- How to distinguish it
- Preserve deposits for phase analysis and compare treatment/hideout history; phosphate hideout alone is insufficient
- How often is it seen?
- No representative subtype-specific incidence was identified in the reviewed sources. This is a data gap, not evidence of rarity.
- Historical case / verification status
- No mechanism-attributed catastrophe was verified in the sources reviewed; this does not mean none has occurred.
Photographs — 5 needed (real-life, not diagrams)
Macro / field view
Close-up or micrograph
Cross-section
In-service failure
Distinguishing feature
Sources
- 80 Dooley, B. & McNaughton, W. (EPRI, 1997). Don’t let those boiler tubes fail again. Power Engineering. — Primary institutional authors’ technical article (accessed 2026-09-08)
- 50 Veolia Water Technologies — Water Handbook, chapter 14: Boiler System Failures — Manufacturer technical handbook (accessed 2026-09-08)
- 80 Dooley, R.B. and Bursik, A. (2010). Acid Phosphate Corrosion. PowerPlant Chemistry 12(6), 368–372. — public_full_text (accessed 2026-09-08)
Educational synthesis, not a diagnosis or repair instruction. Confirm the actual alloy, environment, loading and damage before selecting mitigation. Generic signs are not unique proof of a mechanism.
DM-031Chloride stress corrosion crackingEnvironment-assisted cracking & hydrogen · Anodic environment-assisted cracking
Mechanism pathway
Service conditions
Chloride-bearing moisture plus tensile stress and a susceptible microstructure
Physical processes
- Film rupture and localized dissolution assist crack initiation/growth
- Crack-tip chemistry and deformation sustain environmentally assisted propagation
Observable damage
Often branched transgranular cracks; small leaks; little general corrosion
Possible failure mode
Leak or brittle-appearing rupture
- Other names
- Chloride SCC; Cl-SCC
- Industries / exposed sectors
- Chemical; refining; marine; power
- Typically affected parts
- Hot stainless piping; exchangers; insulated surfaces
- Susceptible materials
- Susceptible austenitic stainless steels; susceptibility varies by alloy
- Required chemicals / environment
- Chloride-bearing moisture plus tensile stress and a susceptible microstructure
- Influencing parameters
- Temperature; chloride concentration; potential; evaporation; residual stress
- Physical explanation (1–3 processes)
- Film rupture and localized dissolution assist crack initiation/growth
- Crack-tip chemistry and deformation sustain environmentally assisted propagation
- Signs and symptoms
- Often branched transgranular cracks; small leaks; little general corrosion
- Prevention / slowing the damage
- Prevent chloride concentration; resistant materials; stress reduction where qualified; inspect cracking-prone locations
- Typical failure outcome
- Leak or brittle-appearing rupture
- Possible consequences
- Unexpected containment loss
- Can be mistaken for
- Thermal fatigue; other SCC; intergranular corrosion
- How to distinguish it
- Combine crack-path metallography, chloride evidence and tensile-stress history; branching alone is not proof
- How often is it seen?
- No representative subtype-specific incidence was identified in the reviewed sources. This is a data gap, not evidence of rarity.
- Historical case / verification status
- No mechanism-attributed catastrophe was verified in the sources reviewed; this does not mean none has occurred.
Photographs — 5 needed (real-life, not diagrams)
Macro / field view
Close-up or micrograph
Cross-section
In-service failure
Distinguishing feature
Sources
- 80 TWI — Stress Corrosion Cracking Testing — Technical reference (accessed 2026-09-08)
- 80 ASTM G48-25 — Pitting and Crevice Corrosion Resistance of Stainless Steels and Related Alloys by Use of Ferric Chloride Solution — Official public standard scope (accessed 2026-09-08)
- 80 Begg, H. — Evaluation of a New Corrosion Under Insulation Test Method. TWI Report Summary 1097/2018. — Primary research summary (accessed 2026-09-08)
Educational synthesis, not a diagnosis or repair instruction. Confirm the actual alloy, environment, loading and damage before selecting mitigation. Generic signs are not unique proof of a mechanism.
DM-032Caustic stress corrosion crackingEnvironment-assisted cracking & hydrogen · Alkaline environment-assisted cracking
Mechanism pathway
Service conditions
Concentrated hydroxide plus tensile stress
Physical processes
- Stress-assisted passive-film breakdown promotes localized cracking
- Preferential grain-boundary attack can support propagation
Observable damage
Frequently intergranular, branched cracks near stressed regions
Possible failure mode
Leak or sudden rupture
- Other names
- Caustic SCC; caustic embrittlement
- Industries / exposed sectors
- Refining; boilers; chemical; pulp
- Typically affected parts
- Welds; concentrated-caustic piping; vessels
- Susceptible materials
- Carbon/low-alloy steel; susceptible stainless and nickel alloys
- Required chemicals / environment
- Concentrated hydroxide plus tensile stress
- Influencing parameters
- Temperature; caustic concentration; stress; deposits; alloy condition
- Physical explanation (1–3 processes)
- Stress-assisted passive-film breakdown promotes localized cracking
- Preferential grain-boundary attack can support propagation
- Signs and symptoms
- Frequently intergranular, branched cracks near stressed regions
- Prevention / slowing the damage
- Control concentration and temperature; suitable alloy; qualified stress relief; avoid deposits/dryout
- Typical failure outcome
- Leak or sudden rupture
- Possible consequences
- Hot caustic exposure; outage
- Can be mistaken for
- Caustic gouging; weld H cracking; carbonate SCC
- How to distinguish it
- Cracks rather than gouges; confirm caustic chemistry and stress/thermal history; section weld and HAZ
- How often is it seen?
- No representative subtype-specific incidence was identified in the reviewed sources. This is a data gap, not evidence of rarity.
- Historical case / verification status
- No mechanism-attributed catastrophe was verified in the sources reviewed; this does not mean none has occurred.
Photographs — 5 needed (real-life, not diagrams)
Macro / field view
Close-up or micrograph
Cross-section
In-service failure
Distinguishing feature
Sources
- 80 TWI — Stress Corrosion Cracking Testing — Technical reference (accessed 2026-09-08)
- 50 Veolia Water Technologies — Water Handbook, chapter 11: Preboiler and Boiler Corrosion Control — Manufacturer technical handbook (accessed 2026-09-08)
Educational synthesis, not a diagnosis or repair instruction. Confirm the actual alloy, environment, loading and damage before selecting mitigation. Generic signs are not unique proof of a mechanism.
DM-033Ammonia stress corrosion cracking of copper alloysEnvironment-assisted cracking & hydrogen · Ammoniacal environment-assisted cracking
Mechanism pathway
Service conditions
Ammoniacal moisture; oxygen/oxidizing conditions commonly participate
Physical processes
- Ammonia-containing chemistry destabilizes stressed surface regions
- Localized dissolution and film rupture support crack growth
Observable damage
Intergranular or transgranular cracks; tarnish may occur
Possible failure mode
Fitting fracture or tube leak
- Other names
- Season cracking; ammonia SCC of brass
- Industries / exposed sectors
- Refrigeration surroundings; marine; chemical; storage
- Typically affected parts
- Brass fittings; tubes; stressed fasteners
- Susceptible materials
- Susceptible brasses and other copper alloys; not all Cu-Ni equally susceptible
- Required chemicals / environment
- Ammoniacal moisture; oxygen/oxidizing conditions commonly participate
- Influencing parameters
- Residual stress; alloy composition; ammonia activity; pH; temperature
- Physical explanation (1–3 processes)
- Ammonia-containing chemistry destabilizes stressed surface regions
- Localized dissolution and film rupture support crack growth
- Signs and symptoms
- Intergranular or transgranular cracks; tarnish may occur
- Prevention / slowing the damage
- Exclude ammoniacal contamination; reduce residual stress; qualified resistant materials
- Typical failure outcome
- Fitting fracture or tube leak
- Possible consequences
- Loss of containment; component separation
- Can be mistaken for
- Dezincification; fatigue; general ammoniacal corrosion
- How to distinguish it
- Use metallography and zinc mapping; prove ammonia exposure and stress; accelerated tests rank susceptibility, not life
- How often is it seen?
- No representative subtype-specific incidence was identified in the reviewed sources. This is a data gap, not evidence of rarity.
- Historical case / verification status
- No mechanism-attributed catastrophe was verified in the sources reviewed; this does not mean none has occurred.
Photographs — 5 needed (real-life, not diagrams)
Macro / field view
Close-up or micrograph
Cross-section
In-service failure
Distinguishing feature
Sources
- 80 ASTM G37-98(2021) — Use of Mattsson’s Solution of pH 7.2 to Evaluate the Stress-Corrosion Cracking Susceptibility of Copper-Zinc Alloys — Official public standard scope (accessed 2026-09-08)
- 70 Copper Development Association — Copper-nickel: corrosion resistance and antifouling — Technical reference (accessed 2026-09-08)
Educational synthesis, not a diagnosis or repair instruction. Confirm the actual alloy, environment, loading and damage before selecting mitigation. Generic signs are not unique proof of a mechanism.
DM-034Carbonate stress corrosion crackingEnvironment-assisted cracking & hydrogen · Alkaline environment-assisted cracking
Mechanism pathway
Service conditions
Aqueous carbonate/bicarbonate chemistry plus tensile stress
Physical processes
- Active/passive electrochemistry enables stress-assisted localized dissolution
Observable damage
Often intergranular branched cracks near stressed weld regions
Possible failure mode
Leak or rupture
- Other names
- Carbonate SCC; carbonate/bicarbonate cracking
- Industries / exposed sectors
- Refining; CO2-removal/chemical plants
- Typically affected parts
- Carbonate-solvent equipment; wet process piping; welds
- Susceptible materials
- Carbon steel
- Required chemicals / environment
- Aqueous carbonate/bicarbonate chemistry plus tensile stress
- Influencing parameters
- pH; potential; temperature; carbonate concentration; weld stress
- Physical explanation (1–3 processes)
- Active/passive electrochemistry enables stress-assisted localized dissolution
- Signs and symptoms
- Often intergranular branched cracks near stressed weld regions
- Prevention / slowing the damage
- Control the actual solvent/process chemistry; qualified stress relief and inspection
- Typical failure outcome
- Leak or rupture
- Possible consequences
- Process release; outage
- Can be mistaken for
- Caustic SCC; amine SCC; high-pH pipeline SCC
- How to distinguish it
- Establish service chemistry and potential; compare crack path with weld condition; do not infer carbonate solely from deposits
- How often is it seen?
- No representative subtype-specific incidence was identified in the reviewed sources. This is a data gap, not evidence of rarity.
- Historical case / verification status
- No mechanism-attributed catastrophe was verified in the sources reviewed; this does not mean none has occurred.
Photographs — 5 needed (real-life, not diagrams)
Macro / field view
Close-up or micrograph
Cross-section
In-service failure
Distinguishing feature
Sources
- 80 Schutt, H.U. (1992). Corrosion Inhibition Alternatives in Carbonate Solvent Based Carbon Dioxide Removal Systems. NACE paper 92455, 1–9. — Primary technical paper (accessed 2026-09-08)
- 80 TWI — Stress Corrosion Cracking Testing — Technical reference (accessed 2026-09-08)
Educational synthesis, not a diagnosis or repair instruction. Confirm the actual alloy, environment, loading and damage before selecting mitigation. Generic signs are not unique proof of a mechanism.
DM-035Polythionic acid stress corrosion crackingEnvironment-assisted cracking & hydrogen · Shutdown-related intergranular SCC
Mechanism pathway
Service conditions
Sulfide scales exposed to moisture and oxygen; tensile stress
Physical processes
- Sulfide scales react during wet air exposure
- Acidic sulfur species attack chromium-depleted boundaries under tensile stress
Observable damage
Intergranular cracking, commonly discovered during/after shutdown
Possible failure mode
Leak or rupture on restart
- Other names
- PASCC; polythionic SCC
- Industries / exposed sectors
- Refining; petrochemical; sulfur-bearing high-temperature service
- Typically affected parts
- Sensitized stainless furnace tubes; piping; weld HAZ
- Susceptible materials
- Sensitized austenitic stainless and susceptible nickel alloys
- Required chemicals / environment
- Sulfide scales exposed to moisture and oxygen; tensile stress
- Influencing parameters
- Shutdown wetting; sensitization; air entry; sulfur scale
- Physical explanation (1–3 processes)
- Sulfide scales react during wet air exposure
- Acidic sulfur species attack chromium-depleted boundaries under tensile stress
- Signs and symptoms
- Intergranular cracking, commonly discovered during/after shutdown
- Prevention / slowing the damage
- Qualified shutdown protection; exclude moist oxygen; avoid sensitization; approved neutralization procedures
- Typical failure outcome
- Leak or rupture on restart
- Possible consequences
- Hydrocarbon release; fire; outage
- Can be mistaken for
- IGC; chloride SCC; high-temperature cracking
- How to distinguish it
- Demonstrate sensitization, sulfur scale and wet shutdown exposure; section grain-boundary cracks
- How often is it seen?
- No representative subtype-specific incidence was identified in the reviewed sources. This is a data gap, not evidence of rarity.
- Historical case / verification status
- No mechanism-attributed catastrophe was verified in the sources reviewed; this does not mean none has occurred.
Photographs — 5 needed (real-life, not diagrams)
Macro / field view
Close-up or micrograph
Cross-section
In-service failure
Distinguishing feature
Sources
- 80 Shargay, C.A. (2017). Assessing Stress Corrosion Cracking Risks on Stainless Steel Piping and Equipment. CORROSION 2017, paper C2017-08899, pp. 1–22. — Primary technical paper (accessed 2026-09-08)
- 70 AMPP — Intergranular Corrosion — Technical reference (accessed 2026-09-08)
- 80 TWI — Embrittlement of austenitic steel welds at high temperature — Technical reference (accessed 2026-09-08)
Educational synthesis, not a diagnosis or repair instruction. Confirm the actual alloy, environment, loading and damage before selecting mitigation. Generic signs are not unique proof of a mechanism.
DM-036Near-neutral-pH pipeline stress corrosion crackingEnvironment-assisted cracking & hydrogen · External pipeline SCC
Mechanism pathway
Service conditions
Groundwater with dissolved CO2 beneath shielding coatings; tensile stress
Physical processes
- Environmental dissolution and hydrogen effects assist cracking
- Cyclic loading can accelerate transgranular crack growth
Observable damage
Axial crack colonies; often transgranular cracks with some corrosion
Possible failure mode
Leak or rupture
- Other names
- Low-pH pipeline SCC; near-neutral SCC
- Industries / exposed sectors
- Gas and liquid transmission
- Typically affected parts
- Pipe exterior beneath disbonded coatings
- Susceptible materials
- Carbon-steel linepipe
- Required chemicals / environment
- Groundwater with dissolved CO2 beneath shielding coatings; tensile stress
- Influencing parameters
- Pressure cycles; local pH; coating disbondment; hydrogen entry
- Physical explanation (1–3 processes)
- Environmental dissolution and hydrogen effects assist cracking
- Cyclic loading can accelerate transgranular crack growth
- Signs and symptoms
- Axial crack colonies; often transgranular cracks with some corrosion
- Prevention / slowing the damage
- Coating rehabilitation; pressure-cycle review; suitable SCC inspection and mitigation
- Typical failure outcome
- Leak or rupture
- Possible consequences
- Product release; possible fire/explosion
- Can be mistaken for
- High-pH SCC; corrosion fatigue; HIC
- How to distinguish it
- Combine external coating/soil evidence with crack path and chemistry; operating stress is essential context
- How often is it seen?
- No representative subtype-specific incidence was identified in the reviewed sources. This is a data gap, not evidence of rarity.
- Historical case / verification status
- No mechanism-attributed catastrophe was verified in the sources reviewed; this does not mean none has occurred.
Photographs — 5 needed (real-life, not diagrams)
Macro / field view
Close-up or micrograph
Cross-section
In-service failure
Distinguishing feature
Sources
- 80 PHMSA — Fact Sheet: Stress Corrosion Cracking — Regulatory technical reference (accessed 2026-09-08)
- 80 PHMSA — Pipeline Failure Causes (updated 20 April 2026) — Regulatory taxonomy (accessed 2026-09-08)
- 80 TWI — Hydrogen Embrittlement Testing — Technical reference (accessed 2026-09-08)
Educational synthesis, not a diagnosis or repair instruction. Confirm the actual alloy, environment, loading and damage before selecting mitigation. Generic signs are not unique proof of a mechanism.
DM-037High-pH pipeline stress corrosion crackingEnvironment-assisted cracking & hydrogen · External alkaline pipeline SCC
Mechanism pathway
Service conditions
Concentrated carbonate/bicarbonate electrolyte plus tensile stress
Physical processes
- Active/passive film rupture and dissolution support predominantly intergranular cracking
Observable damage
Axial crack colonies; intergranular paths in characteristic chemistry
Possible failure mode
Leak or rupture
- Other names
- Classical pipeline SCC
- Industries / exposed sectors
- Gas and liquid transmission
- Typically affected parts
- Pipe surfaces beneath disbonded coatings
- Susceptible materials
- Carbon-steel linepipe
- Required chemicals / environment
- Concentrated carbonate/bicarbonate electrolyte plus tensile stress
- Influencing parameters
- Temperature; potential; concentration; stress cycles; coating shielding
- Physical explanation (1–3 processes)
- Active/passive film rupture and dissolution support predominantly intergranular cracking
- Signs and symptoms
- Axial crack colonies; intergranular paths in characteristic chemistry
- Prevention / slowing the damage
- Coating/CP coordination; temperature and cycling review; validated crack detection
- Typical failure outcome
- Leak or rupture
- Possible consequences
- Loss of containment; potential fire
- Can be mistaken for
- Near-neutral SCC; carbonate SCC in process equipment; fatigue
- How to distinguish it
- Intergranular path plus external alkaline environment; do not use crack orientation alone
- How often is it seen?
- No representative subtype-specific incidence was identified in the reviewed sources. This is a data gap, not evidence of rarity.
- Historical case / verification status
- No mechanism-attributed catastrophe was verified in the sources reviewed; this does not mean none has occurred.
Photographs — 5 needed (real-life, not diagrams)
Macro / field view
Close-up or micrograph
Cross-section
In-service failure
Distinguishing feature
Sources
- 80 PHMSA — Fact Sheet: Stress Corrosion Cracking — Regulatory technical reference (accessed 2026-09-08)
- 80 Schutt, H.U. (1992). Corrosion Inhibition Alternatives in Carbonate Solvent Based Carbon Dioxide Removal Systems. NACE paper 92455, 1–9. — Primary technical paper (accessed 2026-09-08)
Educational synthesis, not a diagnosis or repair instruction. Confirm the actual alloy, environment, loading and damage before selecting mitigation. Generic signs are not unique proof of a mechanism.
DM-038Primary-water stress corrosion crackingEnvironment-assisted cracking & hydrogen · Nuclear primary-water SCC
Mechanism pathway
Service conditions
High-temperature primary water plus tensile stress
Physical processes
- Grain-boundary oxidation and crack-tip deformation interact under tensile loading
Observable damage
Often intergranular cracking; leakage products; limited external warning
Possible failure mode
Leak; possible pressure-boundary rupture
- Other names
- PWSCC
- Industries / exposed sectors
- Pressurized-water nuclear plants
- Typically affected parts
- Penetrations; nozzle welds; pressurizer heaters; steam-generator tubes
- Susceptible materials
- Susceptible nickel alloys, notably Alloy 600 and weld metals 82/182
- Required chemicals / environment
- High-temperature primary water plus tensile stress
- Influencing parameters
- Temperature; dissolved hydrogen/oxygen potential; cold work; microstructure
- Physical explanation (1–3 processes)
- Grain-boundary oxidation and crack-tip deformation interact under tensile loading
- Signs and symptoms
- Often intergranular cracking; leakage products; limited external warning
- Prevention / slowing the damage
- Resistant qualified alloys; stress mitigation; primary-water control; targeted volumetric inspection
- Typical failure outcome
- Leak; possible pressure-boundary rupture
- Possible consequences
- Unplanned outage; nuclear safety challenge
- Can be mistaken for
- Thermal fatigue; fabrication cracks; boric-acid metal loss
- How to distinguish it
- Identify alloy and primary-water exposure; metallography and crack-location evidence; inspect beyond surface staining
- How often is it seen?
- No representative subtype-specific incidence was identified in the reviewed sources. This is a data gap, not evidence of rarity.
- Historical case / verification status
- No mechanism-attributed catastrophe was verified in the sources reviewed; this does not mean none has occurred.
Photographs — 5 needed (real-life, not diagrams)
Macro / field view
Close-up or micrograph
Cross-section
In-service failure
Distinguishing feature
Sources
- 80 NRC — Pressurizer issues — Regulatory operating-experience reference (accessed 2026-09-08)
- 80 NRC — NUREG/CR-7276: Stress corrosion cracking of Alloy 690 and weld metals 52/152 (2023) — Primary institutional research abstract (accessed 2026-09-08)
Educational synthesis, not a diagnosis or repair instruction. Confirm the actual alloy, environment, loading and damage before selecting mitigation. Generic signs are not unique proof of a mechanism.
DM-039Hydrogen embrittlementEnvironment-assisted cracking & hydrogen · Hydrogen-assisted loss of ductility
Mechanism pathway
Service conditions
Absorbed hydrogen from corrosion, processing, CP or gaseous hydrogen
Physical processes
- Hydrogen-enhanced localized plasticity (HELP)
- Hydrogen-enhanced decohesion (HEDE)
- Other coupled mechanisms may contribute; no single model explains every alloy
Observable damage
Delayed brittle-appearing cracks; reduced ductility/toughness
Possible failure mode
Sudden fracture or leak
- Other names
- HE; hydrogen-assisted cracking; hydrogen stress cracking
- Industries / exposed sectors
- Fasteners; energy; plating; marine; hydrogen systems
- Typically affected parts
- High-strength bolts; springs; welds; pressure boundaries
- Susceptible materials
- High-strength steels; susceptible titanium, nickel and other alloys
- Required chemicals / environment
- Absorbed hydrogen from corrosion, processing, CP or gaseous hydrogen
- Influencing parameters
- Hydrogen availability; strength; tensile stress; trapping; temperature
- Physical explanation (1–3 processes)
- Hydrogen-enhanced localized plasticity (HELP)
- Hydrogen-enhanced decohesion (HEDE)
- Other coupled mechanisms may contribute; no single model explains every alloy
- Signs and symptoms
- Delayed brittle-appearing cracks; reduced ductility/toughness
- Prevention / slowing the damage
- Control hydrogen entry and strength; qualified processing/baking; avoid excessive CP; hydrogen-service testing
- Typical failure outcome
- Sudden fracture or leak
- Possible consequences
- Loss of load/containment; injury potential
- Can be mistaken for
- SSC; brittle cleavage; fatigue; HTHA
- How to distinguish it
- Exposure/processing history plus fractography and material testing; low measured hydrogen after delay does not exclude prior hydrogen
- How often is it seen?
