Calculations & Intervals
Not publishedof exam
Welding Procedure Review
Not publishedof exam
Nondestructive Examination
Not publishedof exam
Practical Knowledge General
Not publishedof exam
Practical Knowledge Specific
Not publishedof exam
Quick Facts
- Exam
- API 570
- Credential
- Piping Inspector
- Body
- API
- Questions
- 170 (140 scored)
- Time
- 7.5-hour exam day
- Pass score
- 400 of 500 scaled
- Format
- Closed + open book
- Level
- Advanced, experienced inspectors
- Blueprint
- Feb 2026 BOK
Corrosion Rate Choice
Compare LT and ST rates; always use the faster
LT vs ST Corrosion Rate
Long-Term (LT)
- Since initial baseline thickness
- Covers full service history
Short-Term (ST)
- Since previous reading only
- Flags recent rate acceleration
Use the higher rate
Inspection Interval Picker
- Remaining life over 20 years→Table 1 max interval(Class-based cap applies)
- Remaining life under 4 years→Full life, max 2yr(Short-life exception rule)
- RBI assessment available→RBI-set due date(Per API 580)
- No RBI, Class 1→5yr thickness and external(Shortest fixed interval)
- No RBI, Class 3→10yr thickness and external(Longest fixed interval)
- Injection point circuit→3yr max thickness(Localized corrosion risk)
Corrosion Rate Formulas
- LT rate
- Baseline minus actual, per year
- ST rate
- Previous minus actual, per year
- Governing rate
- Use the faster of two
- t-actual
- Thickness measured at inspection
- t-required
- Design minimum before allowances
- t-initial
- Baseline thickness at install
- Remaining life
- Actual minus required, over rate
Table 1 Interval Order
Class 1 tightest, Class 4 loosest inspection interval
Point-to-Point vs Circuit Method
Point-to-Point
- Per-CML worst case only
- No statistical pooling used
- Simple and conservative
Circuit/Statistical
- Pools circuit-wide CML data
- Needs fairly uniform corrosion
- Uses a confidence interval
Per-point vs circuit-wide averaging
Inspection Intervals (Table 1)
- Class 1
- 5 years thickness and external
- Class 2
- 10yr thickness, 5yr external
- Class 3
- 10 years thickness and external
- Class 4
- Optional, owner-user discretion
- Injection points
- 3-year max thickness interval
- Soil-to-air interface
- By class; see API 574
- Half-life rule
- Max interval = half remaining life
- Short remaining life
- Under 4yr: full life, max 2yr
MAWP & Thickness Design
- MAWP recalc
- Actual t minus 2x loss
- t-min straight pipe
- ASME B31.3, 304.1.1
- Blank thickness
- ASME B31.3, 304.5.3 rule
- Ej
- Weld joint quality factor
- Ec
- Casting quality factor
- Hydro test pressure
- About 1.5x design pressure
- Pneumatic test
- Riskier; lower safety margin
- Brittle fracture margin
- 30F above MDMT, thick pipe
Flange, Impact & Thermal Calcs
- Flange rating
- Temperature sets max pressure
- Flange class
- Material plus temperature table
- Impact exemption
- Min metal temp curve
- Charpy V-notch
- Min required impact value
- Preheat temperature
- Set by weld size table
- Thermal expansion
- Appendix C, Table C-1
Weld Document Trio
WPS is how; PQR proves it; WPQ certifies welder
PQR vs WPQ
PQR
- Qualifies the weld procedure
- Records mechanical test results
- One per supporting WPS
WPQ
- Qualifies the individual welder
- Tests welder's actual skill
- Per welder, per process
Procedure proof vs person proof
Welding Review Checklist
- Reviewing a WPS→Check essential variables(Match to qualified PQR)
- Reviewing a PQR→Check mechanical test results(Proper type and pass)
- Reviewing a WPQ→Check welder qualification(Coupon per qualified WPS)
- Dissimilar base metal joint→Exclude from exam scope(Not tested this exam)
WPS, PQR, WPQ Review
- WPS
- Welding Procedure Specification, the how
- PQR
- Procedure Qualification Record, proves WPS
- WPQ
- Welder Performance Qualification, proves welder
- Essential variable
- Change requires requalification
- Nonessential variable
- Change needs no retest