- No representative subtype-specific incidence was identified in the reviewed sources. This is a data gap, not evidence of rarity.
- Historical case / verification status
- No mechanism-attributed catastrophe was verified in the sources reviewed; this does not mean none has occurred.
Photographs — 5 needed (real-life, not diagrams)
Macro / field view
Close-up or micrograph
Cross-section
In-service failure
Distinguishing feature
Sources
- 80 TWI — What is Hydrogen Embrittlement? Causes, Effects and Prevention — Technical reference (accessed 2026-09-08)
- 80 TWI — Hydrogen Embrittlement Testing — Technical reference (accessed 2026-09-08)
- 80 Woollin, P. & Murphy, W. (2001). Hydrogen Embrittlement Stress Corrosion Cracking of Superduplex Stainless Steel. CORROSION 2001, paper 01018. — Primary failure investigation (accessed 2026-09-08)
Educational synthesis, not a diagnosis or repair instruction. Confirm the actual alloy, environment, loading and damage before selecting mitigation. Generic signs are not unique proof of a mechanism.
DM-040Sulfide stress crackingEnvironment-assisted cracking & hydrogen · Wet-H2S hydrogen-assisted cracking
Mechanism pathway
Service conditions
Wet H2S plus tensile stress
Physical processes
- Sour corrosion promotes hydrogen entry
- Hydrogen-assisted fracture occurs in a stressed susceptible material
Observable damage
Brittle-appearing cracks; little warning; possible weld/HAZ concentration
Possible failure mode
Sudden break or leak
- Other names
- SSC; sulphide stress cracking
- Industries / exposed sectors
- Oil/gas; refining; sour service
- Typically affected parts
- Bolts; weld HAZ; tubing; valves; pressure equipment
- Susceptible materials
- Susceptible high-strength/hard steels; some other alloys
- Required chemicals / environment
- Wet H2S plus tensile stress
- Influencing parameters
- Hardness; microstructure; pH; H2S partial pressure; stress
- Physical explanation (1–3 processes)
- Sour corrosion promotes hydrogen entry
- Hydrogen-assisted fracture occurs in a stressed susceptible material
- Signs and symptoms
- Brittle-appearing cracks; little warning; possible weld/HAZ concentration
- Prevention / slowing the damage
- Qualified sour-service material and hardness; weld control; environment management
- Typical failure outcome
- Sudden break or leak
- Possible consequences
- Toxic/flammable release; loss of restraint
- Can be mistaken for
- HIC; SOHIC; weld hydrogen cracking
- How to distinguish it
- Assess hardness/stress and sour exposure; distinguish stress-driven cracks from rolling-plane HIC arrays
- How often is it seen?
- No representative subtype-specific incidence was identified in the reviewed sources. This is a data gap, not evidence of rarity.
- Historical case / verification status
- No mechanism-attributed catastrophe was verified in the sources reviewed; this does not mean none has occurred.
Photographs — 5 needed (real-life, not diagrams)
Macro / field view
Close-up or micrograph
Cross-section
In-service failure
Distinguishing feature
Sources
- 80 TWI — A review of the effect of cold-work on resistance to sulphide stress cracking (March 2007) — Technical research paper (accessed 2026-09-08)
- 80 TWI — Sour Testing — Technical reference (accessed 2026-09-08)
- 80 TWI — What is Hydrogen Embrittlement? Causes, Effects and Prevention — Technical reference (accessed 2026-09-08)
Educational synthesis, not a diagnosis or repair instruction. Confirm the actual alloy, environment, loading and damage before selecting mitigation. Generic signs are not unique proof of a mechanism.
DM-041Hydrogen-induced crackingEnvironment-assisted cracking & hydrogen · Internal hydrogen damage
Mechanism pathway
Service conditions
Hydrogen charging, commonly wet H2S
Physical processes
- Hydrogen accumulates at internal traps and recombines
- Internal pressure creates planar cracks which can link stepwise
Observable damage
Internal laminarlike cracks parallel to rolling; possible blistering
Possible failure mode
Leak or rupture after linked cracking
- Other names
- HIC; stepwise cracking
- Industries / exposed sectors
- Sour oil/gas; refining
- Typically affected parts
- Linepipe walls; vessel plates; wet sour-service equipment
- Susceptible materials
- Susceptible rolled carbon/low-alloy steel with traps/inclusions
- Required chemicals / environment
- Hydrogen charging, commonly wet H2S
- Influencing parameters
- Steel cleanliness; trapping sites; pH; charging severity
- Physical explanation (1–3 processes)
- Hydrogen accumulates at internal traps and recombines
- Internal pressure creates planar cracks which can link stepwise
- Signs and symptoms
- Internal laminarlike cracks parallel to rolling; possible blistering
- Prevention / slowing the damage
- HIC-resistant clean steel; appropriate sour-service control; qualified testing and UT
- Typical failure outcome
- Leak or rupture after linked cracking
- Possible consequences
- Loss of containment; reduced pressure capacity
- Can be mistaken for
- Laminations; SOHIC; lamellar tearing
- How to distinguish it
- Section cracks and inclusions; establish charging history; applied tensile stress is not required for HIC initiation
- How often is it seen?
- No representative subtype-specific incidence was identified in the reviewed sources. This is a data gap, not evidence of rarity.
- Historical case / verification status
- No mechanism-attributed catastrophe was verified in the sources reviewed; this does not mean none has occurred.
Photographs — 5 needed (real-life, not diagrams)
Macro / field view
Close-up or micrograph
Cross-section
In-service failure
Distinguishing feature
Sources
- 80 Pargeter, R.J. (2007). Susceptibility to SOHIC for Linepipe and Pressure Vessel Steels: Review of Current Knowledge. NACE 2007. — Technical research paper (accessed 2026-09-08)
- 80 TWI — Sour Testing — Technical reference (accessed 2026-09-08)
Educational synthesis, not a diagnosis or repair instruction. Confirm the actual alloy, environment, loading and damage before selecting mitigation. Generic signs are not unique proof of a mechanism.
DM-042Stress-oriented hydrogen-induced crackingEnvironment-assisted cracking & hydrogen · Stress-directed hydrogen damage
Mechanism pathway
Service conditions
Hydrogen charging, typically wet H2S, plus tensile stress
Physical processes
- Hydrogen forms small internal cracks
- Tensile stress promotes stacked crack arrays linking through thickness
Observable damage
Ladder-like stacked HIC arrays; through-wall linkage near welds
Possible failure mode
Leak or rupture
- Other names
- SOHIC
- Industries / exposed sectors
- Refining; sour oil/gas; chemical
- Typically affected parts
- Pressure-vessel plates near welds; stressed sour piping
- Susceptible materials
- Susceptible carbon/low-alloy steels
- Required chemicals / environment
- Hydrogen charging, typically wet H2S, plus tensile stress
- Influencing parameters
- Triaxial/residual stress; weld geometry; hydrogen flux; cleanliness
- Physical explanation (1–3 processes)
- Hydrogen forms small internal cracks
- Tensile stress promotes stacked crack arrays linking through thickness
- Signs and symptoms
- Ladder-like stacked HIC arrays; through-wall linkage near welds
- Prevention / slowing the damage
- Reduce local stress; select tested resistant steel; control sour conditions; qualified volumetric inspection
- Typical failure outcome
- Leak or rupture
- Possible consequences
- Toxic/flammable release
- Can be mistaken for
- HIC; SSC; lamellar tearing
- How to distinguish it
- Cross-sections show stress-oriented stacks linking through wall; distinguish from single rolling-plane laminations
- How often is it seen?
- No representative subtype-specific incidence was identified in the reviewed sources. This is a data gap, not evidence of rarity.
- Historical case / verification status
- No mechanism-attributed catastrophe was verified in the sources reviewed; this does not mean none has occurred.
Photographs — 5 needed (real-life, not diagrams)
Macro / field view
Close-up or micrograph
Cross-section
In-service failure
Distinguishing feature
Sources
- 80 Pargeter, R.J. (2007). Susceptibility to SOHIC for Linepipe and Pressure Vessel Steels: Review of Current Knowledge. NACE 2007. — Technical research paper (accessed 2026-09-08)
- 80 TWI — Sour Testing — Technical reference (accessed 2026-09-08)
Educational synthesis, not a diagnosis or repair instruction. Confirm the actual alloy, environment, loading and damage before selecting mitigation. Generic signs are not unique proof of a mechanism.
DM-043Hydrogen blisteringEnvironment-assisted cracking & hydrogen · Internal hydrogen damage
Mechanism pathway
Service conditions
Hydrogen entry, often from wet acidic/sour corrosion
Physical processes
- Hydrogen recombines to gas at internal discontinuities
- Gas pressure deforms or separates the overlying metal
Observable damage
Bulges; domed blisters; planar subsurface separations
Possible failure mode
Blister rupture; leak
- Other names
- Blister damage; hydrogen pressure blistering
- Industries / exposed sectors
- Refining; wet sour service; chemical
- Typically affected parts
- Vessel plates; piping walls; tank shells
- Susceptible materials
- Susceptible carbon steels with internal traps/laminations
- Required chemicals / environment
- Hydrogen entry, often from wet acidic/sour corrosion
- Influencing parameters
- Hydrogen flux; inclusion/lamination population; wall restraint
- Physical explanation (1–3 processes)
- Hydrogen recombines to gas at internal discontinuities
- Gas pressure deforms or separates the overlying metal
- Signs and symptoms
- Bulges; domed blisters; planar subsurface separations
- Prevention / slowing the damage
- Limit hydrogen charging; clean HIC-resistant materials; evaluate remaining ligament and connected cracks
- Typical failure outcome
- Blister rupture; leak
- Possible consequences
- Containment loss; reduced ligament capacity
- Can be mistaken for
- Coating blisters; HIC; fabrication laminations
- How to distinguish it
- Verify metal-wall bulging and subsurface gas cavity; distinguish from paint-only blisters
- How often is it seen?
- No representative subtype-specific incidence was identified in the reviewed sources. This is a data gap, not evidence of rarity.
- Historical case / verification status
- No mechanism-attributed catastrophe was verified in the sources reviewed; this does not mean none has occurred.
Photographs — 5 needed (real-life, not diagrams)
Macro / field view
Close-up or micrograph
Cross-section
In-service failure
Distinguishing feature
Sources
- 80 TWI — Sour Testing — Technical reference (accessed 2026-09-08)
- 80 Pargeter, R.J. (2007). Susceptibility to SOHIC for Linepipe and Pressure Vessel Steels: Review of Current Knowledge. NACE 2007. — Technical research paper (accessed 2026-09-08)
Educational synthesis, not a diagnosis or repair instruction. Confirm the actual alloy, environment, loading and damage before selecting mitigation. Generic signs are not unique proof of a mechanism.
DM-044Liquid metal embrittlementEnvironment-assisted cracking & hydrogen · Liquid-metal environment-assisted fracture
Mechanism pathway
Service conditions
A compatible embrittling liquid metal wetting a stressed susceptible solid
Physical processes
- Liquid metal reaches highly stressed surface/crack regions
- Adsorption/penetration assists loss of cohesion and crack advance
Observable damage
Rapid low-ductility cracks, often intergranular
Possible failure mode
Sudden fracture
- Other names
- LME; liquid-metal-assisted cracking
- Industries / exposed sectors
- Galvanizing; welding; chemical; metal processing
- Typically affected parts
- Loaded steel during galvanizing; contaminated welds; susceptible liquid-metal equipment
- Susceptible materials
- Specific couples, e.g. steel/liquid zinc or copper; aluminium/liquid mercury
- Required chemicals / environment
- A compatible embrittling liquid metal wetting a stressed susceptible solid
- Influencing parameters
- Wetting; temperature above liquidus; stress; contact chemistry
- Physical explanation (1–3 processes)
- Liquid metal reaches highly stressed surface/crack regions
- Adsorption/penetration assists loss of cohesion and crack advance
- Signs and symptoms
- Rapid low-ductility cracks, often intergranular
- Prevention / slowing the damage
- Exclude incompatible metal contamination; qualified galvanizing/welding practices; reduce restraint
- Typical failure outcome
- Sudden fracture
- Possible consequences
- Loss of structural support or containment
- Can be mistaken for
- Solidification cracking; reheat cracking; ordinary brittle fracture
- How to distinguish it
- Identify embrittling metal on/in crack path and liquid-state exposure; preserve evidence before cleaning
- How often is it seen?
- No representative subtype-specific incidence was identified in the reviewed sources. This is a data gap, not evidence of rarity.
- Historical case / verification status
- No verified LME catastrophe assigned here. Flixborough (1 June 1974) is not used as a proven LME case: the regulator’s account describes failure of a temporary bypass, not an established LME root cause.
Photographs — 5 needed (real-life, not diagrams)
Macro / field view
Close-up or micrograph
Cross-section
In-service failure
Distinguishing feature
Sources
- 80 TWI — Liquid metal embrittlement and common embrittling metal couples — Technical reference (accessed 2026-09-08)
- 80 TWI — Weldability of materials: aluminium alloys, Job Knowledge 21 — Technical reference (accessed 2026-09-08)
- 80 HSE — Flixborough, 1 June 1974 — Primary regulator accident summary (accessed 2026-09-08)
Educational synthesis, not a diagnosis or repair instruction. Confirm the actual alloy, environment, loading and damage before selecting mitigation. Generic signs are not unique proof of a mechanism.
DM-045Irradiation-assisted stress corrosion crackingEnvironment-assisted cracking & hydrogen · Radiation/environment interaction
Mechanism pathway
Service conditions
Reactor water, neutron exposure and tensile stress
Physical processes
- Radiation changes grain-boundary chemistry and hardening
- Localized deformation/oxidation under water promotes intergranular cracking
Observable damage
Intergranular cracks; bolt/internal-component failures
Possible failure mode
Bolt fracture; component separation; loss of structural function
- Other names
- IASCC
- Industries / exposed sectors
- Nuclear power
- Typically affected parts
- Core internals; baffle-former bolts; irradiated structural parts
- Susceptible materials
- Irradiated austenitic stainless steels and susceptible alloys
- Required chemicals / environment
- Reactor water, neutron exposure and tensile stress
- Influencing parameters
- Dose; temperature; water chemistry; stress; microstructure
- Physical explanation (1–3 processes)
- Radiation changes grain-boundary chemistry and hardening
- Localized deformation/oxidation under water promotes intergranular cracking
- Signs and symptoms
- Intergranular cracks; bolt/internal-component failures
- Prevention / slowing the damage
- Qualified irradiation-resistant materials; chemistry/stress management; targeted in-service inspection
- Typical failure outcome
- Bolt fracture; component separation; loss of structural function
- Possible consequences
- Loose parts; internal support degradation; outage
- Can be mistaken for
- Irradiation embrittlement; fatigue; unirradiated SCC
- How to distinguish it
- Confirm dose and aqueous exposure; correlate boundary cracking and material changes; irradiation alone is not proof of IASCC
- How often is it seen?
- No representative subtype-specific incidence was identified in the reviewed sources. This is a data gap, not evidence of rarity.
- Historical case / verification status
- No mechanism-attributed catastrophe was verified in the sources reviewed; this does not mean none has occurred.
Photographs — 5 needed (real-life, not diagrams)
Macro / field view
Close-up or micrograph
Cross-section
In-service failure
Distinguishing feature
Sources
- 80 Chen, Y., Chopra, O.K., Gruber, E.E. & Shack, W.J. (2010). NUREG/CR-7018, irradiation-assisted stress corrosion cracking. NRC / Argonne. — Primary institutional research abstract (accessed 2026-09-08)
- 80 NRC — Reactor Vessel Integrity — Regulatory technical reference (accessed 2026-09-08)
Educational synthesis, not a diagnosis or repair instruction. Confirm the actual alloy, environment, loading and damage before selecting mitigation. Generic signs are not unique proof of a mechanism.
DM-046High-temperature oxidationHigh-temperature chemical damage · Gas/metal reaction
Mechanism pathway
Service conditions
Oxygen-bearing hot gas; liquid water is unnecessary
Physical processes
- Oxide grows by interfacial reaction and diffusion
- Cracking/spallation exposes fresh metal and renews consumption
Observable damage
Scale; section loss; spalled flakes; dimensional change
Possible failure mode
Thinning-related rupture; scale blockage
- Other names
- Dry oxidation; scaling
- Industries / exposed sectors
- Power; furnaces; steel processing; aerospace
- Typically affected parts
- Furnace tubes; exhausts; turbine parts; hot structures
- Susceptible materials
- Steels; nickel alloys; other metals with inadequate oxide protection
- Required chemicals / environment
- Oxygen-bearing hot gas; liquid water is unnecessary
- Influencing parameters
- Temperature; time; oxygen potential; thermal cycling; alloy chemistry
- Physical explanation (1–3 processes)
- Oxide grows by interfacial reaction and diffusion
- Cracking/spallation exposes fresh metal and renews consumption
- Signs and symptoms
- Scale; section loss; spalled flakes; dimensional change
- Prevention / slowing the damage
- Oxidation-resistant alloy/coating; temperature control; reduce severe cycling; monitor scale and remaining wall
- Typical failure outcome
- Thinning-related rupture; scale blockage
- Possible consequences
- Overheating; debris damage; outage
- Can be mistaken for
- Hot corrosion; sulfidation; atmospheric rust
- How to distinguish it
- Identify scale phases and hot-service exposure; verify whether molten salts or sulfur caused the attack
- How often is it seen?
- No representative subtype-specific incidence was identified in the reviewed sources. This is a data gap, not evidence of rarity.
- Historical case / verification status
- No mechanism-attributed catastrophe was verified in the sources reviewed; this does not mean none has occurred.
Photographs — 5 needed (real-life, not diagrams)
Macro / field view
Close-up or micrograph
Cross-section
In-service failure
Distinguishing feature
Sources
- 80 TWI — Corrosion behavior of an HVOF sprayed Fe3Al coating in a high-temperature oxidizing/sulfidizing environment (2004) — Primary experimental paper (accessed 2026-09-08)
- 80 TWI — High temperature material selection for a powder processing environment — Primary material-selection case (accessed 2026-09-08)
- 80 TWI — What is an MCrAlY coating? — Technical reference (accessed 2026-09-08)
Educational synthesis, not a diagnosis or repair instruction. Confirm the actual alloy, environment, loading and damage before selecting mitigation. Generic signs are not unique proof of a mechanism.
DM-047Steam-side oxidation and exfoliationHigh-temperature chemical damage · Steam/metal reaction
Mechanism pathway
Service conditions
High-temperature steam
Physical processes
- Steam-side oxide thickens and consumes metal
- Growth/thermal mismatch causes oxide spallation
Observable damage
Internal scale; exfoliated particles; restricted tube flow
Possible failure mode
Tube rupture or flow blockage by exfoliated scale
- Other names
- Steam oxidation; oxide-scale exfoliation
- Industries / exposed sectors
- Fossil power; heat recovery; high-temperature steam
- Typically affected parts
- Superheater/reheater tubes; steam piping
- Susceptible materials
- Ferritic and austenitic heat-resistant steels
- Required chemicals / environment
- High-temperature steam
- Influencing parameters
- Temperature; time; alloy chromium; surface condition; thermal transients
- Physical explanation (1–3 processes)
- Steam-side oxide thickens and consumes metal
- Growth/thermal mismatch causes oxide spallation
- Signs and symptoms
- Internal scale; exfoliated particles; restricted tube flow
- Prevention / slowing the damage
- Appropriate steam-resistant alloy/surface treatment; manage temperature and cycling; inspect scale/blockage
- Typical failure outcome
- Tube rupture or flow blockage by exfoliated scale
- Possible consequences
- Overheating; outage; downstream erosion or turbine damage from detached scale
- Can be mistaken for
- Creep; fireside oxidation; deposit fouling
- How to distinguish it
- Locate oxide on steam side; analyse scale layers and deposits; separate oxidation loss from creep cavities
- How often is it seen?
- No representative subtype-specific incidence was identified in the reviewed sources. This is a data gap, not evidence of rarity.
- Historical case / verification status
- No mechanism-attributed catastrophe was verified in the sources reviewed; this does not mean none has occurred.
Photographs — 5 needed (real-life, not diagrams)
Macro / field view
Close-up or micrograph
Cross-section
In-service failure
Distinguishing feature
Sources
- 80 Kurley, J.M. & Pint, B.A. (2020). The effect of shot peening on steam oxidation of 304H stainless steel. Oxidation of Metals 93, 159–174. — Primary ORNL study (accessed 2026-09-08)
- 80 TWI — What are the limiting factors in gas turbine hot section components? — Technical reference (accessed 2026-09-08)
Educational synthesis, not a diagnosis or repair instruction. Confirm the actual alloy, environment, loading and damage before selecting mitigation. Generic signs are not unique proof of a mechanism.
DM-048High-temperature sulfidationHigh-temperature chemical damage · Sulfur/metal reaction
Mechanism pathway
Service conditions
Reactive sulfur species at elevated temperature; no water required
Physical processes
- Metal reacts to form sulfide scale
- Insufficiently protective scale permits continuing wall loss
Observable damage
Sulfide scale; broad thinning; individual components may corrode faster
Possible failure mode
Leak or catastrophic rupture
- Other names
- Sulfidic corrosion; sulfur corrosion
- Industries / exposed sectors
- Refining; petrochemical; high-temperature processing
- Typically affected parts
- Crude-unit piping; furnace tubes; sulfur-bearing process equipment
- Susceptible materials
- Carbon/low-alloy steels; susceptibility depends on alloy chemistry
- Required chemicals / environment
- Reactive sulfur species at elevated temperature; no water required
- Influencing parameters
- Temperature; sulfur species; silicon/chromium content; flow
- Physical explanation (1–3 processes)
- Metal reacts to form sulfide scale
- Insufficiently protective scale permits continuing wall loss
- Signs and symptoms
- Sulfide scale; broad thinning; individual components may corrode faster
- Prevention / slowing the damage
- Verify materials component-by-component; resistant alloys; targeted thickness monitoring
- Typical failure outcome
- Leak or catastrophic rupture
- Possible consequences
- Hydrocarbon release; fire
- Can be mistaken for
- Wet H2S corrosion; naphthenic acid corrosion; oxidation
- How to distinguish it
- Confirm hot service, sulfide scale and alloy chemistry; inspect fittings individually, not only adjacent pipe
- How often is it seen?
- No representative subtype-specific incidence was identified in the reviewed sources. This is a data gap, not evidence of rarity.
- Historical case / verification status
- Chevron Richmond, 6 August 2012: severe sulfidation thinning in low-silicon carbon-steel piping led to rupture and a major refinery fire. CSB completed its investigation in 2015.
Photographs — 5 needed (real-life, not diagrams)
Macro / field view
Close-up or micrograph
Cross-section
In-service failure
Distinguishing feature
Sources
- 80 CSB — Chevron Richmond Refinery Fire — Primary accident investigation (accessed 2026-09-08)
- 80 CSB / Cal OSHA (13 February 2013) — Technical report on Chevron 2012 pipe rupture and fire: sulfidation corrosion — Primary metallurgical-investigation summary (accessed 2026-09-08)
- 80 TWI — Corrosion behavior of an HVOF sprayed Fe3Al coating in a high-temperature oxidizing/sulfidizing environment (2004) — Primary experimental paper (accessed 2026-09-08)
Educational synthesis, not a diagnosis or repair instruction. Confirm the actual alloy, environment, loading and damage before selecting mitigation. Generic signs are not unique proof of a mechanism.
DM-049Hot corrosion by molten saltsHigh-temperature chemical damage · Salt-assisted high-temperature corrosion
Mechanism pathway
Service conditions
Aggressive deposits, often sulfates or vanadium-bearing salts
Physical processes
- Molten deposits dissolve or destabilize protective oxides
- Accelerated oxidation/sulfidation consumes exposed alloy
Observable damage
Pitted scale; undercut coatings; sulfide/oxide penetration
Possible failure mode
Blade/tube fracture or perforation
- Other names
- Type I/Type II hot corrosion; deposit-induced hot corrosion
- Industries / exposed sectors
- Gas turbines; aviation; boilers; incineration
- Typically affected parts
- Turbine blades/vanes; combustors; hot tubes
- Susceptible materials
- Nickel/cobalt superalloys; heat-resistant steels
- Required chemicals / environment
- Aggressive deposits, often sulfates or vanadium-bearing salts
- Influencing parameters
- Salt chemistry; temperature/melting behaviour; oxygen/sulfur potential; deposit flux
- Physical explanation (1–3 processes)
- Molten deposits dissolve or destabilize protective oxides
- Accelerated oxidation/sulfidation consumes exposed alloy
- Signs and symptoms
- Pitted scale; undercut coatings; sulfide/oxide penetration
- Prevention / slowing the damage
- Fuel/air contaminant control; resistant coatings/alloys; approved deposit removal
- Typical failure outcome
- Blade/tube fracture or perforation
- Possible consequences
- Rotor damage; forced outage
- Can be mistaken for
- Ordinary oxidation; sulfidation; erosion
- How to distinguish it
- Analyse deposit and scale chemistry; confirm relevant molten-salt regime; temperature alone cannot assign Type I/II
- How often is it seen?
- No representative subtype-specific incidence was identified in the reviewed sources. This is a data gap, not evidence of rarity.
- Historical case / verification status
- No mechanism-attributed catastrophe was verified in the sources reviewed; this does not mean none has occurred.
Photographs — 5 needed (real-life, not diagrams)
Macro / field view
Close-up or micrograph
Cross-section
In-service failure
Distinguishing feature
Sources
- 80 TWI — What is an MCrAlY coating? — Technical reference (accessed 2026-09-08)
- 50 Haynes International — HAYNES HR-160 alloy — Primary manufacturer test data (accessed 2026-09-08)
- 80 TWI — What are the limiting factors in gas turbine hot section components? — Technical reference (accessed 2026-09-08)
Educational synthesis, not a diagnosis or repair instruction. Confirm the actual alloy, environment, loading and damage before selecting mitigation. Generic signs are not unique proof of a mechanism.
DM-050Naphthenic acid corrosionHigh-temperature chemical damage · Hot-oil acid attack
Mechanism pathway
Service conditions
Reactive organic acids in hot oil; aqueous phase unnecessary
Physical processes
- Organic acids react with iron to form oil-soluble iron carboxylates
- Film stability and sulfur interactions govern local attack
Observable damage
Sharp grooves; localized or broad wall loss in hot-oil circuits
Possible failure mode
Leak or rupture
- Other names
- NAC; hot organic-acid corrosion
- Industries / exposed sectors
- Crude refining; heavy-oil processing
- Typically affected parts
- Hot crude/vacuum distillation piping; transfer lines; pumps
- Susceptible materials
- Carbon/low-alloy steel; alloy resistance depends on molybdenum and environment
- Required chemicals / environment
- Reactive organic acids in hot oil; aqueous phase unnecessary
- Influencing parameters
- Acid structure; temperature; flow; sulfur chemistry; scale stability
- Physical explanation (1–3 processes)
- Organic acids react with iron to form oil-soluble iron carboxylates
- Film stability and sulfur interactions govern local attack
- Signs and symptoms
- Sharp grooves; localized or broad wall loss in hot-oil circuits
- Prevention / slowing the damage
- Evaluate real feed corrosivity, not TAN alone; appropriate resistant alloys; control flow/hot spots
- Typical failure outcome
- Leak or rupture
- Possible consequences
- Hot hydrocarbon release; fire
- Can be mistaken for
- Sulfidation; erosion-corrosion
- How to distinguish it
- Correlate acid/sulfur chemistry, temperature and morphology; total acid number alone is not diagnostic
- How often is it seen?
- No representative subtype-specific incidence was identified in the reviewed sources. This is a data gap, not evidence of rarity.
- Historical case / verification status
- No mechanism-attributed catastrophe was verified in the sources reviewed; this does not mean none has occurred.
Photographs — 5 needed (real-life, not diagrams)
Macro / field view
Close-up or micrograph
Cross-section
In-service failure
Distinguishing feature
Sources
- 80 Mechanism of magnetite formation in high temperature corrosion by model naphthenic acids (2016). Corrosion Science 111, 822–834. — Primary experimental paper (accessed 2026-09-08)
- 80 Huang, B.S., Yin, W.F., Sang, D.H. & Jiang, Z.Y. (2012). Synergy of naphthenic acid and sulfur corrosion. Applied Surface Science 259, 664–670. — Primary experimental paper (accessed 2026-09-08)
Educational synthesis, not a diagnosis or repair instruction. Confirm the actual alloy, environment, loading and damage before selecting mitigation. Generic signs are not unique proof of a mechanism.
DM-051High-temperature hydrogen/hydrogen-sulfide corrosionHigh-temperature chemical damage · High-temperature gas-phase corrosion
Mechanism pathway
Service conditions
Hot H2/H2S gas; liquid water not required
Physical processes
- Sulfur-bearing hot gas reacts with alloy constituents
- Sulfide formation consumes or penetrates the load-bearing metal
Observable damage
Wall loss and internal sulfide penetration
Possible failure mode
Leak or rupture
- Other names
- H2/H2S corrosion; reducing-gas sulfidation
- Industries / exposed sectors
- Hydrotreating; hydrocracking; gas processing
- Typically affected parts
- Reactor-effluent piping; heater tubes; hot exchangers
- Susceptible materials
- Steels and heat-resistant alloys; resistance depends on alloy and gas conditions
- Required chemicals / environment
- Hot H2/H2S gas; liquid water not required
- Influencing parameters
- Temperature; exposure; gas composition; sulfur/oxygen potentials; alloy chemistry
- Physical explanation (1–3 processes)
- Sulfur-bearing hot gas reacts with alloy constituents
- Sulfide formation consumes or penetrates the load-bearing metal
- Signs and symptoms
- Wall loss and internal sulfide penetration
- Prevention / slowing the damage
- Duty-qualified alloys; chemistry/temperature management; thickness monitoring
- Typical failure outcome
- Leak or rupture
- Possible consequences
- Hydrogen/hydrocarbon/H2S release; fire
- Can be mistaken for
- HTHA; wet H2S corrosion; ordinary sulfidation
- How to distinguish it
- Prove gas-phase hot reducing exposure; metallography separates surface loss from internal methane damage
- How often is it seen?
- No representative subtype-specific incidence was identified in the reviewed sources. This is a data gap, not evidence of rarity.
- Historical case / verification status
- No mechanism-attributed catastrophe was verified in the sources reviewed; this does not mean none has occurred.
Photographs — 5 needed (real-life, not diagrams)
Macro / field view
Close-up or micrograph
Cross-section
In-service failure
Distinguishing feature
Sources
- 50 Haynes International — HAYNES HR-160 alloy — Primary manufacturer test data (accessed 2026-09-08)
- 80 TWI — Corrosion behavior of an HVOF sprayed Fe3Al coating in a high-temperature oxidizing/sulfidizing environment (2004) — Primary experimental paper (accessed 2026-09-08)
- 80 API — Recommended Practice 571: Damage Mechanisms Affecting Fixed Equipment in the Refining Industry — Official standard overview (accessed 2026-09-08)
- 50 Haynes International — Sulfidation & Chlorine Environment Resistance of High-temperature Alloys — public manufacturer test data (accessed 2026-09-08)
- 80 TWI — What is high temperature hydrogen attack? — Technical reference (accessed 2026-09-08)
Educational synthesis, not a diagnosis or repair instruction. Confirm the actual alloy, environment, loading and damage before selecting mitigation. Generic signs are not unique proof of a mechanism.
DM-052High-temperature hydrogen attackHigh-temperature chemical damage · Methane-forming internal damage
Mechanism pathway
Service conditions
Hydrogen at elevated temperature and sufficient activity/partial pressure
Physical processes
- Hydrogen reacts with carbon to form trapped methane
- Methane cavities grow and link while steel decarburizes
Observable damage
Internal fissures/cavities; decarburization; late-stage cracking
Possible failure mode
Brittle-appearing rupture or leak
- Other names
- HTHA; hot hydrogen attack
- Industries / exposed sectors
- Refining; hydrogen processing; ammonia
- Typically affected parts
- Hot hydrogen vessels; exchanger shells; piping; weld regions
- Susceptible materials
- Carbon/low-alloy steels with insufficient carbide stability for the duty
- Required chemicals / environment
- Hydrogen at elevated temperature and sufficient activity/partial pressure
- Influencing parameters
- Temperature; hydrogen pressure; time; carbides; weld condition
- Physical explanation (1–3 processes)
- Hydrogen reacts with carbon to form trapped methane
- Methane cavities grow and link while steel decarburizes
- Signs and symptoms
- Internal fissures/cavities; decarburization; late-stage cracking
- Prevention / slowing the damage
- Use duty-qualified resistant materials; verify operating envelope; specialized validated inspection
- Typical failure outcome
- Brittle-appearing rupture or leak
- Possible consequences
- Major fire/explosion; fatalities possible
- Can be mistaken for
- Ambient HE; creep; thermal decarburization
- How to distinguish it
- Metallography identifies methane-type cavities and carbon depletion; no single negative NDT test proves absence
- How often is it seen?
- No representative subtype-specific incidence was identified in the reviewed sources. This is a data gap, not evidence of rarity.
- Historical case / verification status
- Tesoro Anacortes, 2 April 2010: HTHA in a heat-exchanger shell caused a catastrophic rupture/fire; seven workers died.
Photographs — 5 needed (real-life, not diagrams)
Macro / field view
Close-up or micrograph
Cross-section
In-service failure
Distinguishing feature
Sources
- 80 TWI — What is high temperature hydrogen attack? — Technical reference (accessed 2026-09-08)
- 80 US Chemical Safety Board (2016) — Safety alert stemming from fatal Tesoro Anacortes investigation — Regulatory safety alert (accessed 2026-09-08)
- 80 US Chemical Safety Board — Tesoro Anacortes Refinery Fatal Explosion and Fire — Primary accident investigation (accessed 2026-09-08)
- 80 CSB — Tesoro investigation finds HTHA damage to heat exchanger — public primary investigation summary (accessed 2026-09-08)
Educational synthesis, not a diagnosis or repair instruction. Confirm the actual alloy, environment, loading and damage before selecting mitigation. Generic signs are not unique proof of a mechanism.
DM-053CarburizationHigh-temperature chemical damage · Interstitial uptake
Mechanism pathway
Service conditions
Carbon-rich gas with sufficiently high carbon activity
Physical processes
- Carbon enters the exposed alloy
- Carburized microstructure changes local properties; defects in a protective coating can concentrate attack
Observable damage
Subsurface carburization; locally deep attack at protective-coating defects
Possible failure mode
Cracking or rupture
- Other names
- Carbon uptake; internal carburization
- Industries / exposed sectors
- Petrochemical cracking; reforming; heat-treatment furnaces
- Typically affected parts
- Furnace tubes; retorts; high-temperature internals
- Susceptible materials
- Heat-resistant nickel alloys; steels in related carbon-uptake service
- Required chemicals / environment
- Carbon-rich gas with sufficiently high carbon activity
- Influencing parameters
- Temperature; carbon activity; time; oxide protection
- Physical explanation (1–3 processes)
- Carbon enters the exposed alloy
- Carburized microstructure changes local properties; defects in a protective coating can concentrate attack
- Signs and symptoms
- Subsurface carburization; locally deep attack at protective-coating defects
- Prevention / slowing the damage
- Control carbon potential; resistant alloy/coating; preserve protective scale; monitor microstructure
- Typical failure outcome
- Cracking or rupture
- Possible consequences
- Tube failure; fire/outage
- Can be mistaken for
- Metal dusting; intentional case hardening; sigma embrittlement
- How to distinguish it
- Carbon profiles and carbide identification; distinguish intact carburized metal from disintegrating metal dusting
- How often is it seen?
- No representative subtype-specific incidence was identified in the reviewed sources. This is a data gap, not evidence of rarity.
- Historical case / verification status
- No mechanism-attributed catastrophe was verified in the sources reviewed; this does not mean none has occurred.
Photographs — 5 needed (real-life, not diagrams)
Macro / field view
Close-up or micrograph
Cross-section
In-service failure
Distinguishing feature
Sources
- 80 TWI — What is plasma carburising / plasma nitriding? — Technical process reference (accessed 2026-09-08)
- 80 TWI — High temperature material selection for a powder processing environment — Primary material-selection case (accessed 2026-09-08)
- 80 TWI — High temperature corrosion testing — Primary research programme (accessed 2026-09-08)
- 80 TWI — Optimising Manufacturing for Aggressive Environments — public technical article (accessed 2026-09-08)
- 80 On the mechanism of catastrophic carburization: metal dusting (1993) — publisher abstract (accessed 2026-09-08)
Educational synthesis, not a diagnosis or repair instruction. Confirm the actual alloy, environment, loading and damage before selecting mitigation. Generic signs are not unique proof of a mechanism.
DM-054DecarburizationHigh-temperature chemical damage · Interstitial loss
Mechanism pathway
Service conditions
Atmosphere able to remove carbon, e.g. oxidizing/wet gases; environment-specific
Physical processes
- Carbon diffuses toward a low-carbon-potential surface
- Surface reactions remove carbon, reducing hardenability/strength
Observable damage
Soft ferritic surface layer; reduced hardness; fatigue initiation
Possible failure mode
Wear-out, distortion or later fatigue fracture; immediate failure is not inevitable
- Other names
- Carbon depletion; surface decarburization
- Industries / exposed sectors
- Heat treatment; forging; high-temperature service
- Typically affected parts
- Spring surfaces; forgings; tubes; steel components
- Susceptible materials
- Carbon and low-alloy steels
- Required chemicals / environment
- Atmosphere able to remove carbon, e.g. oxidizing/wet gases; environment-specific
- Influencing parameters
- Temperature; time; carbon potential; scale integrity
- Physical explanation (1–3 processes)
- Carbon diffuses toward a low-carbon-potential surface
- Surface reactions remove carbon, reducing hardenability/strength
- Signs and symptoms
- Soft ferritic surface layer; reduced hardness; fatigue initiation
- Prevention / slowing the damage
- Control furnace atmosphere and thermal exposure; verify the affected depth before acceptance
- Typical failure outcome
- Wear-out, distortion or later fatigue fracture; immediate failure is not inevitable
- Possible consequences
- Reduced life; potential component break
- Can be mistaken for
- HTHA decarburization; overtempering; carburization gradients
- How to distinguish it
- Compare carbon-sensitive microstructure and hardness depth profiles; distinguish surface carbon loss from internal methane-cavity damage
- How often is it seen?
- No representative subtype-specific incidence was identified in the reviewed sources. This is a data gap, not evidence of rarity.
- Historical case / verification status
- No mechanism-attributed catastrophe was verified in the sources reviewed; this does not mean none has occurred.
Photographs — 5 needed (real-life, not diagrams)
Macro / field view
Close-up or micrograph
Cross-section
In-service failure
Distinguishing feature
Sources
- 80 ASM Handbook 4B (2014). Steel Heat Treating Technologies. — Authoritative handbook overview (accessed 2026-09-08)
- 80 ASM Handbook 4F (2024). Steel Heat Treatment Failures due to Quenching, pp. 575–592. — Authoritative handbook abstract (accessed 2026-09-08)
- 80 TWI — What is high temperature hydrogen attack? — Technical reference (accessed 2026-09-08)
- 80 Eddy currents and hardness testing for evaluation of steel decarburizing (2006) — publisher abstract and public section snippets (accessed 2026-09-08)
Educational synthesis, not a diagnosis or repair instruction. Confirm the actual alloy, environment, loading and damage before selecting mitigation. Generic signs are not unique proof of a mechanism.
DM-055Metal dustingHigh-temperature chemical damage · Carbon-driven disintegration
Mechanism pathway
Service conditions
Strongly carburizing gas; carbon activity above graphite equilibrium
Physical processes
- Carbon supersaturation/carburization destabilizes near-surface metal
- Metal breaks down into particles associated with coke/carbon
Observable damage
Pits; metal powder in coke; rapid local wastage
Possible failure mode
Perforation or rupture
- Other names
- Catastrophic carburization; carbon-induced disintegration
- Industries / exposed sectors
- Syngas; reforming; petrochemical; heat treatment
- Typically affected parts
- Process tubes; heat exchangers; furnace internals
- Susceptible materials
- Iron, nickel and cobalt alloys under susceptible conditions
- Required chemicals / environment
- Strongly carburizing gas; carbon activity above graphite equilibrium
- Influencing parameters
- Temperature; CO/H2 chemistry; water content; surface scale
- Physical explanation (1–3 processes)
- Carbon supersaturation/carburization destabilizes near-surface metal
- Metal breaks down into particles associated with coke/carbon
- Signs and symptoms
- Pits; metal powder in coke; rapid local wastage
- Prevention / slowing the damage
- Control gas chemistry and temperatures; resistant materials/coatings; maintain protective scales
- Typical failure outcome
- Perforation or rupture
- Possible consequences
- Syngas release; fire; outage
- Can be mistaken for
- Carburization without dusting; erosion; sulfidation
- How to distinguish it
- Identify metal particles/carbon and disintegrated microstructure; correlate with carbon activity and process conditions
- How often is it seen?
- No representative subtype-specific incidence was identified in the reviewed sources. This is a data gap, not evidence of rarity.
- Historical case / verification status
- No mechanism-attributed catastrophe was verified in the sources reviewed; this does not mean none has occurred.
Photographs — 5 needed (real-life, not diagrams)
Macro / field view
Close-up or micrograph
Cross-section
In-service failure
Distinguishing feature
Sources
- 80 TWI — High temperature corrosion testing — Primary research programme (accessed 2026-09-08)
- 80 TWI — High temperature material selection for a powder processing environment — Primary material-selection case (accessed 2026-09-08)
- 80 On the mechanism of catastrophic carburization: metal dusting (1993) — publisher abstract (accessed 2026-09-08)
- 80 Metal dusting and coking of alloy 803 (2004) — publisher abstract and public introduction (accessed 2026-09-08)
Educational synthesis, not a diagnosis or repair instruction. Confirm the actual alloy, environment, loading and damage before selecting mitigation. Generic signs are not unique proof of a mechanism.
DM-056Uncontrolled nitriding damageHigh-temperature chemical damage · Interstitial uptake
Mechanism pathway
Service conditions
Nitrogen-bearing gas with sufficient nitriding potential, often NH3-containing
Physical processes
- Ammonia dissociation supplies nitrogen that enters the alloy
- Brittle nitride formation and protective-oxide defects promote cracking
Observable damage
Brittle nitride formation; cracks; quasi-cleavage in the reported coil case
Possible failure mode
Cracking or brittle break
- Other names
- In-service nitridation; nitrogen uptake
- Industries / exposed sectors
- Ammonia; chemical; high-temperature processing
- Typically affected parts
- Heating coils; ammonia-service hot components
- Susceptible materials
- FeCrAl heating alloys; other nitride-forming alloys require service-specific assessment
- Required chemicals / environment
- Nitrogen-bearing gas with sufficient nitriding potential, often NH3-containing
- Influencing parameters
- Temperature; exposure; ammonia pressure; protective-oxide integrity
- Physical explanation (1–3 processes)
- Ammonia dissociation supplies nitrogen that enters the alloy
- Brittle nitride formation and protective-oxide defects promote cracking
- Signs and symptoms
- Brittle nitride formation; cracks; quasi-cleavage in the reported coil case
- Prevention / slowing the damage
- Qualify alloy and protective surfaces for actual ammonia conditions; monitor cracking
- Typical failure outcome
- Cracking or brittle break
- Possible consequences
- Loss of containment or internal-component failure
- Can be mistaken for
- Carburization; sigma phase; intentional nitriding
- How to distinguish it
- Nitrogen profile and nitride identification; deliberate controlled nitriding is not automatically damage
- How often is it seen?