- Supplemental essential
- Not tested on this exam
- Signed & dated
- Required on PQR and WPQ
Essential vs Nonessential Variables
Essential Variable
- Requires WPS requalification test
- Affects mechanical properties directly
Nonessential Variable
- No requalification needed here
- Documentation update only needed
Requalify vs simply revise
Welding Review Limits
- Processes covered
- SMAW, GTAW, GMAW, or SAW
- One process per WPS
- No multi-process WPS on exam
- Filler metal limit
- One filler metal per process
- Base metals tested
- P-1, P-3, P-4, P-5, P-8
- Dissimilar metals
- Excluded from exam scope
- Brazing
- Not covered on this exam
- Transition temps (exam)
- 1330F lower, 1600F upper
NDE Surface vs Volume
PT and MT see surface; RT and UT see inside
RT vs UT
RT
- Internal flaws and slag
- Porosity and inclusion detection
- Film or digital image
UT
- Elongated, planar flaw sizing
- Thickness measurement capability
- Angle beam for cracks
Imaging vs sizing and thickness
NDE Method Picker
- Surface cracks, nonmagnetic material→PT(Liquid penetrant)
- Surface cracks, ferromagnetic material→MT(Yoke or prod)
- Internal flaws, weld slag→RT(Radiography)
- Elongated internal or surface flaw→UT flaw detection(Angle beam technique)
- Manual thickness measurement needed→UT (SE-797)(Pulse-echo contact method)
- Overall external condition check→VT(Visual examination)
- Through-thickness defect suspected→Leak test(Article 10 method)
Section V NDE Methods
- RT (Article 2)
- Radiography for internal flaws
- PT (Article 6)
- Penetrant for surface cracks
- MT (Article 7)
- Yoke/prod for ferromagnetic cracks
- VT (Article 9)
- Visual for overall condition
- Leak test (Article 10)
- Bubble test, direct pressure
- UT (Article 23)
- SE-797 manual thickness only
- IQI
- Image quality indicator for RT
PT vs MT
PT
- Nonmagnetic material required
- Surface-breaking flaws only
- Liquid dye penetrant
MT
- Ferromagnetic material required
- Yoke or prod technique
- Magnetic flux leakage
Material magnetism decides method
NDE Method Selection Notes
- Surface vs volumetric
- PT/MT surface, RT/UT internal
- Calibration
- Required before every NDE method
- Record keeping
- Required for all NDE articles
- Ultrasonic accuracy limits
- Coatings, roughness, temp above 150F
- Owner/user responsibility
- Define procedures and acceptance criteria
- Section V scope
- Main article body only tested
Class 1 vs Class 2 Piping
Class 1
- Immediate emergency potential
- Rapid vaporizing, H2S, HF
- 5-year thickness and external
Class 2
- Most unit process piping
- Slow-vaporizing, on-site service
- 10yr thickness, 5yr external
Consequence of failure severity
Piping Class Picker
- Rapid vaporizing C2-C4→Class 1(Immediate emergency risk)
- H2S over 3%→Class 1(Toxic gaseous stream)
- Anhydrous HCl or HF→Class 1(Acid service)
- Piping over water or roads→Class 1(Public exposure risk)
- Slow-vaporizing on-site hydrocarbon→Class 2(Most unit piping)
- On-site acids or caustics→Class 2(Strong chemical service)
- Off-site tank farm lines→Class 3(Remote, below flash point)
- Nonflammable utility service→Class 4(Steam, air, nitrogen, water)
CML & Circuitization
- CML
- Condition monitoring location on circuit
- Circuit
- Grouped piping with similar corrosion
- More CMLs
- Higher risk or localized corrosion
- Fewer CMLs
- Low risk, noncorrosive, straight run
- Point-to-point method
- Worst-case CML sets interval
- Circuit/statistical method
- Pools data, needs uniform corrosion
Closed-Book vs Open-Book Exam
Closed-Book
- 110 questions, 2.75 hours
- Memorized formulas and rules
- No references allowed
Open-Book
- 60 questions, 3.75 hours
- On-screen PDF references given
- Only effectivity sheet documents
Memory speed vs lookup speed
Deadlegs, SBP & Injection Points
- Deadleg
- Low-flow branch, accelerated corrosion risk
- Small bore piping
- Vents, drains, bridles, level