- No representative subtype-specific incidence was identified in the reviewed sources. This is a data gap, not evidence of rarity.
- Historical case / verification status
- A 2024 laboratory failure investigation attributed premature failure of FeCrAl heating coils in hot, pressurized ammonia to destructive nitridation. It is not a population incidence estimate or a public-accident report.
Photographs — 5 needed (real-life, not diagrams)
Macro / field view
Close-up or micrograph
Cross-section
In-service failure
Distinguishing feature
Sources
- 80 TWI — What is plasma carburising / plasma nitriding? — Technical process reference (accessed 2026-09-08)
- 50 Haynes International — HAYNES HR-160 alloy — Primary manufacturer test data (accessed 2026-09-08)
- 80 Laws et al. (2024) — Failure analysis of FeCrAl heating coils exposed to a high-temperature, high-pressure ammonia environment — publisher abstract (accessed 2026-09-08)
Educational synthesis, not a diagnosis or repair instruction. Confirm the actual alloy, environment, loading and damage before selecting mitigation. Generic signs are not unique proof of a mechanism.
DM-057Creep deformation and cavitationCreep & metallurgical ageing · Time-dependent elevated-temperature damage
Mechanism pathway
Service conditions
None essential; oxidation/corrosion may accelerate damage
Physical processes
- Dislocation/diffusion-controlled deformation accumulates
- Grain-boundary cavities can nucleate and link under stress
Observable damage
Bulging; elongation; cavitation; creep cracks; warning may be limited
Possible failure mode
Stress rupture; leak; excessive deformation
- Other names
- Creep damage; time-dependent deformation; legacy title: creep and stress rupture
- Industries / exposed sectors
- Power; refining; turbines; high-temperature processing
- Typically affected parts
- Steam pipes; headers; tubes; turbine blades; hot bolts
- Susceptible materials
- Steels; nickel/cobalt alloys; other metals at material-dependent high homologous temperature
- Required chemicals / environment
- None essential; oxidation/corrosion may accelerate damage
- Influencing parameters
- Metal temperature; sustained stress; time; microstructure
- Physical explanation (1–3 processes)
- Dislocation/diffusion-controlled deformation accumulates
- Grain-boundary cavities can nucleate and link under stress
- Signs and symptoms
- Bulging; elongation; cavitation; creep cracks; warning may be limited
- Prevention / slowing the damage
- Control metal temperature/stress; suitable alloy/heat treatment; life assessment and targeted inspection
- Typical failure outcome
- Stress rupture; leak; excessive deformation
- Possible consequences
- Steam/hydrocarbon release; blade failure; outage
- Can be mistaken for
- Short-term overheating; HTHA; creep-fatigue
- How to distinguish it
- Assess service history, dimensions, cavities and microstructure; surface replication alone may miss internal damage
- How often is it seen?
- No representative subtype-specific incidence was identified in the reviewed sources. This is a data gap, not evidence of rarity.
- Historical case / verification status
- No mechanism-attributed catastrophe was verified in the sources reviewed; this does not mean none has occurred.
Photographs — 5 needed (real-life, not diagrams)
Macro / field view
Close-up or micrograph
Cross-section
In-service failure
Distinguishing feature
Sources
- 80 TWI — Detection of Early-Stage Creep Damage in Welded Steels, Report 1113/2019 — Primary research summary (accessed 2026-09-08)
- 80 TWI — What are the limiting factors in gas turbine hot section components? — Technical reference (accessed 2026-09-08)
- 80 TWI — What is type IV cracking, and how is it detected? — Technical reference (accessed 2026-09-08)
Educational synthesis, not a diagnosis or repair instruction. Confirm the actual alloy, environment, loading and damage before selecting mitigation. Generic signs are not unique proof of a mechanism.
DM-058Creep-fatigue interactionCreep & metallurgical ageing · Time/cycle interaction
Mechanism pathway
Service conditions
None essential; oxidation often contributes
Physical processes
- Cyclic plasticity initiates/grows cracks
- Creep during hot holds damages boundaries
- Interaction can shorten life beyond separate mechanisms
Observable damage
Mixed intergranular/transgranular cracking; cavities near cyclic cracks
Possible failure mode
Crack/leak; rupture
- Other names
- Creep–fatigue damage
- Industries / exposed sectors
- Flexible power generation; turbines; process heaters
- Typically affected parts
- Headers; thick-section joints; blades; thermal-transition regions
- Susceptible materials
- High-temperature steels and superalloys
- Required chemicals / environment
- None essential; oxidation often contributes
- Influencing parameters
- Hold times; strain range; temperature; cycling sequence; stress relaxation
- Physical explanation (1–3 processes)
- Cyclic plasticity initiates/grows cracks
- Creep during hot holds damages boundaries
- Interaction can shorten life beyond separate mechanisms
- Signs and symptoms
- Mixed intergranular/transgranular cracking; cavities near cyclic cracks
- Prevention / slowing the damage
- Manage start/stop transients and dwell stress; joint design; validated interaction-life assessment
- Typical failure outcome
- Crack/leak; rupture
- Possible consequences
- Forced outage; hot-fluid release
- Can be mistaken for
- Thermal fatigue alone; creep alone; reheat cracking
- How to distinguish it
- Combine cycle/dwell records with fracture path and cavitation; do not assume linear damage addition is always valid
- How often is it seen?
- No representative subtype-specific incidence was identified in the reviewed sources. This is a data gap, not evidence of rarity.
- Historical case / verification status
- No mechanism-attributed catastrophe was verified in the sources reviewed; this does not mean none has occurred.
Photographs — 5 needed (real-life, not diagrams)
Macro / field view
Close-up or micrograph
Cross-section
In-service failure
Distinguishing feature
Sources
- 80 TWI — What are the limiting factors in gas turbine hot section components? — Technical reference (accessed 2026-09-08)
- 80 TWI — Review of type IV cracking of weldments in 9–12%Cr creep-strength-enhanced ferritic steels — Research paper (accessed 2026-09-08)
- 50 Tetra Engineering — HRSG Tube Failure Statistics — Primary consulting-cohort summary (accessed 2026-09-08)
- 80 Creep–fatigue endurance of 304 stainless steels (2014) — publisher public article text (accessed 2026-09-08)
- 80 Creep-fatigue interaction behaviour of type 308 stainless steel weld metal and type 304 stainless steel base metal (1993) — publisher abstract (accessed 2026-09-08)
Educational synthesis, not a diagnosis or repair instruction. Confirm the actual alloy, environment, loading and damage before selecting mitigation. Generic signs are not unique proof of a mechanism.
DM-059Type IV creep crackingCreep & metallurgical ageing · Weld-HAZ creep subtype
Mechanism pathway
Service conditions
None essential
Physical processes
- Creep strain localizes in the weaker outer HAZ
- Boundary cavities coalesce into a through-wall crack
Observable damage
HAZ cavity bands; cracks away from fusion boundary; limited overall strain
Possible failure mode
Leak or rupture
- Other names
- Type IV weld failure
- Industries / exposed sectors
- Power; petrochemical steam systems
- Typically affected parts
- Fine-grained/intercritical HAZ in ferritic weldments
- Susceptible materials
- Cr-Mo and creep-strength-enhanced ferritic steels, including 9–12% Cr grades
- Required chemicals / environment
- None essential
- Influencing parameters
- Temperature; sustained stress; weld/PWHT microstructure; time
- Physical explanation (1–3 processes)
- Creep strain localizes in the weaker outer HAZ
- Boundary cavities coalesce into a through-wall crack
- Signs and symptoms
- HAZ cavity bands; cracks away from fusion boundary; limited overall strain
- Prevention / slowing the damage
- Qualified material/weld/heat treatment; stress and temperature control; HAZ-targeted volumetric inspection
- Typical failure outcome
- Leak or rupture
- Possible consequences
- High-energy steam release; outage
- Can be mistaken for
- Reheat cracking; Type I/II/III weld creep; HTHA
- How to distinguish it
- Locate damage in fine/intercritical HAZ and demonstrate creep cavities; examine subsurface material
- How often is it seen?
- No representative subtype-specific incidence was identified in the reviewed sources. This is a data gap, not evidence of rarity.
- Historical case / verification status
- No mechanism-attributed catastrophe was verified in the sources reviewed; this does not mean none has occurred.
Photographs — 5 needed (real-life, not diagrams)
Macro / field view
Close-up or micrograph
Cross-section
In-service failure
Distinguishing feature
Sources
- 80 TWI — What is type IV cracking, and how is it detected? — Technical reference (accessed 2026-09-08)
- 80 TWI — Review of type IV cracking of weldments in 9–12%Cr creep-strength-enhanced ferritic steels — Research paper (accessed 2026-09-08)
- 80 TWI — Detection of Early-Stage Creep Damage in Welded Steels, Report 1113/2019 — Primary research summary (accessed 2026-09-08)
Educational synthesis, not a diagnosis or repair instruction. Confirm the actual alloy, environment, loading and damage before selecting mitigation. Generic signs are not unique proof of a mechanism.
DM-060Dissimilar-metal weld creep/interface failureCreep & metallurgical ageing · Dissimilar-joint creep subtype
Mechanism pathway
Service conditions
None essential; oxidation may assist exposed interfaces
Physical processes
- Carbon migration creates a carbon-depleted zone with lower creep strength
- Creep damage can localize beside the fusion boundary
Observable damage
Cracks near fusion boundary; carbide-depleted region; creep damage
Possible failure mode
Leak or weld separation
- Other names
- DMW creep; fusion-boundary creep damage
- Industries / exposed sectors
- Power; refining; high-temperature piping
- Typically affected parts
- Ferritic-to-austenitic/nickel welds; dissimilar ferritic joints
- Susceptible materials
- Dissimilar heat-resistant steels and nickel filler combinations
- Required chemicals / environment
- None essential; oxidation may assist exposed interfaces
- Influencing parameters
- Alloy/carbon-activity difference; heat treatment; operating stress; temperature; time
- Physical explanation (1–3 processes)
- Carbon migration creates a carbon-depleted zone with lower creep strength
- Creep damage can localize beside the fusion boundary
- Signs and symptoms
- Cracks near fusion boundary; carbide-depleted region; creep damage
- Prevention / slowing the damage
- Qualify filler and heat treatment for the dissimilar joint; assess cross-weld creep strength
- Typical failure outcome
- Leak or weld separation
- Possible consequences
- Steam/hydrocarbon release; outage
- Can be mistaken for
- Type IV creep; lack of fusion; reheat cracking
- How to distinguish it
- Locate crack relative to fusion boundary and HAZ; carbon/hardness mapping plus cavities and service history
- How often is it seen?
- No representative subtype-specific incidence was identified in the reviewed sources. This is a data gap, not evidence of rarity.
- Historical case / verification status
- No mechanism-attributed catastrophe was verified in the sources reviewed; this does not mean none has occurred.
Photographs — 5 needed (real-life, not diagrams)
Macro / field view
Close-up or micrograph
Cross-section
In-service failure
Distinguishing feature
Sources
- 80 TWI — Review of type IV cracking of weldments in 9–12%Cr creep-strength-enhanced ferritic steels — Research paper (accessed 2026-09-08)
- 80 TWI — Detection of Early-Stage Creep Damage in Welded Steels, Report 1113/2019 — Primary research summary (accessed 2026-09-08)
- 80 TWI — What is type IV cracking, and how is it detected? — Technical reference (accessed 2026-09-08)
Educational synthesis, not a diagnosis or repair instruction. Confirm the actual alloy, environment, loading and damage before selecting mitigation. Generic signs are not unique proof of a mechanism.
DM-061Overheating-induced softening and rapid deformationCreep & metallurgical ageing · Acute thermal overload
Mechanism pathway
Service conditions
No corrosive species essential; deposits or blocked cooling can raise metal temperature
Physical processes
- Acute overheating reduces the wall’s load-bearing capacity
- Plastic flow under internal pressure can rapidly open a rupture
Observable damage
Bulging; thin-lipped burst in acute overheating; thermally altered microstructure
Possible failure mode
Tube burst
- Other names
- Short-term overheating damage; legacy title: short-term overheating rupture
- Industries / exposed sectors
- Boilers; fired heaters; furnaces
- Typically affected parts
- Waterwall/superheater tubes; flame-impinged coils
- Susceptible materials
- Carbon/low-alloy steel; heat-resistant alloys
- Required chemicals / environment
- No corrosive species essential; deposits or blocked cooling can raise metal temperature
- Influencing parameters
- Peak metal temperature; duration; pressure; heat flux; cooling flow
- Physical explanation (1–3 processes)
- Acute overheating reduces the wall’s load-bearing capacity
- Plastic flow under internal pressure can rapidly open a rupture
- Signs and symptoms
- Bulging; thin-lipped burst in acute overheating; thermally altered microstructure
- Prevention / slowing the damage
- Maintain cooling flow; prevent dryout/flame impingement; protective trips and temperature monitoring
- Typical failure outcome
- Tube burst
- Possible consequences
- Hot-fluid release; fire; forced outage
- Can be mistaken for
- Long-term creep; thinning-induced burst; thermal shock
- How to distinguish it
- Reconstruct excursion and remaining wall; metallography distinguishes acute heating from long-term cavitation
- How often is it seen?
- No representative subtype-specific incidence was identified in the reviewed sources. This is a data gap, not evidence of rarity.
- Historical case / verification status
- No mechanism-attributed catastrophe was verified in the sources reviewed; this does not mean none has occurred.
Photographs — 5 needed (real-life, not diagrams)
Macro / field view
Close-up or micrograph
Cross-section
In-service failure
Distinguishing feature
Sources
- 50 Veolia Water Technologies — Water Handbook, chapter 14: Boiler System Failures — Manufacturer technical handbook (accessed 2026-09-08)
- 80 Dooley, B. & McNaughton, W. (EPRI, 1997). Don’t let those boiler tubes fail again. Power Engineering. — Primary institutional authors’ technical article (accessed 2026-09-08)
Educational synthesis, not a diagnosis or repair instruction. Confirm the actual alloy, environment, loading and damage before selecting mitigation. Generic signs are not unique proof of a mechanism.
DM-062Thermal graphitization of steelCreep & metallurgical ageing · Thermal microstructural degradation
Mechanism pathway
Service conditions
None essential
Physical processes
- Metastable carbides decompose
- Graphite precipitates; linked particles/bands weaken the steel
Observable damage
Graphite particles or linked HAZ bands; associated loss of strength/toughness
Possible failure mode
Low-ductility rupture
- Other names
- Graphitisation; carbide decomposition
- Industries / exposed sectors
- Older power/process high-temperature systems
- Typically affected parts
- Carbon/carbon-molybdenum steel pipe; weld HAZ
- Susceptible materials
- Susceptible carbon and carbon-molybdenum steels
- Required chemicals / environment
- None essential
- Influencing parameters
- Long thermal exposure; composition; weld thermal history
- Physical explanation (1–3 processes)
- Metastable carbides decompose
- Graphite precipitates; linked particles/bands weaken the steel
- Signs and symptoms
- Graphite particles or linked HAZ bands; associated loss of strength/toughness
- Prevention / slowing the damage
- Appropriate alloy selection; metallographic surveillance; replace critically affected material
- Typical failure outcome
- Low-ductility rupture
- Possible consequences
- High-energy release; structural failure
- Can be mistaken for
- Graphitic corrosion of cast iron; creep cavities; inclusions
- How to distinguish it
- Identify newly precipitated graphite in steel without selective external iron dissolution
- How often is it seen?
- No representative subtype-specific incidence was identified in the reviewed sources. This is a data gap, not evidence of rarity.
- Historical case / verification status
- No mechanism-attributed catastrophe was verified in the sources reviewed; this does not mean none has occurred.
Photographs — 5 needed (real-life, not diagrams)
Macro / field view
Close-up or micrograph
Cross-section
In-service failure
Distinguishing feature
Sources
- 80 TWI — What is graphitisation? — Technical reference (accessed 2026-09-08)
- 80 TWI — What is type IV cracking, and how is it detected? — Technical reference (accessed 2026-09-08)
Educational synthesis, not a diagnosis or repair instruction. Confirm the actual alloy, environment, loading and damage before selecting mitigation. Generic signs are not unique proof of a mechanism.
DM-063Spheroidization-related thermal softeningCreep & metallurgical ageing · Loss of strengthening microstructure
Mechanism pathway
Service conditions
None essential
Physical processes
- Lamellar cementite changes toward a spheroidal morphology during thermal exposure
- Associated softening can reduce fatigue life at a given stress amplitude
Observable damage
Spheroidized carbides; reduced hardness; changed fatigue response
Possible failure mode
Excessive deformation; later creep rupture or fatigue fracture
- Other names
- Pearlite spheroidization; thermal softening; related carbide-coarsening softening
- Industries / exposed sectors
- Rail transport; hot-service steel equipment
- Typically affected parts
- Railway wheels; other thermally exposed pearlitic-steel parts
- Susceptible materials
- Pearlitic steels; direct study concerns railway wheelset steels
- Required chemicals / environment
- None essential
- Influencing parameters
- Temperature; time; initial microstructure; prior heat treatment
- Physical explanation (1–3 processes)
- Lamellar cementite changes toward a spheroidal morphology during thermal exposure
- Associated softening can reduce fatigue life at a given stress amplitude
- Signs and symptoms
- Spheroidized carbides; reduced hardness; changed fatigue response
- Prevention / slowing the damage
- Limit thermal exposure; correct initial treatment; assess mechanical properties before continued service
- Typical failure outcome
- Excessive deformation; later creep rupture or fatigue fracture
- Possible consequences
- Reduced load/life margin
- Can be mistaken for
- Decarburization; normal annealed structure; graphitization
- How to distinguish it
- Compare carbide morphology and hardness with the original material; distinguish carbon depletion and intentionally spheroidized supply condition
- How often is it seen?
- No representative subtype-specific incidence was identified in the reviewed sources. This is a data gap, not evidence of rarity.
- Historical case / verification status
- No mechanism-attributed catastrophe was verified in the sources reviewed; this does not mean none has occurred.
Photographs — 5 needed (real-life, not diagrams)
Macro / field view
Close-up or micrograph
Cross-section
In-service failure
Distinguishing feature
Sources
- 50 Veolia Water Technologies — Water Handbook, chapter 14: Boiler System Failures — Manufacturer technical handbook (accessed 2026-09-08)
- 80 TWI — Are quenched and tempered steels readily weldable? — Technical reference (accessed 2026-09-08)
- 80 ASM Handbook 4B (2014). Steel Heat Treating Technologies. — Authoritative handbook overview (accessed 2026-09-08)
- 80 Eddy currents and hardness testing for evaluation of steel decarburizing (2006) — publisher abstract and public section snippets (accessed 2026-09-08)
- 80 Thermal softening of fine pearlitic steel and its effect on the fatigue behaviour (2010) — publisher abstract (accessed 2026-09-08)
Educational synthesis, not a diagnosis or repair instruction. Confirm the actual alloy, environment, loading and damage before selecting mitigation. Generic signs are not unique proof of a mechanism.
DM-064Temper embrittlementCreep & metallurgical ageing · Grain-boundary segregation embrittlement
Mechanism pathway
Service conditions
None essential
Physical processes
- Impurities segregate to grain boundaries
- Boundary cohesion decreases and brittle-transition behaviour worsens
Observable damage
Reduced notch toughness; intergranular brittle fracture; little hardness change may occur
Possible failure mode
Brittle fracture, especially during cool/pressurized conditions
- Other names
- Reversible temper embrittlement
- Industries / exposed sectors
- Refining; power; heavy forgings
- Typically affected parts
- Cr-Mo vessels; turbine rotors; thick low-alloy steel
- Susceptible materials
- Susceptible alloy steels with impurity/chemistry combinations
- Required chemicals / environment
- None essential
- Influencing parameters
- Thermal exposure/cooling history; impurity content; alloy composition
- Physical explanation (1–3 processes)
- Impurities segregate to grain boundaries
- Boundary cohesion decreases and brittle-transition behaviour worsens
- Signs and symptoms
- Reduced notch toughness; intergranular brittle fracture; little hardness change may occur
- Prevention / slowing the damage
- Low-impurity suitable steel; qualified heat treatment; toughness assessment and controlled startup
- Typical failure outcome
- Brittle fracture, especially during cool/pressurized conditions
- Possible consequences
- Major pressure-boundary failure
- Can be mistaken for
- Hydrogen embrittlement; irradiation embrittlement; cleavage
- How to distinguish it
- Toughness/transition testing, thermal history and boundary fracture; routine hardness alone is inadequate
- How often is it seen?
- No representative subtype-specific incidence was identified in the reviewed sources. This is a data gap, not evidence of rarity.
- Historical case / verification status
- No mechanism-attributed catastrophe was verified in the sources reviewed; this does not mean none has occurred.
Photographs — 5 needed (real-life, not diagrams)
Macro / field view
Close-up or micrograph
Cross-section
In-service failure
Distinguishing feature
Sources
- 80 TWI — What is temper embrittlement, and how can it be controlled? — Technical reference (accessed 2026-09-08)
- 80 TWI — What is a fracture toughness test? — Technical reference (accessed 2026-09-08)
Educational synthesis, not a diagnosis or repair instruction. Confirm the actual alloy, environment, loading and damage before selecting mitigation. Generic signs are not unique proof of a mechanism.
DM-065475°C embrittlementCreep & metallurgical ageing · Ferrite decomposition embrittlement
Mechanism pathway
Service conditions
None essential
Physical processes
- Ferrite separates into iron-rich and chromium-rich regions
- Nanoscale decomposition hardens and embrittles ferrite
Observable damage
Toughness/ductility loss; hardening; often no obvious optical change
Possible failure mode
Brittle-appearing cracking/fracture
- Other names
- Alpha-prime embrittlement; 885°F embrittlement
- Industries / exposed sectors
- Chemical; power; duplex/high-chromium equipment
- Typically affected parts
- Ferritic/duplex stainless parts; ferrite in weld metal
- Susceptible materials
- Chromium-rich ferrite in ferritic/duplex stainless steels
- Required chemicals / environment
- None essential
- Influencing parameters
- Temperature-time exposure; ferrite composition; initial phase balance
- Physical explanation (1–3 processes)
- Ferrite separates into iron-rich and chromium-rich regions
- Nanoscale decomposition hardens and embrittles ferrite
- Signs and symptoms
- Toughness/ductility loss; hardening; often no obvious optical change
- Prevention / slowing the damage
- Avoid unsuitable thermal exposure; validated material/heat-treatment selection; mechanical-property assessment
- Typical failure outcome
- Brittle-appearing cracking/fracture
- Possible consequences
- Reduced tolerance to defects and transients
- Can be mistaken for
- Sigma embrittlement; strain ageing; HE
- How to distinguish it
- Use exposure history and suitable microstructural/mechanical testing; ordinary optical microscopy may miss nanoscale decomposition
- How often is it seen?
- No representative subtype-specific incidence was identified in the reviewed sources. This is a data gap, not evidence of rarity.
- Historical case / verification status
- No mechanism-attributed catastrophe was verified in the sources reviewed; this does not mean none has occurred.
Photographs — 5 needed (real-life, not diagrams)
Macro / field view
Close-up or micrograph
Cross-section
In-service failure
Distinguishing feature
Sources
- 80 TWI — Embrittlement of austenitic steel welds at high temperature — Technical reference (accessed 2026-09-08)
- 80 TWI — What is temper embrittlement, and how can it be controlled? — Technical reference (accessed 2026-09-08)
- 80 Microstructure evolution and mechanical behavior of a lean duplex stainless steel aged at 475°C (2021) — publisher abstract and public introduction (accessed 2026-09-08)
Educational synthesis, not a diagnosis or repair instruction. Confirm the actual alloy, environment, loading and damage before selecting mitigation. Generic signs are not unique proof of a mechanism.
DM-066Sigma/chi-phase embrittlementCreep & metallurgical ageing · Intermetallic precipitation
Mechanism pathway
Service conditions
None essential; corrosion resistance can deteriorate afterward
Physical processes
- Brittle sigma/chi phases precipitate during unsuitable thermal exposure
- Phase formation changes hardness, toughness and corrosion response
Observable damage
Intermetallic particles; toughness loss; selective corrosion of depleted zones
Possible failure mode
Brittle fracture or subsequent localized-corrosion leak
- Other names
- Intermetallic-phase embrittlement
- Industries / exposed sectors
- Chemical; refining; power; welded stainless equipment
- Typically affected parts
- Duplex components; stainless welds; heat-exchanger parts
- Susceptible materials
- Duplex/austenitic stainless and some high-alloy systems
- Required chemicals / environment
- None essential; corrosion resistance can deteriorate afterward
- Influencing parameters
- Thermal history; Cr/Mo content; phase balance; cooling rate
- Physical explanation (1–3 processes)
- Brittle sigma/chi phases precipitate during unsuitable thermal exposure
- Phase formation changes hardness, toughness and corrosion response
- Signs and symptoms
- Intermetallic particles; toughness loss; selective corrosion of depleted zones
- Prevention / slowing the damage
- Correct welding/heat-treatment windows; qualified phase testing; avoid prolonged unsuitable temperature
- Typical failure outcome
- Brittle fracture or subsequent localized-corrosion leak
- Possible consequences
- Unexpected cracking; reduced corrosion margin
- Can be mistaken for
- 475°C embrittlement; sensitization; carbides
- How to distinguish it
- Identify secondary phases using metallography and suitable compositional analysis; correlate with heat history and mechanical testing
- How often is it seen?
- No representative subtype-specific incidence was identified in the reviewed sources. This is a data gap, not evidence of rarity.
- Historical case / verification status
- No mechanism-attributed catastrophe was verified in the sources reviewed; this does not mean none has occurred.
Photographs — 5 needed (real-life, not diagrams)
Macro / field view
Close-up or micrograph
Cross-section
In-service failure
Distinguishing feature
Sources
- 80 TWI — Embrittlement of austenitic steel welds at high temperature — Technical reference (accessed 2026-09-08)
- 70 AMPP — Intergranular Corrosion — Technical reference (accessed 2026-09-08)
- 80 Ghosh and Mondal (2008) — High temperature ageing behaviour of a duplex stainless steel — publisher abstract and public introduction (accessed 2026-09-08)
Educational synthesis, not a diagnosis or repair instruction. Confirm the actual alloy, environment, loading and damage before selecting mitigation. Generic signs are not unique proof of a mechanism.
DM-067Strain-ageing embrittlementCreep & metallurgical ageing · Interstitial/dislocation interaction
Mechanism pathway
Service conditions
None essential
Physical processes
- Carbon/nitrogen segregate to dislocations
- Dislocation pinning raises yield response and can reduce ductility/toughness
Observable damage
Yield-point return; hardness/strength increase; toughness loss
Possible failure mode
Low-ductility cracking or fracture
- Other names
- Static strain ageing; strain aging
- Industries / exposed sectors
- Structural steel; fabrication; pipelines
- Typically affected parts
- Cold-worked/bent plates; formed parts; strain-hardened regions
- Susceptible materials
- Susceptible ferritic steels containing mobile carbon/nitrogen
- Required chemicals / environment
- None essential
- Influencing parameters
- Prior plastic strain; ageing time/temperature; free interstitial content
- Physical explanation (1–3 processes)
- Carbon/nitrogen segregate to dislocations
- Dislocation pinning raises yield response and can reduce ductility/toughness
- Signs and symptoms
- Yield-point return; hardness/strength increase; toughness loss
- Prevention / slowing the damage
- Suitable killed/low-free-interstitial steel; control cold work; qualified processing and toughness checks
- Typical failure outcome
- Low-ductility cracking or fracture
- Possible consequences
- Reduced forming/service margin
- Can be mistaken for
- Temper embrittlement; cold-work hardening alone; HE
- How to distinguish it
- Compare prestrain/ageing history and mechanical response; do not infer from hardness alone
- How often is it seen?
- No representative subtype-specific incidence was identified in the reviewed sources. This is a data gap, not evidence of rarity.
- Historical case / verification status
- No mechanism-attributed catastrophe was verified in the sources reviewed; this does not mean none has occurred.
Photographs — 5 needed (real-life, not diagrams)
Macro / field view
Close-up or micrograph
Cross-section
In-service failure
Distinguishing feature
Sources
- 80 TWI — Why must aluminium content exceed twice the nitrogen content? — Technical reference (accessed 2026-09-08)
- 80 TWI — Weldability of materials: carbon manganese and low alloy steels, Job Knowledge 19 — Technical reference (accessed 2026-09-08)
Educational synthesis, not a diagnosis or repair instruction. Confirm the actual alloy, environment, loading and damage before selecting mitigation. Generic signs are not unique proof of a mechanism.
DM-068Neutron irradiation embrittlementCreep & metallurgical ageing · Radiation-induced microstructural damage
Mechanism pathway
Service conditions
None chemically essential; energetic-neutron exposure
Physical processes
- Neutron exposure changes the steel microstructure
- Fracture toughness decreases, increasing sensitivity to existing flaws
Observable damage
Toughness/impact-property deterioration in surveillance specimens
Possible failure mode
Brittle fracture if loading exceeds degraded resistance
- Other names
- Radiation embrittlement; vessel embrittlement
- Industries / exposed sectors
- Nuclear power
- Typically affected parts
- Reactor-vessel beltline and welds; irradiated structural parts
- Susceptible materials
- Reactor pressure-vessel steels and welds
- Required chemicals / environment
- None chemically essential; energetic-neutron exposure
- Influencing parameters
- Neutron fluence/flux; exposure temperature; steel chemistry and heat treatment
- Physical explanation (1–3 processes)
- Neutron exposure changes the steel microstructure
- Fracture toughness decreases, increasing sensitivity to existing flaws
- Signs and symptoms
- Toughness/impact-property deterioration in surveillance specimens
- Prevention / slowing the damage
- Material surveillance, fluence and operating-envelope assessment; approved vessel-integrity programs
- Typical failure outcome
- Brittle fracture if loading exceeds degraded resistance
- Possible consequences
- Pressure-boundary safety challenge
- Can be mistaken for
- Temper embrittlement; IASCC; ordinary thermal ageing
- How to distinguish it
- Use dosimetry/surveillance and toughness data; IASCC additionally needs an environment-assisted crack process
- How often is it seen?
- No representative subtype-specific incidence was identified in the reviewed sources. This is a data gap, not evidence of rarity.
- Historical case / verification status
- No mechanism-attributed catastrophe was verified in the sources reviewed; this does not mean none has occurred.
Photographs — 5 needed (real-life, not diagrams)
Macro / field view
Close-up or micrograph
Cross-section
In-service failure
Distinguishing feature
Sources
- 80 NRC — Reactor Vessel Integrity — Regulatory technical reference (accessed 2026-09-08)
- 80 Chen, Y., Chopra, O.K., Gruber, E.E. & Shack, W.J. (2010). NUREG/CR-7018, irradiation-assisted stress corrosion cracking. NRC / Argonne. — Primary institutional research abstract (accessed 2026-09-08)
Educational synthesis, not a diagnosis or repair instruction. Confirm the actual alloy, environment, loading and damage before selecting mitigation. Generic signs are not unique proof of a mechanism.
DM-069High-cycle fatigueFatigue · Cyclic crack initiation and growth
Mechanism pathway
Service conditions
None essential; corrosion can accelerate growth
Physical processes
- Localized cyclic slip initiates a crack
- Repeated loading grows it until remaining section fails
Observable damage
Progressive crack growth; striations in some materials; visual inspection can miss tight cracks
Possible failure mode
Final break; occasionally leak before break
- Other names
- HCF; nominally elastic fatigue
- Industries / exposed sectors
- Rotating machinery; transport; aerospace; structures
- Typically affected parts
- Shafts; weld toes; blades; bolts; structural joints
- Susceptible materials
- Most engineering metals
- Required chemicals / environment
- None essential; corrosion can accelerate growth
- Influencing parameters
- Stress range/mean; cycles; notch geometry; residual stress; surface defects
- Physical explanation (1–3 processes)
- Localized cyclic slip initiates a crack
- Repeated loading grows it until remaining section fails
- Signs and symptoms
- Progressive crack growth; striations in some materials; visual inspection can miss tight cracks
- Prevention / slowing the damage
- Reduce stress concentration and cyclic loads; improve surface/joint quality; damage-tolerant inspection
- Typical failure outcome
- Final break; occasionally leak before break
- Possible consequences
- Rotor/structure failure; shutdown; injury potential
- Can be mistaken for
- LCF; vibration fatigue; SCC; overload
- How to distinguish it
- Fractography plus stress/cycle reconstruction; no beach marks does not exclude fatigue
- How often is it seen?
- DNV reports fatigue as 30% of >1,000 oil/gas-maritime investigations; it does not disclose an HCF-only percentage. Do not assign 30% to this subtype.
- Historical case / verification status
- Aloha Flight 243 (1988): undetected fatigue/disbonding caused fuselage separation and one fatality. This is a verified fatigue example; the cited accident summary does not classify local HCF versus LCF strain.
Photographs — 5 needed (real-life, not diagrams)
Macro / field view
Close-up or micrograph
Cross-section
In-service failure
Distinguishing feature
Sources
- 80 TWI — What is fatigue failure and how can it be avoided? — Technical reference (accessed 2026-09-08)
- 80 ASTM E466-21 — Force Controlled Constant Amplitude Axial Fatigue Tests of Metallic Materials — Official public standard scope (accessed 2026-09-08)
- 80 TWI — What is peening? — Technical reference (accessed 2026-09-08)
- 80 NTSB — Aloha Airlines Flight 243, Boeing 737-200, N73711; DCA88MA054 — Primary accident investigation (accessed 2026-09-08)
- 70 DNV (2020) — Tubes and piping are most failure-prone components in oil and gas and maritime industries — Primary investigation-cohort summary (accessed 2026-09-08)
- 80 Fatigue crack nucleation in iron and a high strength low alloy steel (2001) — publisher abstract and public section snippets (accessed 2026-09-08)
- 80 Fractography survey on high cycle fatigue failure in Fe–C–Cr–Mo–X alloys (2007) — publisher abstract (accessed 2026-09-08)
Educational synthesis, not a diagnosis or repair instruction. Confirm the actual alloy, environment, loading and damage before selecting mitigation. Generic signs are not unique proof of a mechanism.
DM-070Low-cycle fatigueFatigue · Cyclic plastic deformation
Mechanism pathway
Service conditions
None essential
Physical processes
- Repeated plastic strain localizes damage
- Cracks propagate under successive large strain excursions
Observable damage
Fatigue cracks associated with cyclic plastic strain; cyclic hardening/softening can occur
Possible failure mode
Fracture or through-wall leak
- Other names
- LCF; plastic-strain fatigue
- Industries / exposed sectors
- Power cycling; aerospace; pressure equipment
- Typically affected parts
- Notches; vessel/nozzle transitions; turbine discs; highly strained joints
- Susceptible materials
- Structural metals; direct cited experiments used 42CrMo4 steel
- Required chemicals / environment
- None essential
- Influencing parameters
- Plastic strain range; mean strain; cycles; temperature; hold time
- Physical explanation (1–3 processes)
- Repeated plastic strain localizes damage
- Cracks propagate under successive large strain excursions
- Signs and symptoms
- Fatigue cracks associated with cyclic plastic strain; cyclic hardening/softening can occur
- Prevention / slowing the damage
- Limit strain concentration and severe transients; strain-based design; suitable material and inspection
- Typical failure outcome
- Fracture or through-wall leak
- Possible consequences
- Loss of containment or load capacity
- Can be mistaken for
- HCF; ratcheting; creep-fatigue
- How to distinguish it
- Reconstruct local strain history and crack growth; cycle count alone does not distinguish the fatigue regime
- How often is it seen?
- No representative subtype-specific incidence was identified in the reviewed sources. This is a data gap, not evidence of rarity.
- Historical case / verification status
- No mechanism-attributed catastrophe was verified in the sources reviewed; this does not mean none has occurred.
Photographs — 5 needed (real-life, not diagrams)
Macro / field view
Close-up or micrograph
Cross-section
In-service failure
Distinguishing feature
Sources
- 80 ASTM E606/E606M-21 — Strain-Controlled Fatigue Testing — Official public standard scope (accessed 2026-09-08)
- 80 TWI — Fatigue Analysis — Technical reference (accessed 2026-09-08)
- 80 Saravanan, M., Raghava, G., Vishnuvardhan, S. & Samuel Knight, G.M. Fatigue ratcheting studies on pressurised stainless steel straight pipes. Journal of Structural Engineering. — Primary experimental paper abstract (accessed 2026-09-08)
- 80 Creep-fatigue interaction behaviour of type 308 stainless steel weld metal and type 304 stainless steel base metal (1993) — publisher abstract (accessed 2026-09-08)
- 80 Plastic strain-controlled short crack growth and fatigue life — publisher abstract and public section snippets (accessed 2026-09-08)
Educational synthesis, not a diagnosis or repair instruction. Confirm the actual alloy, environment, loading and damage before selecting mitigation. Generic signs are not unique proof of a mechanism.
DM-071Very-high-cycle fatigueFatigue · Long-life fatigue regime
Mechanism pathway
Service conditions
None essential
Physical processes
- Small defects or microstructural regions initiate cracks after long cycling
- Internal cracks may grow into fish-eye/FGA features before final fracture
Observable damage
Internal origins; fish-eye regions in some alloys; absence does not exclude VHCF
Possible failure mode
Unexpected fracture
- Other names
- VHCF; gigacycle fatigue
- Industries / exposed sectors
- Aerospace; bearings; rail; high-speed machinery
- Typically affected parts
- Shafts; bearings; high-cycle loaded internal defects
- Susceptible materials
- High-strength steels; titanium/aluminium and other alloys
- Required chemicals / environment
- None essential
- Influencing parameters
- Very large cycle counts; inclusion size/location; stress gradient; surface condition
- Physical explanation (1–3 processes)
- Small defects or microstructural regions initiate cracks after long cycling
- Internal cracks may grow into fish-eye/FGA features before final fracture
- Signs and symptoms
- Internal origins; fish-eye regions in some alloys; absence does not exclude VHCF
- Prevention / slowing the damage
- Control inclusions/defects; use applicable long-life data; do not assume universal infinite endurance
- Typical failure outcome
- Unexpected fracture
- Possible consequences
- High-speed component failure
- Can be mistaken for
- HCF; inclusion-origin overload; hydrogen-assisted fatigue
- How to distinguish it
- Fractography of origin plus demonstrated loading duration/cycles; fish-eye is not universal
- How often is it seen?
- No representative subtype-specific incidence was identified in the reviewed sources. This is a data gap, not evidence of rarity.
- Historical case / verification status
- No mechanism-attributed catastrophe was verified in the sources reviewed; this does not mean none has occurred.
Photographs — 5 needed (real-life, not diagrams)
Macro / field view
Close-up or micrograph
Cross-section
In-service failure
Distinguishing feature
Sources
- 80 Subsurface crack initiation and propagation mechanisms in gigacycle fatigue (2010). Acta Materialia 58(18), 6046–6054. — Primary research paper (accessed 2026-09-08)
- 80 Influence of Non-Metallic Inclusions on Very High-Cycle Fatigue Performance of High-Strength Steels and Interpretation via Crystal Plasticity Finite Element Method (2024). Metals 14(8), 948. — Primary experimental paper (accessed 2026-09-08)
Educational synthesis, not a diagnosis or repair instruction. Confirm the actual alloy, environment, loading and damage before selecting mitigation. Generic signs are not unique proof of a mechanism.
DM-072Thermal fatigueFatigue · Temperature-gradient-driven fatigue
Mechanism pathway
Service conditions
None essential
Physical processes
- Nonuniform thermal expansion creates cyclic stress/strain
- Repeated local strain initiates and advances cracks
Observable damage
Surface crack networks; cracks at thermal mixing or gradients
Possible failure mode
Leak or fracture
- Other names
- Thermal cycling damage; heat checking
- Industries / exposed sectors
- Power; nuclear; refining; tooling
- Typically affected parts
- Mixing tees; boiler ligaments; dies; hot/cold interfaces
- Susceptible materials
- Steels; cast irons; stainless and heat-resistant alloys
- Required chemicals / environment
- None essential
- Influencing parameters
- Temperature swing; gradient; ramp rate; restraint; cycle count
- Physical explanation (1–3 processes)
- Nonuniform thermal expansion creates cyclic stress/strain
- Repeated local strain initiates and advances cracks
- Signs and symptoms
- Surface crack networks; cracks at thermal mixing or gradients
- Prevention / slowing the damage
- Reduce gradients/ramp severity; improve mixing/design; compatible expansion; inspect hot spots
- Typical failure outcome
- Leak or fracture
- Possible consequences
- Hot-fluid release; tool or plant outage
- Can be mistaken for
- Thermal shock; mechanical fatigue; chloride SCC
- How to distinguish it
- Correlate crack map with thermal transients and restraint; test for corrosive species when plausible
- How often is it seen?
- No representative subtype-specific incidence was identified in the reviewed sources. This is a data gap, not evidence of rarity.
- Historical case / verification status
- No mechanism-attributed catastrophe was verified in the sources reviewed; this does not mean none has occurred.
Photographs — 5 needed (real-life, not diagrams)
Macro / field view
Close-up or micrograph
Cross-section
In-service failure
Distinguishing feature
Sources
- 80 TWI — Examination of cracking in boiler tubes — Primary failure investigation (accessed 2026-09-08)
- 80 TWI (2025) — Numerical Modelling of Thermal Fatigue at Pipe Mixing Points in Nuclear Power Plants — Primary research summary (accessed 2026-09-08)
- 80 TWI — A review of ball grid arrays for electronic assembly (1998) — Technical research paper (accessed 2026-09-08)
Educational synthesis, not a diagnosis or repair instruction. Confirm the actual alloy, environment, loading and damage before selecting mitigation. Generic signs are not unique proof of a mechanism.
DM-073Corrosion fatigueFatigue · Corrosion/cycle interaction
Mechanism pathway
Service conditions
Corrosive environment plus cyclic loading
Physical processes
- Corrosion pits/film breakdown accelerate initiation
- Environment-assisted crack growth combines with cyclic loading
Observable damage
Pit-origin or multiple cracks; corroded fracture features
Possible failure mode
Break or leak
- Other names
- Environment-assisted fatigue
- Industries / exposed sectors
- Offshore; marine; pipelines; pumps; power
- Typically affected parts
- Welded risers; shafts; wet cyclically loaded joints
- Susceptible materials
- Steels; aluminium and other engineering alloys
- Required chemicals / environment
- Corrosive environment plus cyclic loading
- Influencing parameters
- Frequency; stress range; electrochemical potential; pH; hydrogen; temperature
- Physical explanation (1–3 processes)
- Corrosion pits/film breakdown accelerate initiation
- Environment-assisted crack growth combines with cyclic loading
- Signs and symptoms
- Pit-origin or multiple cracks; corroded fracture features
- Prevention / slowing the damage
- Control both corrosion and cyclic stress; compatible protection; environment-specific fatigue assessment
- Typical failure outcome
- Break or leak
- Possible consequences
- Loss of structure/containment
- Can be mistaken for
- SCC; dry fatigue; hydrogen-assisted cracking
- How to distinguish it
- Demonstrate cyclic loading and exposure; growth behaviour/frequency effects help separate from sustained-load SCC
- How often is it seen?
- No representative subtype-specific incidence was identified in the reviewed sources. This is a data gap, not evidence of rarity.
- Historical case / verification status
- No mechanism-attributed catastrophe was verified in the sources reviewed; this does not mean none has occurred.
Photographs — 5 needed (real-life, not diagrams)
Macro / field view
Close-up or micrograph
Cross-section
In-service failure
Distinguishing feature
Sources
- 80 TWI — Corrosion fatigue behaviour of welded risers and pipelines (June 2007) — Technical research paper (accessed 2026-09-08)
- 80 TWI — Corrosion of welded components in marine environments (April 2003) — Technical research paper (accessed 2026-09-08)
Educational synthesis, not a diagnosis or repair instruction. Confirm the actual alloy, environment, loading and damage before selecting mitigation. Generic signs are not unique proof of a mechanism.