- Injection point upstream
- 12in or 3 diameters, greater
- Injection point downstream
- 25ft or next flow-direction change
- SBP Class 1/2
- Same rules as primary piping
- Threaded connections
- Inspect like small-bore piping
- Auxiliary piping
- Optional; risk-based inspection only
Records & Program Basics
- Permanent records
- Kept for piping system life
- Progressive records
- Updated after every inspection
- Baseline thickness
- Set at installation inspection
- Owner-user duty
- 20% time on inspection work
- CPD hours
- 24 hours per 3-year cycle
Damage Mechanism Memory Groups
Amine, caustic, and chloride all cause stress cracking
Sulfidation vs Sour Water Corrosion
Sulfidation
- High-temperature sulfur compound attack
- No water phase required
Sour Water Corrosion
- Aqueous H2S and cyanide
- Acidic condensate, pitting common
Temperature regime and phase differ
Damage Mechanisms (RP 571)
- Amine SCC
- Rich amine unit cracking
- Atmospheric corrosion
- Weather-exposed external metal loss
- Boiler water corrosion
- Condensate and steam system loss
- Caustic corrosion
- Concentrated NaOH localized attack
- Caustic SCC
- Cracking under caustic and stress
- Chloride SCC
- Austenitic stainless under chloride/stress
- CUI
- Corrosion under wet insulation
- Erosion/erosion-corrosion
- Flow-induced wall thinning
- Galvanic corrosion
- Dissimilar metals, electrolyte present
- HCl corrosion
- Hydrochloric acid, often overhead
- Mechanical fatigue
- Vibration-induced cyclic cracking
- MIC
- Microbiologically influenced localized corrosion
- Soil corrosion
- Buried piping external attack
- Sour water corrosion
- Acidic H2S condensate attack
- Sulfidation
- High-temp sulfur compound thinning
PRDs (RP 576) & PMI (RP 578)
- PRD test interval
- 5yr typical, 10yr clean service
- Stuck-shut default
- 150% of set pressure limit
- PRD scope tested
- RP 576 sections 5, 6.1-6.5, 7
- PMI program
- Confirms installed material matches spec
- PMI verification
- 100%, risk-based, or sampling
- Retroactive PMI
- Targets legacy alloy piping systems
PCC-2 Repair Articles
- Art. 201
- Butt-welded insert plates
- Art. 206
- Full encirclement reinforcing sleeves
- Art. 209
- Alternatives to postweld heat treatment
- Art. 210
- In-service welding on carbon steel
- Art. 211
- Weld overlay and clad restoration
- Art. 304
- Flaw excavation and weld repair
- Art. 305/306
- Flange repair, mechanical clamp repair
RP 574 & RP 577 Basics
- RP 574 scope
- Entire document tested, components
- RP 577 scope
- Entire document tested, welding metallurgy
- Piping components
- Valves, flanges, fittings inspection practices
- Weld metallurgy basics
- HAZ, dilution, hardness for inspectors
- RP 578 scope
- Material verification, new and existing
Common Traps
LT rate ≠ ST rate
LT uses the baseline ≠ ST uses the previous reading
Remaining life ≠ corrosion rate
Life counts years left ≠ Rate counts loss per year
Class 1 ≠ Class 3 interval
Class 1 is all 5-year ≠ Class 3 is all 10-year
PQR ≠ WPQ
PQR qualifies the procedure ≠ WPQ qualifies the welder
Essential ≠ nonessential variable
Essential change needs retest ≠ Nonessential change just noted
RT ≠ UT purpose
RT images internal flaws ≠ UT sizes and measures thickness
Closed-book ≠ open-book portion
Closed-book tests memorized rules ≠ Open-book tests document lookup
Circuit ≠ single CML
Circuit groups many CMLs ≠ CML is one location
Last Minute
- 1.170 questions, 140 scored total
- 2.110 closed-book, 60 open-book
- 3.7.5-hour exam day, 45-min lunch
- 4.Pass score: 400 of 500
- 5.Use the higher LT/ST rate
- 6.Remaining life = actual minus required
- 7.Class 1 interval: 5 and 5
- 8.Class 3 interval: 10 and 10
- 9.Injection points: 3-year thickness max
- 10.MAWP recalc uses 2x corrosion loss
- 11.PQR proves procedure; WPQ proves welder
- 12.Open-book allows only effectivity-sheet documents
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