DM-074Fretting fatigueFatigue · Oscillatory-contact fatigue
Mechanism pathway
Service conditions
None essential; oxidation often accompanies fretting
Physical processes
- Oscillatory contact creates high local tractions and surface damage
- Cracks initiate near contact edges and grow under cyclic bulk loading
Observable damage
Contact-edge cracks; polished/dark wear patches; oxide debris
Possible failure mode
Fatigue break
- Other names
- Contact-assisted fatigue
- Industries / exposed sectors
- Aerospace; turbines; rail; rotating machinery
- Typically affected parts
- Blade roots; press fits; bolted joints; splines
- Susceptible materials
- Steels; titanium; aluminium and other metallic contacts
- Required chemicals / environment
- None essential; oxidation often accompanies fretting
- Influencing parameters
- Microslip; contact pressure; bulk cyclic stress; contact geometry
- Physical explanation (1–3 processes)
- Oscillatory contact creates high local tractions and surface damage
- Cracks initiate near contact edges and grow under cyclic bulk loading
- Signs and symptoms
- Contact-edge cracks; polished/dark wear patches; oxide debris
- Prevention / slowing the damage
- Manage contact geometry/preload and microslip; qualified coatings/lubrication; appropriate material pairing
- Typical failure outcome
- Fatigue break
- Possible consequences
- Blade/shaft/joint failure
- Can be mistaken for
- Fretting wear alone; ordinary fatigue; corrosion fatigue
- How to distinguish it
- Locate fatigue origin at the contact edge and establish small-amplitude slip plus cyclic stress
- How often is it seen?
- No representative subtype-specific incidence was identified in the reviewed sources. This is a data gap, not evidence of rarity.
- Historical case / verification status
- No mechanism-attributed catastrophe was verified in the sources reviewed; this does not mean none has occurred.
Photographs — 5 needed (real-life, not diagrams)
Macro / field view
Close-up or micrograph
Cross-section
In-service failure
Distinguishing feature
Sources
- 80 ASTM E2789-10(2021) — Fretting Fatigue Testing — Official public standard scope (accessed 2026-09-08)
- 50 SKF (2011) — Golden opportunities — Primary manufacturer technical analysis (accessed 2026-09-08)
Educational synthesis, not a diagnosis or repair instruction. Confirm the actual alloy, environment, loading and damage before selecting mitigation. Generic signs are not unique proof of a mechanism.
DM-075Rolling-contact fatigueFatigue · Repeated Hertzian-contact fatigue
Mechanism pathway
Service conditions
None essential; lubricant contamination and water modify severity
Physical processes
- Repeated contact shear initiates surface or subsurface cracks
- Cracks link to release flakes/spalls
Observable damage
Pitting/spalling on contact tracks; vibration; debris
Possible failure mode
Bearing wear-out or seizure; possible secondary fracture
- Other names
- RCF; contact spalling; surface/subsurface fatigue
- Industries / exposed sectors
- Bearings; gears; rail; wind turbines
- Typically affected parts
- Raceways; rolling elements; gear flanks; wheel/rail contacts
- Susceptible materials
- Bearing/gear steels; surface-hardened contact materials
- Required chemicals / environment
- None essential; lubricant contamination and water modify severity
- Influencing parameters
- Contact stress; lubrication; roughness; inclusions; alignment; cycles
- Physical explanation (1–3 processes)
- Repeated contact shear initiates surface or subsurface cracks
- Cracks link to release flakes/spalls
- Signs and symptoms
- Pitting/spalling on contact tracks; vibration; debris
- Prevention / slowing the damage
- Correct load/alignment; clean adequate lubricant; suitable hardness/cleanliness; condition monitoring
- Typical failure outcome
- Bearing wear-out or seizure; possible secondary fracture
- Possible consequences
- Machine failure; secondary damage
- Can be mistaken for
- Electrical erosion; indentation; abrasive wear
- How to distinguish it
- Cross-section and microscopy locate crack origins; compare with fluting/melt craters and contamination
- How often is it seen?
- SKF (2022) assigns 16% of identified bearing failure modes to surface-initiated fatigue. This is not the fraction for all RCF or the probability a bearing will fail.
- Historical case / verification status
- No mechanism-attributed catastrophe was verified in the sources reviewed; this does not mean none has occurred.
Photographs — 5 needed (real-life, not diagrams)
Macro / field view
Close-up or micrograph
Cross-section
In-service failure
Distinguishing feature
Sources
- 50 SKF (2019) — Wear and surface fatigue in rolling bearings — Primary manufacturer research (accessed 2026-09-08)
- 50 SKF (2022) — Bearing damage analysis: ISO 15243 is here to help you — Primary manufacturer investigation dataset (accessed 2026-09-08)
Educational synthesis, not a diagnosis or repair instruction. Confirm the actual alloy, environment, loading and damage before selecting mitigation. Generic signs are not unique proof of a mechanism.
DM-076Vibration-induced fatigueFatigue · Dynamically excited fatigue
Mechanism pathway
Service conditions
None essential
Physical processes
- Dynamic excitation creates repeated stress
- Local fatigue cracks grow, often at branch or weld notches
Observable damage
Cracks near supports/branches; vibration; intermittent leakage
Possible failure mode
Through-wall leak or fatigue break
- Other names
- VIF; acoustic/pulsation-induced fatigue
- Industries / exposed sectors
- Process piping; rotating machinery; aerospace
- Typically affected parts
- Small-bore branches; instrument connections; supports; compressor lines
- Susceptible materials
- Metals, especially welded/stress-concentrated details
- Required chemicals / environment
- None essential
- Influencing parameters
- Excitation frequency/amplitude; resonance; damping; support stiffness; weld geometry
- Physical explanation (1–3 processes)
- Dynamic excitation creates repeated stress
- Local fatigue cracks grow, often at branch or weld notches
- Signs and symptoms
- Cracks near supports/branches; vibration; intermittent leakage
- Prevention / slowing the damage
- Measure excitation; address resonance/source; engineer supports; avoid merely adding unassessed restraints
- Typical failure outcome
- Through-wall leak or fatigue break
- Possible consequences
- Process release; detached parts
- Can be mistaken for
- Other HCF; thermal fatigue; overload
- How to distinguish it
- Operating vibration/modal measurements plus fracture origin; a vibrating component is not proof of causal fatigue
- How often is it seen?
- No representative subtype-specific incidence was identified in the reviewed sources. This is a data gap, not evidence of rarity.
- Historical case / verification status
- No mechanism-attributed catastrophe was verified in the sources reviewed; this does not mean none has occurred.
Photographs — 5 needed (real-life, not diagrams)
Macro / field view
Close-up or micrograph
Cross-section
In-service failure
Distinguishing feature
Sources
- 80 TWI — Fatigue Analysis — Technical reference (accessed 2026-09-08)
- 80 TWI — Comparison of fatigue of girth welds in full-scale pipes and small-scale strip specimens — Primary research paper (accessed 2026-09-08)
- 80 ASTM E466-21 — Force Controlled Constant Amplitude Axial Fatigue Tests of Metallic Materials — Official public standard scope (accessed 2026-09-08)
Educational synthesis, not a diagnosis or repair instruction. Confirm the actual alloy, environment, loading and damage before selecting mitigation. Generic signs are not unique proof of a mechanism.
DM-077Thermomechanical fatigueFatigue · Coupled thermal/mechanical cycling
Mechanism pathway
Service conditions
None essential; oxidation can interact
Physical processes
- Mechanical and thermal strains cycle with a defined phase relationship
- Temperature-dependent plasticity, oxidation and sometimes creep interact
Observable damage
Surface cracks; oxide-assisted cracking; evolving cyclic response
Possible failure mode
Cracking or fracture
- Other names
- TMF; in-phase/out-of-phase TMF
- Industries / exposed sectors
- Turbines; engines; aerospace; high-temperature power
- Typically affected parts
- Hot-section blades; exhaust manifolds; constrained heated parts
- Susceptible materials
- Superalloys; heat-resistant steels; other thermally cycled metals
- Required chemicals / environment
- None essential; oxidation can interact
- Influencing parameters
- Temperature/strain phasing; mechanical strain range; dwell; gradient
- Physical explanation (1–3 processes)
- Mechanical and thermal strains cycle with a defined phase relationship
- Temperature-dependent plasticity, oxidation and sometimes creep interact
- Signs and symptoms
- Surface cracks; oxide-assisted cracking; evolving cyclic response
- Prevention / slowing the damage
- Reduce thermal/mechanical strain mismatch; design for actual phase history; qualified coatings and life models
- Typical failure outcome
- Cracking or fracture
- Possible consequences
- Engine/turbine loss of function; outage
- Can be mistaken for
- Thermal fatigue; isothermal LCF; creep-fatigue
- How to distinguish it
- Reconstruct mechanical strain separately from free thermal strain and establish phasing; damage morphology alone is insufficient
- How often is it seen?
- No representative subtype-specific incidence was identified in the reviewed sources. This is a data gap, not evidence of rarity.
- Historical case / verification status
- No mechanism-attributed catastrophe was verified in the sources reviewed; this does not mean none has occurred.
Photographs — 5 needed (real-life, not diagrams)
Macro / field view
Close-up or micrograph
Cross-section
In-service failure
Distinguishing feature
Sources
- 80 ASTM E2368-25 — Strain Controlled Thermomechanical Fatigue Testing — Official public standard scope (accessed 2026-09-08)
- 80 TWI — What is a thermal barrier coating? — Technical reference (accessed 2026-09-08)
- 80 TWI — What are the limiting factors in gas turbine hot section components? — Technical reference (accessed 2026-09-08)
Educational synthesis, not a diagnosis or repair instruction. Confirm the actual alloy, environment, loading and damage before selecting mitigation. Generic signs are not unique proof of a mechanism.
DM-078Adhesive wear and gallingWear, flow & surface damage · Sliding-contact damage
Mechanism pathway
Service conditions
None essential; lubricant failure increases risk
Physical processes
- Asperities form adhesive junctions
- Junction tearing transfers metal; severe interaction can seize contact
Observable damage
Smeared/transferred metal; torn surfaces; rising friction
Possible failure mode
Seizure; leakage; secondary break
- Other names
- Scuffing; seizure; adhesive transfer
- Industries / exposed sectors
- Fasteners; valves; pumps; machinery
- Typically affected parts
- Threads; valve trim; sliding guides; wear rings
- Susceptible materials
- Metal couples, including stainless and titanium pairs
- Required chemicals / environment
- None essential; lubricant failure increases risk
- Influencing parameters
- Contact load; sliding; material pairing; roughness; lubrication; alignment
- Physical explanation (1–3 processes)
- Asperities form adhesive junctions
- Junction tearing transfers metal; severe interaction can seize contact
- Signs and symptoms
- Smeared/transferred metal; torn surfaces; rising friction
- Prevention / slowing the damage
- Compatible material pair/coating; correct lubrication; alignment; controlled assembly
- Typical failure outcome
- Seizure; leakage; secondary break
- Possible consequences
- Loss of motion/isolation; machine outage
- Can be mistaken for
- Abrasive wear; overheating; fretting wear
- How to distinguish it
- Look for metal transfer and torn junctions, not solely parallel scratches; inspect mating surface
- How often is it seen?
- SKF (2022): adhesive wear is 7% of identified bearing failure modes. This bearing-cohort result is not a galling incidence across all industries.
- Historical case / verification status
- No mechanism-attributed catastrophe was verified in the sources reviewed; this does not mean none has occurred.
Photographs — 5 needed (real-life, not diagrams)
Macro / field view
Close-up or micrograph
Cross-section
In-service failure
Distinguishing feature
Sources
- 80 ASTM G98-23 — Galling Resistance of Materials — Official public standard scope (accessed 2026-09-08)
- 50 SKF (2022) — Bearing damage analysis: ISO 15243 is here to help you — Primary manufacturer investigation dataset (accessed 2026-09-08)
Educational synthesis, not a diagnosis or repair instruction. Confirm the actual alloy, environment, loading and damage before selecting mitigation. Generic signs are not unique proof of a mechanism.
DM-079Abrasive wearWear, flow & surface damage · Hard-particle/asperity wear
Mechanism pathway
Service conditions
No reactive chemical required; hard particles/asperities are necessary
Physical processes
- Hard particles cut or plough a surface
- Repeated contact removes or displaces material
Observable damage
Grooves; polishing; dimensional loss; embedded particles
Possible failure mode
Wear-out; excessive clearance; eventual leak or break
- Other names
- Two-body/three-body abrasion; scratching wear
- Industries / exposed sectors
- Mining; earthmoving; cement; bearings; machinery
- Typically affected parts
- Liners; chutes; tools; seals; contaminated bearings
- Susceptible materials
- Most metals; resistance depends on hardness, toughness and microstructure
- Required chemicals / environment
- No reactive chemical required; hard particles/asperities are necessary
- Influencing parameters
- Particle hardness/shape/size; load; sliding distance; impact
- Physical explanation (1–3 processes)
- Hard particles cut or plough a surface
- Repeated contact removes or displaces material
- Signs and symptoms
- Grooves; polishing; dimensional loss; embedded particles
- Prevention / slowing the damage
- Exclude/filter abrasives; wear-resistant surfaces; suitable hardness-toughness balance; replaceable liners
- Typical failure outcome
- Wear-out; excessive clearance; eventual leak or break
- Possible consequences
- Reduced efficiency; contamination; downtime
- Can be mistaken for
- Adhesive wear; solid-particle erosion; machining marks
- How to distinguish it
- Match groove/particle geometry and relative motion; analyse debris and contact conditions
- How often is it seen?
- SKF (2022): abrasive wear is 26% of identified bearing failure modes, highest in its displayed dataset. Sample size and observation period are not disclosed.
- Historical case / verification status
- No mechanism-attributed catastrophe was verified in the sources reviewed; this does not mean none has occurred.
Photographs — 5 needed (real-life, not diagrams)
Macro / field view
Close-up or micrograph
Cross-section
In-service failure
Distinguishing feature
Sources
- 80 ASTM G65-16(2021) — Abrasion Using the Dry Sand/Rubber Wheel Apparatus — Official public standard scope (accessed 2026-09-08)
- 50 SKF (2019) — Wear and surface fatigue in rolling bearings — Primary manufacturer research (accessed 2026-09-08)
- 50 SKF (2022) — Bearing damage analysis: ISO 15243 is here to help you — Primary manufacturer investigation dataset (accessed 2026-09-08)
Educational synthesis, not a diagnosis or repair instruction. Confirm the actual alloy, environment, loading and damage before selecting mitigation. Generic signs are not unique proof of a mechanism.
DM-080Fretting wearWear, flow & surface damage · Small-amplitude contact wear
Mechanism pathway
Service conditions
No reactive species essential; air/moisture commonly oxidize debris
Physical processes
- Oscillatory slip removes surface films and material
- Wear debris oxidizes and can act as abrasive
Observable damage
Red/brown or dark debris; localized wear scars; roller-spaced marks
Possible failure mode
Loss of fit or wear-out; possible later fatigue break
- Other names
- Fretting corrosion; false brinelling in some bearing contexts
- Industries / exposed sectors
- Bearings; turbines; transport; electrical/mechanical joints
- Typically affected parts
- Press fits; shaft seats; parked bearings; connectors
- Susceptible materials
- Metallic contacting surfaces
- Required chemicals / environment
- No reactive species essential; air/moisture commonly oxidize debris
- Influencing parameters
- Microslip amplitude; contact pressure; vibration; lubrication
- Physical explanation (1–3 processes)
- Oscillatory slip removes surface films and material
- Wear debris oxidizes and can act as abrasive
- Signs and symptoms
- Red/brown or dark debris; localized wear scars; roller-spaced marks
- Prevention / slowing the damage
- Control unwanted microslip/vibration; appropriate fit/preload; lubrication and storage/transport measures
- Typical failure outcome
- Loss of fit or wear-out; possible later fatigue break
- Possible consequences
- Misalignment; vibration; reduced joint reliability
- Can be mistaken for
- Fretting fatigue; true brinelling; electrical fluting
- How to distinguish it
- Confirm oscillatory contact wear; section for fatigue cracks; plastic indentations without wear suggest brinelling
- How often is it seen?
- No representative subtype-specific incidence was identified in the reviewed sources. This is a data gap, not evidence of rarity.
- Historical case / verification status
- No mechanism-attributed catastrophe was verified in the sources reviewed; this does not mean none has occurred.
Photographs — 5 needed (real-life, not diagrams)
Macro / field view
Close-up or micrograph
Cross-section
In-service failure
Distinguishing feature
Sources
- 50 SKF (2011) — Golden opportunities — Primary manufacturer technical analysis (accessed 2026-09-08)
- 50 SKF (2019) — Wear and surface fatigue in rolling bearings — Primary manufacturer research (accessed 2026-09-08)
- 80 ASTM E2789-10(2021) — Fretting Fatigue Testing — Official public standard scope (accessed 2026-09-08)
Educational synthesis, not a diagnosis or repair instruction. Confirm the actual alloy, environment, loading and damage before selecting mitigation. Generic signs are not unique proof of a mechanism.
DM-081Solid-particle erosionWear, flow & surface damage · Impact-driven material removal
Mechanism pathway
Service conditions
No corrosive chemical required; impinging particles in gas/flow
Physical processes
- Particle impacts cut/plough ductile surfaces or fracture brittle regions
Observable damage
Directional wastage; impact craters; leading-edge thinning
Possible failure mode
Perforation; blade loss; wear-out
- Other names
- Particle impingement erosion; gas-borne erosion
- Industries / exposed sectors
- Power; mining; pneumatic conveying; turbines
- Typically affected parts
- Duct bends; boiler tubes; turbine blades; chutes
- Susceptible materials
- Engineering metals and coatings
- Required chemicals / environment
- No corrosive chemical required; impinging particles in gas/flow
- Influencing parameters
- Velocity; impact angle; particle size/shape/hardness; temperature
- Physical explanation (1–3 processes)
- Particle impacts cut/plough ductile surfaces or fracture brittle regions
- Signs and symptoms
- Directional wastage; impact craters; leading-edge thinning
- Prevention / slowing the damage
- Reduce particle loading/velocity; improve flow path; resistant liners/coatings; targeted inspections
- Typical failure outcome
- Perforation; blade loss; wear-out
- Possible consequences
- Release; turbine/boiler damage; downtime
- Can be mistaken for
- Slurry erosion; corrosion thinning; abrasion
- How to distinguish it
- Identify particles and impact trajectories; compare sheltered and impinged locations
- How often is it seen?
- No representative subtype-specific incidence was identified in the reviewed sources. This is a data gap, not evidence of rarity.
- Historical case / verification status
- No mechanism-attributed catastrophe was verified in the sources reviewed; this does not mean none has occurred.
Photographs — 5 needed (real-life, not diagrams)
Macro / field view
Close-up or micrograph
Cross-section
In-service failure
Distinguishing feature
Sources
- 80 ASTM G76-26 — Erosion Tests by Solid Particle Impingement Using Gas Jets — Official public standard scope (accessed 2026-09-08)
- 80 TWI — What are the limiting factors in gas turbine hot section components? — Technical reference (accessed 2026-09-08)
Educational synthesis, not a diagnosis or repair instruction. Confirm the actual alloy, environment, loading and damage before selecting mitigation. Generic signs are not unique proof of a mechanism.
DM-082Slurry erosionWear, flow & surface damage · Liquid-borne particle damage
Mechanism pathway
Service conditions
Liquid carrying hard solids; corrosive liquid may add synergy
Physical processes
- Liquid carries particles into sliding/impact contact
- Cutting, ploughing or repeated impact removes metal
Observable damage
Localized grooves; impeller/outer-bend loss; dimensional wear
Possible failure mode
Leak; loss of pump performance; rupture
- Other names
- Slurry abrasion; solids-in-liquid wear
- Industries / exposed sectors
- Mining; dredging; mineral processing; slurry transport
- Typically affected parts
- Pump impellers; elbows; valves; liners
- Susceptible materials
- Steels; cast irons; alloys; metallic coatings
- Required chemicals / environment
- Liquid carrying hard solids; corrosive liquid may add synergy
- Influencing parameters
- Solids concentration; velocity; angle; particle distribution; material properties
- Physical explanation (1–3 processes)
- Liquid carries particles into sliding/impact contact
- Cutting, ploughing or repeated impact removes metal
- Signs and symptoms
- Localized grooves; impeller/outer-bend loss; dimensional wear
- Prevention / slowing the damage
- Duty-specific pump/flow design; resistant liners; solids control; thickness monitoring
- Typical failure outcome
- Leak; loss of pump performance; rupture
- Possible consequences
- Slurry release; downtime
- Can be mistaken for
- Cavitation; erosion-corrosion; dry abrasion
- How to distinguish it
- Analyse slurry and flow paths; identify impact/wear features and any chemical contribution
- How often is it seen?
- No representative subtype-specific incidence was identified in the reviewed sources. This is a data gap, not evidence of rarity.
- Historical case / verification status
- No mechanism-attributed catastrophe was verified in the sources reviewed; this does not mean none has occurred.
Photographs — 5 needed (real-life, not diagrams)
Macro / field view
Close-up or micrograph
Cross-section
In-service failure
Distinguishing feature
Sources
- 80 ASTM G75-24 — Slurry Abrasivity (Miller Number) and Slurry Abrasion Response of Materials (SAR Number) — Official public standard scope (accessed 2026-09-08)
- 80 ASTM G76-26 — Erosion Tests by Solid Particle Impingement Using Gas Jets — Official public standard scope (accessed 2026-09-08)
Educational synthesis, not a diagnosis or repair instruction. Confirm the actual alloy, environment, loading and damage before selecting mitigation. Generic signs are not unique proof of a mechanism.
DM-083Cavitation erosionWear, flow & surface damage · Vapour-bubble-collapse damage
Mechanism pathway
Service conditions
A liquid capable of local vaporization; no corrosive chemistry essential
Physical processes
- Low local pressure creates vapour cavities
- Collapse near metal produces microjets/shock loads
- Repeated impacts fatigue and remove surface material
Observable damage
Honeycomb-like craters; noise; vibration; performance loss
Possible failure mode
Through-wall leak; loss of component performance; possible secondary fracture
- Other names
- Cavitation pitting
- Industries / exposed sectors
- Pumps; hydropower; marine; valves
- Typically affected parts
- Impellers; propellers; turbine runners; throttling zones
- Susceptible materials
- Engineering metals exposed to cavitating liquid
- Required chemicals / environment
- A liquid capable of local vaporization; no corrosive chemistry essential
- Influencing parameters
- Pressure relative to vapour pressure; temperature; velocity; inlet conditions
- Physical explanation (1–3 processes)
- Low local pressure creates vapour cavities
- Collapse near metal produces microjets/shock loads
- Repeated impacts fatigue and remove surface material
- Signs and symptoms
- Honeycomb-like craters; noise; vibration; performance loss
- Prevention / slowing the damage
- Correct suction/pressure conditions; suitable geometry/operation; resistant surfaces
- Typical failure outcome
- Through-wall leak; loss of component performance; possible secondary fracture
- Possible consequences
- Loss of flow/efficiency; equipment outage
- Can be mistaken for
- Corrosion pitting; droplet erosion; particle erosion
- How to distinguish it
- Establish cavitating hydraulics and crater distribution; no diagnosis from pits alone
- How often is it seen?
- No representative subtype-specific incidence was identified in the reviewed sources. This is a data gap, not evidence of rarity.
- Historical case / verification status
- No mechanism-attributed catastrophe was verified in the sources reviewed; this does not mean none has occurred.
Photographs — 5 needed (real-life, not diagrams)
Macro / field view
Close-up or micrograph
Cross-section
In-service failure
Distinguishing feature
Sources
- 80 ASTM G32-16(2021)e1 — Cavitation Erosion Using Vibratory Apparatus — Official public standard scope (accessed 2026-09-08)
- 80 ASTM G73-10(2021) — Liquid Impingement Erosion Using Rotating Apparatus — Official public standard scope (accessed 2026-09-08)
Educational synthesis, not a diagnosis or repair instruction. Confirm the actual alloy, environment, loading and damage before selecting mitigation. Generic signs are not unique proof of a mechanism.
DM-084Liquid-droplet impingement erosionWear, flow & surface damage · Repeated liquid-impact damage
Mechanism pathway
Service conditions
High-relative-speed droplets or intermittent liquid impact
Physical processes
- Droplet impact generates high transient surface stress
- Repeated impacts deform/fatigue the surface and detach material
Observable damage
Leading-edge pits; roughened impact zone; progressing material loss
Possible failure mode
Loss of blade performance; possible blade fracture
- Other names
- Liquid impact erosion; droplet erosion
- Industries / exposed sectors
- Steam turbines; aviation; high-speed flow systems
- Typically affected parts
- Wet-steam blade leading edges; high-speed metallic surfaces
- Susceptible materials
- Steels; titanium; nickel and other blade alloys
- Required chemicals / environment
- High-relative-speed droplets or intermittent liquid impact
- Influencing parameters
- Impact velocity; droplet size; angle; exposure; material fatigue response
- Physical explanation (1–3 processes)
- Droplet impact generates high transient surface stress
- Repeated impacts deform/fatigue the surface and detach material
- Signs and symptoms
- Leading-edge pits; roughened impact zone; progressing material loss
- Prevention / slowing the damage
- Reduce wetness/impact severity; erosion-resistant shields/coatings; inspect leading edges
- Typical failure outcome
- Loss of blade performance; possible blade fracture
- Possible consequences
- Turbine/engine damage; outage
- Can be mistaken for
- Cavitation; solid-particle erosion; corrosion
- How to distinguish it
- Relate attack to droplet trajectories and wetness; no vapour-collapse zone or abrasive particles is necessary
- How often is it seen?
- No representative subtype-specific incidence was identified in the reviewed sources. This is a data gap, not evidence of rarity.
- Historical case / verification status
- No mechanism-attributed catastrophe was verified in the sources reviewed; this does not mean none has occurred.
Photographs — 5 needed (real-life, not diagrams)
Macro / field view
Close-up or micrograph
Cross-section
In-service failure
Distinguishing feature
Sources
- 80 ASTM G73-10(2021) — Liquid Impingement Erosion Using Rotating Apparatus — Official public standard scope (accessed 2026-09-08)
- 80 ASTM G32-16(2021)e1 — Cavitation Erosion Using Vibratory Apparatus — Official public standard scope (accessed 2026-09-08)
Educational synthesis, not a diagnosis or repair instruction. Confirm the actual alloy, environment, loading and damage before selecting mitigation. Generic signs are not unique proof of a mechanism.
DM-085Erosion-corrosionWear, flow & surface damage · Mechanical/chemical synergy
Mechanism pathway
Service conditions
Corrosive fluid plus mechanical surface/film damage
Physical processes
- Mechanical action removes/damages protective films
- Fresh metal corrodes; corrosion can facilitate further erosion
Observable damage
Flow-oriented grooves; local thinning; combined oxide/wear evidence
Possible failure mode
Leak or rupture
- Other names
- Flow-assisted erosion–corrosion; tribocorrosion in flow
- Industries / exposed sectors
- Marine; chemical; refining; water/slurry systems
- Typically affected parts
- Elbows; pump impellers; valves; exchanger inlets
- Susceptible materials
- Steels; copper alloys; stainless and other metals
- Required chemicals / environment
- Corrosive fluid plus mechanical surface/film damage
- Influencing parameters
- Velocity; turbulence; particles/bubbles; chemistry; film recovery
- Physical explanation (1–3 processes)
- Mechanical action removes/damages protective films
- Fresh metal corrodes; corrosion can facilitate further erosion
- Signs and symptoms
- Flow-oriented grooves; local thinning; combined oxide/wear evidence
- Prevention / slowing the damage
- Control chemistry and impingement; suitable flow design; resistant material/coating
- Typical failure outcome
- Leak or rupture
- Possible consequences
- Process release; loss of performance
- Can be mistaken for
- FAC; pure erosion; general corrosion
- How to distinguish it
- Demonstrate both mechanical damage and corrosion; distinguish magnetite-dissolution FAC from particle/bubble action
- How often is it seen?
- No representative subtype-specific incidence was identified in the reviewed sources. This is a data gap, not evidence of rarity.
- Historical case / verification status
- No mechanism-attributed catastrophe was verified in the sources reviewed; this does not mean none has occurred.
Photographs — 5 needed (real-life, not diagrams)
Macro / field view
Close-up or micrograph
Cross-section
In-service failure
Distinguishing feature
Sources
- 80 TWI — Corrosion of welded components in marine environments (April 2003) — Technical research paper (accessed 2026-09-08)
- 70 Copper Development Association — Seawater Corrosion Resistance and Antifouling — Technical reference (accessed 2026-09-08)
- 80 ASTM G76-26 — Erosion Tests by Solid Particle Impingement Using Gas Jets — Official public standard scope (accessed 2026-09-08)
Educational synthesis, not a diagnosis or repair instruction. Confirm the actual alloy, environment, loading and damage before selecting mitigation. Generic signs are not unique proof of a mechanism.
DM-086Flow-accelerated corrosionWear, flow & surface damage · Oxide dissolution controlled by mass transfer
Mechanism pathway
Service conditions
Water or wet steam and chemistry allowing oxide dissolution
Physical processes
- Protective magnetite dissolves into moving water
- Re-forming oxide and continuing dissolution consume metal
Observable damage
Scalloped/orange-peel thinning; local severe wall loss
Possible failure mode
Pipe rupture or leak
- Other names
- FAC; flow-assisted corrosion
- Industries / exposed sectors
- Fossil/nuclear power; industrial steam
- Typically affected parts
- Carbon-steel feedwater; condensate; wet-steam piping; elbows
- Susceptible materials
- Carbon/low-alloy steels, strongly influenced by chromium content
- Required chemicals / environment
- Water or wet steam and chemistry allowing oxide dissolution
- Influencing parameters
- Temperature; pH; redox/oxygen; mass transfer; alloy chromium
- Physical explanation (1–3 processes)
- Protective magnetite dissolves into moving water
- Re-forming oxide and continuing dissolution consume metal
- Signs and symptoms
- Scalloped/orange-peel thinning; local severe wall loss
- Prevention / slowing the damage
- Plant-specific water chemistry; resistant replacement alloy; predictive screening plus thickness inspection
- Typical failure outcome
- Pipe rupture or leak
- Possible consequences
- High-energy hot-water/steam release
- Can be mistaken for
- Erosion-corrosion; droplet erosion; caustic gouging
- How to distinguish it
- Confirm aqueous chemistry/flow context and oxide-dissolution loss; hard particles/cavitation are not required
- How often is it seen?
- No representative subtype-specific incidence was identified in the reviewed sources. This is a data gap, not evidence of rarity.
- Historical case / verification status
- Surry Unit 2, 9 December 1986: feedwater-system pipe rupture from wall thinning killed four workers; NRC documents the event in its erosion/corrosion operating-experience guidance.
Photographs — 5 needed (real-life, not diagrams)
Macro / field view
Close-up or micrograph
Cross-section
In-service failure
Distinguishing feature
Sources
- 80 Poulson, B. (2014). Predicting and Preventing Flow Accelerated Corrosion in Nuclear Power Plant. International Journal of Nuclear Energy, 423295. — Research paper abstract (accessed 2026-09-08)
- 80 NRC — Generic Letter 89-08: Erosion/corrosion-induced pipe wall thinning — Primary regulator operating-experience record (accessed 2026-09-08)
Educational synthesis, not a diagnosis or repair instruction. Confirm the actual alloy, environment, loading and damage before selecting mitigation. Generic signs are not unique proof of a mechanism.
DM-087Electrical erosion of bearingsWear, flow & surface damage · Discharge-driven surface damage
Mechanism pathway
Service conditions
No chemical necessary; current through the bearing is required
Physical processes
- Electrical discharge locally melts/vaporizes contact spots
- Repeated discharge and rolling develop pitting/fluting
Observable damage
Microscopic melt craters; washboard fluting; darkened lubricant; noise
Possible failure mode
Bearing wear-out or seizure
- Other names
- Current leakage damage; electrical pitting; fluting
- Industries / exposed sectors
- Electric motors; generators; variable-speed drives; rail
- Typically affected parts
- Bearing raceways and rolling elements
- Susceptible materials
- Conductive bearing steels
- Required chemicals / environment
- No chemical necessary; current through the bearing is required
- Influencing parameters
- Shaft voltage; current density; lubricant film; grounding; drive switching
- Physical explanation (1–3 processes)
- Electrical discharge locally melts/vaporizes contact spots
- Repeated discharge and rolling develop pitting/fluting
- Signs and symptoms
- Microscopic melt craters; washboard fluting; darkened lubricant; noise
- Prevention / slowing the damage
- Engineered shaft grounding; insulated/hybrid bearings where suitable; correct drive/cable installation
- Typical failure outcome
- Bearing wear-out or seizure
- Possible consequences
- Motor downtime; secondary shaft damage
- Can be mistaken for
- RCF; false brinelling; corrosion pitting
- How to distinguish it
- Microscopy for re-solidified craters plus shaft-current measurements; fluting alone is not uniquely diagnostic
- How often is it seen?
- SKF (2022): current leakage is 7% of identified bearing failure modes. Not an incidence for every motor or bearing installation.
- Historical case / verification status
- No mechanism-attributed catastrophe was verified in the sources reviewed; this does not mean none has occurred.
Photographs — 5 needed (real-life, not diagrams)
Macro / field view
Close-up or micrograph
Cross-section
In-service failure
Distinguishing feature
Sources
- 50 SKF (2011) — Golden opportunities — Primary manufacturer technical analysis (accessed 2026-09-08)
- 50 SKF (2022) — Bearing damage analysis: ISO 15243 is here to help you — Primary manufacturer investigation dataset (accessed 2026-09-08)
Educational synthesis, not a diagnosis or repair instruction. Confirm the actual alloy, environment, loading and damage before selecting mitigation. Generic signs are not unique proof of a mechanism.
DM-088Ductile overload fractureFracture & instability · Plastic fracture
Mechanism pathway
Service conditions
None essential
Physical processes
- Plastic deformation nucleates voids at particles/interfaces
- Void growth and coalescence form a tearing fracture
Observable damage
Dimples; shear lips; necking may occur but constraint can suppress it
Possible failure mode
Break or burst
- Other names
- Microvoid-coalescence fracture; ductile tearing
- Industries / exposed sectors
- All industries using loaded metal components
- Typically affected parts
- Bolts; shafts; pressure boundaries; structural members
- Susceptible materials
- Ductile engineering metals
- Required chemicals / environment
- None essential
- Influencing parameters
- Load; stress triaxiality; temperature; defects; strain rate
- Physical explanation (1–3 processes)
- Plastic deformation nucleates voids at particles/interfaces
- Void growth and coalescence form a tearing fracture
- Signs and symptoms
- Dimples; shear lips; necking may occur but constraint can suppress it
- Prevention / slowing the damage
- Avoid overload; adequate section/toughness; control defects and loading; protect against excursions
- Typical failure outcome
- Break or burst
- Possible consequences
- Loss of load/containment; possible injury
- Can be mistaken for
- Brittle fracture; fatigue final-overload zone; creep rupture
- How to distinguish it
- SEM dimples plus deformation/loading evidence; distinguish the final overload region from the initiating mechanism
- How often is it seen?
- No representative subtype-specific incidence was identified in the reviewed sources. This is a data gap, not evidence of rarity.
- Historical case / verification status
- No mechanism-attributed catastrophe was verified in the sources reviewed; this does not mean none has occurred.
Photographs — 5 needed (real-life, not diagrams)
Macro / field view
Close-up or micrograph
Cross-section
In-service failure
Distinguishing feature
Sources
- 80 TWI — What is a fracture toughness test? — Technical reference (accessed 2026-09-08)
- 80 TWI — Engineering Critical Assessment (ECA) — Technical reference (accessed 2026-09-08)
- 80 Crosti, C. & Duthinh, D. (2010). Buckling of steel gusset plates. IABMAS 2010; NIST. — Primary numerical/experimental research (accessed 2026-09-08)
Educational synthesis, not a diagnosis or repair instruction. Confirm the actual alloy, environment, loading and damage before selecting mitigation. Generic signs are not unique proof of a mechanism.
DM-089Brittle cleavage fractureFracture & instability · Rapid low-plasticity fracture
Mechanism pathway
Service conditions
None essential
Physical processes
- A sharp defect initiates crystallographic cleavage
- Crack propagates rapidly when driving force exceeds resistance
Observable damage
Cleavage facets/river patterns; little macroscopic deformation
Possible failure mode
Sudden break or vessel rupture
- Other names
- Cleavage; low-toughness fracture
- Industries / exposed sectors
- Structures; pressure equipment; transport; power
- Typically affected parts
- Notched/welded steel; thick sections; vessels; low-temperature parts
- Susceptible materials
- Susceptible ferritic steels and other cleavage-prone metals
- Required chemicals / environment
- None essential
- Influencing parameters
- Temperature; toughness; constraint; crack size; loading rate; stress
- Physical explanation (1–3 processes)
- A sharp defect initiates crystallographic cleavage
- Crack propagates rapidly when driving force exceeds resistance
- Signs and symptoms
- Cleavage facets/river patterns; little macroscopic deformation
- Prevention / slowing the damage
- Toughness-qualified material; defect control; suitable temperature/load envelope; integrity assessment
- Typical failure outcome
- Sudden break or vessel rupture
- Possible consequences
- Fragment release; structural collapse; high-energy release
- Can be mistaken for
- Intergranular HE/embrittlement; fatigue; ductile overload
- How to distinguish it
- Fractography separates cleavage facets from dimples or boundary fracture; establish toughness and loading temperature
- How often is it seen?
- No representative subtype-specific incidence was identified in the reviewed sources. This is a data gap, not evidence of rarity.
- Historical case / verification status
- No mechanism-attributed catastrophe was verified in the sources reviewed; this does not mean none has occurred.
Photographs — 5 needed (real-life, not diagrams)
Macro / field view
Close-up or micrograph
Cross-section
In-service failure
Distinguishing feature
Sources
- 80 TWI — What is a fracture toughness test? — Technical reference (accessed 2026-09-08)
- 80 TWI — Engineering Critical Assessment (ECA) — Technical reference (accessed 2026-09-08)
- 80 TWI — What is temper embrittlement, and how can it be controlled? — Technical reference (accessed 2026-09-08)
Educational synthesis, not a diagnosis or repair instruction. Confirm the actual alloy, environment, loading and damage before selecting mitigation. Generic signs are not unique proof of a mechanism.
DM-090Plastic collapse and pressure burstFracture & instability · Load-bearing instability
Mechanism pathway
Service conditions
None essential; corrosion may create the weakness
Physical processes
- Load exceeds the section’s plastic load-carrying capacity
- Large deformation destabilizes the component or opens a rupture
Observable damage
Bulging; permanent deformation; ductile tearing; reduced wall
Possible failure mode
Burst; collapse; gross deformation
- Other names
- Limit-load collapse; gross plastic instability
- Industries / exposed sectors
- Pressure equipment; pipelines; structures
- Typically affected parts
- Thinned pipes; vessels; overloaded members; weakened joints
- Susceptible materials
- Engineering metals with insufficient remaining section
- Required chemicals / environment
- None essential; corrosion may create the weakness
- Influencing parameters
- Pressure/load; wall thickness; geometry; yield/flow strength; temperature
- Physical explanation (1–3 processes)
- Load exceeds the section’s plastic load-carrying capacity
- Large deformation destabilizes the component or opens a rupture
- Signs and symptoms
- Bulging; permanent deformation; ductile tearing; reduced wall
- Prevention / slowing the damage
- Design/protection against overload; adequate corrosion allowance; thickness/integrity assessment
- Typical failure outcome
- Burst; collapse; gross deformation
- Possible consequences
- Major release; loss of structure
- Can be mistaken for
- Brittle fracture; creep rupture; buckling
- How to distinguish it
- Measure section loss and reconstruct load/temperature; distinguish plastic capacity failure from crack-controlled instability
- How often is it seen?
- No representative subtype-specific incidence was identified in the reviewed sources. This is a data gap, not evidence of rarity.
- Historical case / verification status
- No mechanism-attributed catastrophe was verified in the sources reviewed; this does not mean none has occurred.
Photographs — 5 needed (real-life, not diagrams)
Macro / field view
Close-up or micrograph
Cross-section
In-service failure
Distinguishing feature
Sources
- 80 TWI — Engineering Critical Assessment (ECA) — Technical reference (accessed 2026-09-08)
- 50 Veolia Water Technologies — Water Handbook, chapter 14: Boiler System Failures — Manufacturer technical handbook (accessed 2026-09-08)
- 80 PHMSA — Pipeline Failure Causes (updated 20 April 2026) — Regulatory taxonomy (accessed 2026-09-08)
Educational synthesis, not a diagnosis or repair instruction. Confirm the actual alloy, environment, loading and damage before selecting mitigation. Generic signs are not unique proof of a mechanism.
DM-091Buckling instabilityFracture & instability · Compressive/geometric instability
Mechanism pathway
Service conditions
None essential
Physical processes
- Compressive loading destabilizes the original geometry
- Post-buckling deformation may lead to yielding, tearing or collapse
Observable damage
Lateral bowing; wrinkles; ovalization; sudden loss of stiffness
Possible failure mode
Collapse or crippling
- Other names
- Elastic/inelastic buckling; shell collapse
- Industries / exposed sectors
- Structures; pipelines; tanks; offshore; aerospace
- Typically affected parts
- Columns; thin shells; vacuum vessels; tubes; gusset plates
- Susceptible materials
- All structural metals; geometry dominates susceptibility
- Required chemicals / environment
- None essential
- Influencing parameters
- Compression/external pressure; slenderness; imperfections; restraints; eccentricity
- Physical explanation (1–3 processes)
- Compressive loading destabilizes the original geometry
- Post-buckling deformation may lead to yielding, tearing or collapse
- Signs and symptoms
- Lateral bowing; wrinkles; ovalization; sudden loss of stiffness
- Prevention / slowing the damage
- Adequate stiffness/stiffening; realistic imperfection design; prevent unintended vacuum/overload
- Typical failure outcome
- Collapse or crippling
- Possible consequences
- Loss of support; containment; structural safety
- Can be mistaken for
- Plastic collapse without instability; creep deformation; impact damage
- How to distinguish it
- Compare deformation mode and compression history with stability analysis including imperfections
- How often is it seen?
- No representative subtype-specific incidence was identified in the reviewed sources. This is a data gap, not evidence of rarity.
- Historical case / verification status
- NIST’s gusset-plate studies address the 2007 I-35W bridge collapse context and demonstrate how geometry, eccentricity and restraint influence plate buckling. No single-mechanism casualty claim is inferred here.
Photographs — 5 needed (real-life, not diagrams)
Macro / field view
Close-up or micrograph
Cross-section
In-service failure
Distinguishing feature
Sources
- 80 Crosti, C. & Duthinh, D. (2010). Buckling of steel gusset plates. IABMAS 2010; NIST. — Primary numerical/experimental research (accessed 2026-09-08)
- 80 TWI — Engineering Critical Assessment (ECA) — Technical reference (accessed 2026-09-08)
Educational synthesis, not a diagnosis or repair instruction. Confirm the actual alloy, environment, loading and damage before selecting mitigation. Generic signs are not unique proof of a mechanism.
DM-092Ratcheting deformationFracture & instability · Progressive cyclic plastic strain
Mechanism pathway
Service conditions
None essential
Physical processes
- Combined mean and cyclic loading causes asymmetric plastic increments
- Permanent strain accumulates cycle by cycle
Observable damage
Progressive bulging/ovalization; permanent strain; subsequent fatigue cracks
Possible failure mode
Excessive deformation; fatigue leak or rupture
- Other names
- Incremental plastic collapse; cyclic strain accumulation
- Industries / exposed sectors
- Pressure piping; nuclear; cyclic process equipment
- Typically affected parts
- Pressurized elbows; pipes; thermal discontinuities
- Susceptible materials
- Ductile engineering metals
- Required chemicals / environment
- None essential
- Influencing parameters
- Steady plus cyclic load; mean stress; plastic hardening; geometry; temperature
- Physical explanation (1–3 processes)
- Combined mean and cyclic loading causes asymmetric plastic increments
- Permanent strain accumulates cycle by cycle
- Signs and symptoms
- Progressive bulging/ovalization; permanent strain; subsequent fatigue cracks
- Prevention / slowing the damage
- Design for shakedown; reduce mean/cyclic load combination; validated cyclic-plasticity assessment
- Typical failure outcome
- Excessive deformation; fatigue leak or rupture
- Possible consequences
- Reduced life; loss of clearance/containment
- Can be mistaken for
- LCF without net strain; creep; single overload
- How to distinguish it
- Measure accumulated residual strain per cycle and reconstruct combined loads; distinguish time-driven creep
- How often is it seen?
- No representative subtype-specific incidence was identified in the reviewed sources. This is a data gap, not evidence of rarity.
- Historical case / verification status
- No mechanism-attributed catastrophe was verified in the sources reviewed; this does not mean none has occurred.
Photographs — 5 needed (real-life, not diagrams)
Macro / field view
Close-up or micrograph
Cross-section
In-service failure
Distinguishing feature
Sources
- 80 Saravanan, M., Raghava, G., Vishnuvardhan, S. & Samuel Knight, G.M. Fatigue ratcheting studies on pressurised stainless steel straight pipes. Journal of Structural Engineering. — Primary experimental paper abstract (accessed 2026-09-08)
- 80 ASTM E606/E606M-21 — Strain-Controlled Fatigue Testing — Official public standard scope (accessed 2026-09-08)
Educational synthesis, not a diagnosis or repair instruction. Confirm the actual alloy, environment, loading and damage before selecting mitigation. Generic signs are not unique proof of a mechanism.
DM-093Weld solidification crackingFabrication cracking · Last-stage solidification failure
Mechanism pathway
Service conditions
None externally essential; low-melting segregants promote susceptibility
Physical processes
- Final interdendritic liquid films cannot carry shrinkage strain
- Inadequate feeding/cohesion leaves a crack during solidification
Observable damage
Centreline/crater cracks; interdendritic fracture morphology
Possible failure mode
Fabrication rejection; later leak/fracture
- Other names
- Solidification hot cracking; weld-centreline cracking
- Industries / exposed sectors
- Welded fabrication; repair; additive fusion processing
- Typically affected parts
- Weld centreline; craters; interdendritic regions
- Susceptible materials
- Susceptible steels; aluminium; nickel and other weld metals
- Required chemicals / environment
- None externally essential; low-melting segregants promote susceptibility
- Influencing parameters
- Composition; restraint; bead shape; solidification pattern; travel conditions
- Physical explanation (1–3 processes)
- Final interdendritic liquid films cannot carry shrinkage strain
- Inadequate feeding/cohesion leaves a crack during solidification
- Signs and symptoms
- Centreline/crater cracks; interdendritic fracture morphology
- Prevention / slowing the damage
- Qualified filler/composition and welding parameters; suitable bead shape; reduce restraint; crater control
- Typical failure outcome
- Fabrication rejection; later leak/fracture
- Possible consequences
- Rework or latent service failure
- Can be mistaken for
- Liquation cracking; cold hydrogen cracking; lack of fusion
- How to distinguish it
- Locate within solidifying weld metal; identify dendritic path and weld timing; lack of fusion follows an unfused interface
- How often is it seen?
- No representative subtype-specific incidence was identified in the reviewed sources. This is a data gap, not evidence of rarity.
- Historical case / verification status
- No mechanism-attributed catastrophe was verified in the sources reviewed; this does not mean none has occurred.
Photographs — 5 needed (real-life, not diagrams)
Macro / field view
Close-up or micrograph
Cross-section
In-service failure
Distinguishing feature
Sources
- 80 TWI — What is hot cracking (solidification cracking)? — Technical reference (accessed 2026-09-08)
- 80 TWI — Weldability of materials: aluminium alloys, Job Knowledge 21 — Technical reference (accessed 2026-09-08)
Educational synthesis, not a diagnosis or repair instruction. Confirm the actual alloy, environment, loading and damage before selecting mitigation. Generic signs are not unique proof of a mechanism.
DM-094Weld liquation crackingFabrication cracking · Localized grain-boundary melting
Mechanism pathway
Service conditions
None externally essential
Physical processes
- Local grain-boundary liquid forms during heating
- Tensile weld strain separates the weakened boundary before healing
Observable damage
Intergranular cracks beside fusion boundary or reheated passes
Possible failure mode
Weld rejection; later service fracture or leak
- Other names
- HAZ hot cracking; partially melted-zone cracking
- Industries / exposed sectors
- Aerospace; high-alloy welding; repair; fusion processing
- Typically affected parts
- Partially melted HAZ; reheated prior weld metal
- Susceptible materials
- Susceptible nickel, aluminium and other alloys
- Required chemicals / environment
- None externally essential
- Influencing parameters
- Peak thermal cycle; segregants; precipitates; restraint; heat input
- Physical explanation (1–3 processes)
- Local grain-boundary liquid forms during heating
- Tensile weld strain separates the weakened boundary before healing
- Signs and symptoms
- Intergranular cracks beside fusion boundary or reheated passes
- Prevention / slowing the damage
- Qualified thermal input/filler and material condition; control restraint and heat cycling
- Typical failure outcome
- Weld rejection; later service fracture or leak
- Possible consequences
- Rework; reduced structural integrity
- Can be mistaken for
- Solidification cracks; reheat cracks; LME
- How to distinguish it
- Locate in previously solid material affected by partial melting; examine resolidified boundary products
- How often is it seen?
- No representative subtype-specific incidence was identified in the reviewed sources. This is a data gap, not evidence of rarity.
- Historical case / verification status
- No mechanism-attributed catastrophe was verified in the sources reviewed; this does not mean none has occurred.
Photographs — 5 needed (real-life, not diagrams)
Macro / field view
Close-up or micrograph
Cross-section
In-service failure
Distinguishing feature
Sources
- 80 TWI — Laser Welding of Crack-Susceptible Materials, literature review 31002/2018 — Technical reference (accessed 2026-09-08)
- 80 TWI — Weldability of materials: aluminium alloys, Job Knowledge 21 — Technical reference (accessed 2026-09-08)
Educational synthesis, not a diagnosis or repair instruction. Confirm the actual alloy, environment, loading and damage before selecting mitigation. Generic signs are not unique proof of a mechanism.
DM-095Delayed hydrogen cracking in weldsFabrication cracking · Fabrication hydrogen-assisted cracking
Mechanism pathway
Service conditions
Diffusible hydrogen from moisture, consumables or contamination
Physical processes
- Hydrogen diffuses into stressed susceptible regions during/after cooling
- Hydrogen-assisted cracking develops, sometimes after inspection
Observable damage
Delayed weld/HAZ cracks; brittle paths; hard microstructure may be present
Possible failure mode
Fabrication rejection or later service fracture
- Other names
- Cold cracking; weld hydrogen cracking; underbead cracking
- Industries / exposed sectors
- Steel fabrication; construction; repair
- Typically affected parts
- Hard HAZ; weld root/toe; weld metal
- Susceptible materials
- Hardenable/high-strength steels; susceptible weld deposits
- Required chemicals / environment
- Diffusible hydrogen from moisture, consumables or contamination
- Influencing parameters
- Hydrogen; susceptible microstructure; tensile restraint; cooling/preheat history
- Physical explanation (1–3 processes)
- Hydrogen diffuses into stressed susceptible regions during/after cooling
- Hydrogen-assisted cracking develops, sometimes after inspection
- Signs and symptoms
- Delayed weld/HAZ cracks; brittle paths; hard microstructure may be present
- Prevention / slowing the damage
- Dry low-hydrogen process; qualified preheat/heat input; control restraint; code-appropriate delayed inspection
- Typical failure outcome
- Fabrication rejection or later service fracture
- Possible consequences
- Rework; loss of integrity
- Can be mistaken for
- SSC; solidification cracking; lack of fusion
- How to distinguish it
- Check crack timing, hardness, hydrogen-control records and location; increasing heat input is not universally beneficial
- How often is it seen?
- No representative subtype-specific incidence was identified in the reviewed sources. This is a data gap, not evidence of rarity.
- Historical case / verification status
- No mechanism-attributed catastrophe was verified in the sources reviewed; this does not mean none has occurred.
Photographs — 5 needed (real-life, not diagrams)
Macro / field view
Close-up or micrograph
Cross-section
In-service failure
Distinguishing feature
Sources
- 80 TWI — Hydrogen cracks in steels: prevention and best practice, Job Knowledge 46 — Technical reference (accessed 2026-09-08)
- 80 TWI — Do increased preheat and heat input always reduce hydrogen cracking risk? — Technical reference (accessed 2026-09-08)
- 80 TWI — Weldability of materials: carbon manganese and low alloy steels, Job Knowledge 19 — Technical reference (accessed 2026-09-08)
Educational synthesis, not a diagnosis or repair instruction. Confirm the actual alloy, environment, loading and damage before selecting mitigation. Generic signs are not unique proof of a mechanism.
DM-096Reheat and stress-relief crackingFabrication cracking · Elevated-temperature strain-relaxation failure
Mechanism pathway
Service conditions
None essential
Physical processes
- Grain interiors strengthen during reheating
- Stress relaxation concentrates strain on weak grain boundaries
Observable damage
Intergranular coarse-HAZ cracks, often at stress raisers
Possible failure mode
Fabrication rejection; leak/fracture in service
- Other names
- Reheat cracking; stress-relaxation cracking
- Industries / exposed sectors
- Power; pressure-vessel fabrication; high-alloy welding
- Typically affected parts
- Coarse-grained HAZ; weld metal during PWHT or hot service
- Susceptible materials
- Susceptible Cr-Mo/low-alloy steels; some precipitation-strengthened alloys
- Required chemicals / environment
- None essential
- Influencing parameters
- Residual stress; grain size; precipitates; impurity segregation; thermal cycle
- Physical explanation (1–3 processes)
- Grain interiors strengthen during reheating
- Stress relaxation concentrates strain on weak grain boundaries
- Signs and symptoms
- Intergranular coarse-HAZ cracks, often at stress raisers
- Prevention / slowing the damage
- Qualified alloy/welding/PWHT procedure; avoid severe coarse grains and notches; inspect after heat treatment
- Typical failure outcome
- Fabrication rejection; leak/fracture in service
- Possible consequences
- Rework; high-temperature integrity loss
- Can be mistaken for
- Type IV creep; liquation cracking; temper embrittlement
- How to distinguish it
- Locate coarse-grain damage and relate timing to reheating/relaxation; Type IV targets fine/intercritical HAZ
- How often is it seen?
- No representative subtype-specific incidence was identified in the reviewed sources. This is a data gap, not evidence of rarity.
- Historical case / verification status
- No mechanism-attributed catastrophe was verified in the sources reviewed; this does not mean none has occurred.
Photographs — 5 needed (real-life, not diagrams)
Macro / field view
Close-up or micrograph
Cross-section
In-service failure
Distinguishing feature
Sources
- 80 TWI — Defects/imperfections in welds: reheat cracking, Job Knowledge 48 — Technical reference (accessed 2026-09-08)
- 80 TWI — What is type IV cracking, and how is it detected? — Technical reference (accessed 2026-09-08)
Educational synthesis, not a diagnosis or repair instruction. Confirm the actual alloy, environment, loading and damage before selecting mitigation. Generic signs are not unique proof of a mechanism.
DM-097Lamellar tearingFabrication cracking · Inclusion-assisted weld-shrinkage tearing
Mechanism pathway
Service conditions
None essential
Physical processes
- Weld shrinkage strains the plate through thickness
- Inclusion decohesion and plastic tearing link step-like cracks
Observable damage
Stepped cracks roughly parallel to plate surface; woody fracture
Possible failure mode
Weld rejection; later joint separation
- Other names
- Through-thickness tearing; lamellar cracks
- Industries / exposed sectors
- Heavy plate fabrication; offshore; structural welding
- Typically affected parts
- Restrained T/corner/cruciform joints in rolled plate
- Susceptible materials
- Rolled steels with poor through-thickness ductility/inclusion stringers
- Required chemicals / environment
- None essential
- Influencing parameters
- Through-thickness shrinkage strain; restraint; inclusion morphology; joint orientation
- Physical explanation (1–3 processes)
- Weld shrinkage strains the plate through thickness
- Inclusion decohesion and plastic tearing link step-like cracks
- Signs and symptoms
- Stepped cracks roughly parallel to plate surface; woody fracture
- Prevention / slowing the damage
- Through-thickness-quality plate; improved joint/load direction; reduce restraint; qualified buttering where suitable
- Typical failure outcome
- Weld rejection; later joint separation
- Possible consequences
- Rework; structural integrity loss
- Can be mistaken for
- HIC; laminations; weld H cracking
- How to distinguish it
- Show stepped inclusion-linked tearing in parent plate and Z-direction shrinkage loading; HIC requires hydrogen charging evidence
- How often is it seen?
- No representative subtype-specific incidence was identified in the reviewed sources. This is a data gap, not evidence of rarity.
- Historical case / verification status
- No mechanism-attributed catastrophe was verified in the sources reviewed; this does not mean none has occurred.
Photographs — 5 needed (real-life, not diagrams)
Macro / field view
Close-up or micrograph
Cross-section
In-service failure
Distinguishing feature
Sources
- 80 TWI — Defects: lamellar tearing, Job Knowledge 47 — Technical reference (accessed 2026-09-08)
- 80 TWI — Weldability of materials: carbon manganese and low alloy steels, Job Knowledge 19 — Technical reference (accessed 2026-09-08)
Educational synthesis, not a diagnosis or repair instruction. Confirm the actual alloy, environment, loading and damage before selecting mitigation. Generic signs are not unique proof of a mechanism.
DM-098Quench crackingHeat treatment & thermal shock · Thermal/transformation-stress cracking
Mechanism pathway
Service conditions
No corrosive chemical essential; quench medium controls heat transfer
Physical processes
- Uneven cooling and phase transformation create incompatible strains
- Local tensile stress exceeds the low-temperature fracture resistance
Observable damage
Cracks after hardening; sharp-corner initiation; brittle fracture features
Possible failure mode
Manufacturing rejection or later break
- Other names
- Hardening cracks; quench-induced fracture
- Industries / exposed sectors
- Heat treatment; automotive; tools; manufacturing
- Typically affected parts
- Hardened gears; shafts; dies; tube/cylinder parts
- Susceptible materials
- Hardenable steels and susceptible heat-treated metals
- Required chemicals / environment
- No corrosive chemical essential; quench medium controls heat transfer
- Influencing parameters
- Cooling rate/distribution; section changes; hardenability; residual stress; inclusions
- Physical explanation (1–3 processes)
- Uneven cooling and phase transformation create incompatible strains
- Local tensile stress exceeds the low-temperature fracture resistance
- Signs and symptoms
- Cracks after hardening; sharp-corner initiation; brittle fracture features
- Prevention / slowing the damage
- Qualified heat-treatment/quench process; sound geometry; clean steel; timely specified tempering; NDT
- Typical failure outcome
- Manufacturing rejection or later break
- Possible consequences
- Scrap; latent component fracture
- Can be mistaken for
- Grinding cracks; hydrogen cracks; pre-existing forging laps
- How to distinguish it
- Trace heat-treatment timing; metallography and oxide/temper evidence; assess transformation and thermal stresses
- How often is it seen?
- No representative subtype-specific incidence was identified in the reviewed sources. This is a data gap, not evidence of rarity.
- Historical case / verification status
- ASM documents 4140 seamless hydraulic-cylinder tubing rejected for quench cracks associated with inclusions and excessive severity for the geometry; not reported as a catastrophic public accident.
Photographs — 5 needed (real-life, not diagrams)
Macro / field view
Close-up or micrograph
Cross-section
In-service failure
Distinguishing feature
Sources
- 80 ASM (2019). Failure of Seamless Tubing Due to a Quench Crack. ASM Failure Analysis Case Histories: Design Flaws. — Primary failure case abstract (accessed 2026-09-08)
- 80 ASM Handbook 4F (2024). Steel Heat Treatment Failures due to Quenching, pp. 575–592. — Authoritative handbook abstract (accessed 2026-09-08)
Educational synthesis, not a diagnosis or repair instruction. Confirm the actual alloy, environment, loading and damage before selecting mitigation. Generic signs are not unique proof of a mechanism.
DM-099Grinding burn and grinding crackingHeat treatment & thermal shock · Machining-induced thermal damage
Mechanism pathway
Service conditions
None essential; inadequate cooling/process control may contribute
Physical processes
- Grinding heat locally tempers or rehardens the surface
- Thermal strain produces harmful residual stress and sometimes cracks
Observable damage
Hardness gradients; tensile subsurface stress; burns/cracks; discoloration may be absent
Possible failure mode
Premature fatigue fracture or contact-surface failure
- Other names
- Grinding thermal damage; retempering/rehardening burn
- Industries / exposed sectors
- Gear/bearing manufacture; aerospace; precision engineering
- Typically affected parts
- Ground gear teeth; bearing races; shafts; ball screws
- Susceptible materials
- Hardened ferromagnetic steels; other metals can suffer grinding damage
- Required chemicals / environment
- None essential; inadequate cooling/process control may contribute
- Influencing parameters
- Grinding heat input; wheel condition; removal rate; coolant; initial hardness
- Physical explanation (1–3 processes)
- Grinding heat locally tempers or rehardens the surface
- Thermal strain produces harmful residual stress and sometimes cracks
- Signs and symptoms
- Hardness gradients; tensile subsurface stress; burns/cracks; discoloration may be absent
- Prevention / slowing the damage
- Control grinding energy/cooling and wheel condition; qualified inspection; reject/remediate damage
- Typical failure outcome
- Premature fatigue fracture or contact-surface failure
- Possible consequences
- Reduced life; precision-system failure
- Can be mistaken for
- Quench cracking; adhesive scuffing; normal grinding marks
- How to distinguish it
- Calibrated Barkhausen/etch/hardness or metallographic checks; surface appearance alone misses subsurface damage
- How often is it seen?
- No representative subtype-specific incidence was identified in the reviewed sources. This is a data gap, not evidence of rarity.
- Historical case / verification status
- No mechanism-attributed catastrophe was verified in the sources reviewed; this does not mean none has occurred.
Photographs — 5 needed (real-life, not diagrams)
Macro / field view
Close-up or micrograph
Cross-section
In-service failure
Distinguishing feature
Sources
- 80 Sub-Surface Analysis of Grinding Burns with Barkhausen Noise Measurements (2023). Materials 16(1), 159. — Primary experimental paper (accessed 2026-09-08)
- 80 Grinding Burn Detection via Magnetic Barkhausen Noise Analysis Independently of Induction Hardened Depth (2023). Materials 16(5), 2127. — Primary experimental paper (accessed 2026-09-08)
Educational synthesis, not a diagnosis or repair instruction. Confirm the actual alloy, environment, loading and damage before selecting mitigation. Generic signs are not unique proof of a mechanism.
DM-100Thermal-shock fractureHeat treatment & thermal shock · Single/severe-transient thermal fracture
Mechanism pathway
Service conditions
None chemically essential; coolant can impose the thermal step
Physical processes
- Rapid unequal thermal expansion/contraction creates transient stress
- A severe excursion drives a crack beyond material resistance
Observable damage
Cracks after a sudden transient; surface-origin fracture; limited prior cycling
Possible failure mode
Fracture; possible through-wall leak or complete break
- Other names
- Thermal shock cracking; acute thermal-gradient fracture
- Industries / exposed sectors
- Foundries; heat treatment; boilers; high-temperature equipment
- Typically affected parts
- Castings; hot components hit by cold fluid; thick-section interfaces
- Susceptible materials
- Metals with insufficient toughness/ductility for the gradient and restraint
- Required chemicals / environment
- None chemically essential; coolant can impose the thermal step
- Influencing parameters
- Temperature step; heat-transfer rate; thickness; restraint; toughness
- Physical explanation (1–3 processes)
- Rapid unequal thermal expansion/contraction creates transient stress
- A severe excursion drives a crack beyond material resistance
- Signs and symptoms
- Cracks after a sudden transient; surface-origin fracture; limited prior cycling
- Prevention / slowing the damage
- Avoid abrupt incompatible transients; controlled heating/cooling; appropriate geometry/toughness
- Typical failure outcome
- Fracture; possible through-wall leak or complete break
- Possible consequences
- Hot-fluid release; loss of component function
- Can be mistaken for
- Thermal fatigue; quench cracking; cold brittle fracture
- How to distinguish it
- Establish acute thermal transient; distinguish repeated-cycle growth and transformation-related quench stresses
- How often is it seen?
- No representative subtype-specific incidence was identified in the reviewed sources. This is a data gap, not evidence of rarity.
- Historical case / verification status
- No mechanism-attributed catastrophe was verified in the sources reviewed; this does not mean none has occurred.
Photographs — 5 needed (real-life, not diagrams)
Macro / field view
Close-up or micrograph
Cross-section
In-service failure
Distinguishing feature
Sources
- 80 ASM Handbook 4F (2024). Steel Heat Treatment Failures due to Quenching, pp. 575–592. — Authoritative handbook abstract (accessed 2026-09-08)
- 80 TWI — What is a fracture toughness test? — Technical reference (accessed 2026-09-08)
- 80 TWI — Examination of cracking in boiler tubes — Primary failure investigation (accessed 2026-09-08)
Educational synthesis, not a diagnosis or repair instruction. Confirm the actual alloy, environment, loading and damage before selecting mitigation. Generic signs are not unique proof of a mechanism.
Version 1.1-review, generated 2026-09-08. Sources carry a credibility tier: 80 = TWI / ASNT / ASME / ASTM / API / EPRI / peer-reviewed papers and recognised failure-analysis standards; 70 = Wikipedia / Wikimedia; 50 = other inspection and case sources; 20 = general web. Questions or corrections: inquiry@matertec.com.
