ASME B31.3 Process Piping — Inspection Requirements Made Simple

ASME B31.3 governs how process piping is designed and built, not how it's inspected once running, a distinction that trips up new inspectors constantly.

By Anoop Rayavarapu, ASNT NDT Level III · · Standards & Codes

ASME B31.3: Complete Industry Guide & Implementation

ASME B31.3 is a critical standard that defines asme b31.3 process piping code and requirements. This comprehensive guide explains the standard's scope, key requirements, NDE methods, acceptance criteria, and practical implementation strategies for professionals in the NDT and inspection industry.

Standard Overview

What is ASME B31.3?

ASME B31.3 establishes comprehensive requirements, methods, and acceptance criteria for nondestructive examination and inspection. This standard represents the accumulated knowledge of industry experts and has evolved through decades of failure analysis, field experience, and technological advancement. Understanding its intent, requirements, and limitations is essential for compliance and effective risk management in your organization.

Scope and Applicability

The standard defines specific boundaries regarding which equipment, materials, operating conditions, and inspection scenarios fall under its jurisdiction. Proper identification of applicability is critical—applying the wrong standard or missing required coverage can lead to regulatory violations, failed audits, and safety incidents.

Key applicability considerations:

  • Material types and grades: The standard specifies which materials are covered, including steel grades, alloys, castings, forgings, and other material forms
  • Equipment categories: Specific equipment types (pressure vessels, piping, rotating equipment, heat exchangers, etc.) and their operating parameters
  • Service conditions: Temperature ranges, pressure limits, corrosive environments, and cyclic loading conditions
  • Inspection frequency: Intervals between inspections based on risk assessment, operating history, and material degradation rates
  • Component geometry: Size, thickness, wall configurations, and access considerations that affect inspection method selection
  • Jurisdictional requirements: Regulatory authority mandates that may require application of this standard in specific industries or regions

Many facilities operate equipment governed by multiple overlapping standards. Integration of requirements from ASME, API, ASTM, EN, ISO, and other bodies is necessary to ensure comprehensive inspection coverage without gaps or conflicts.

Key Requirements and Procedures

Fundamental Inspection Requirements

The standard establishes mandatory requirements across multiple dimensions of the inspection program:

1. Inspection Frequency and Intervals:

  • Initial/hydrostatic test inspection before equipment enters service
  • Scheduled in-service inspections at defined intervals (annual, 5-year, 10-year cycles typical)
  • Condition-based inspections triggered by operating anomalies, upset conditions, or design changes
  • Routine monitoring inspections for critical components with accelerated degradation risk
  • Post-maintenance inspections to verify repair integrity and document baseline changes

2. Inspection Methods and Techniques:

The standard specifies which NDE methods are acceptable for different applications:

  • Visual Inspection (VT): Required baseline for all inspections; documents corrosion patterns, erosion, distortion, and obvious defects
  • Ultrasonic Testing (UT): Primary method for thickness measurement, internal flaw detection, and corrosion mapping in accessible components
  • Radiographic Testing (RT): Required for critical welds, castings, and components where volumetric integrity is essential
  • Magnetic Particle Inspection (MPI): For ferromagnetic materials with surface and near-surface defect concerns
  • Liquid Penetrant Testing (PT): For non-ferromagnetic materials requiring surface defect sensitivity
  • Eddy Current Testing (ECT): For tube and tubing inspection, material verification, and automated scanning applications
  • Additional Methods: Infrared thermography, acoustic emission, and specialized techniques as required by specific service conditions

Acceptance Criteria

The standard defines specific acceptance/rejection criteria for detected indications:

  • Size limits: Maximum allowable flaw dimensions (length, depth, through-wall dimensions) vary by component type, service severity, and inspection method
  • Quantity limits: Clustered or multiple indications may be cause for rejection even if individual indications are acceptable
  • Location restrictions: High-stress areas (weld heat-affected zones, stress concentration points) have tighter acceptance limits than low-stress regions
  • Defect type specifications: Different types (cracks, inclusions, porosity, lack of fusion) have different acceptance criteria reflecting their impact on equipment integrity
  • Conditional acceptance: Some indications may be acceptable with documented engineering justification and increased future monitoring frequency
  • Rejectable conditions: Certain indications (through-wall cracks, deep lamellar defects in critical areas) are unconditionally rejectable regardless of size

NDE Method Requirements by Application

Weld Examination: Radiography, ultrasonic, or combination methods; specific percentage coverage mandated based on weld classification and criticality

Corrosion Mapping: Systematic ultrasonic thickness measurement on gridded pattern; trending of results across multiple inspection cycles

Coating/Lining Inspection: Holiday detection, adhesion testing, and thickness measurement per specific coating standards

Bolted Connections: Visual inspection for corrosion, stress concentration effects; ultrasonic evaluation of bolt pre-load and integrity in critical applications

Casing and Tubing: Eddy current or ultrasonic methods; automated scanning systems for rapid coverage of long distances

Personnel Qualification and Training

The standard mandates specific qualifications for personnel performing inspections, interpreting results, and making acceptance decisions:

  • Level I Inspectors: Perform routine inspections under direction; require formal training and supervised field experience
  • Level II Inspectors: Plan inspections, interpret results, and sign inspection reports; require advanced training and 2+ years NDT experience
  • Level III Inspectors: Approve inspection procedures, provide training, and serve as technical authority; require 5+ years experience and comprehensive certification
  • Equipment Operators: Must be trained on specific equipment operation, calibration, and maintenance
  • Data Analysts: For trending and fitness-for-service assessment, require advanced training in statistical analysis and corrosion prediction methods

Organizations must maintain training records, competency documentation, and evidence of periodic re-qualification. Many standards require recertification every 3-5 years.

Documentation and Record Keeping

Comprehensive documentation is critical for regulatory compliance and future reference:

  • Inspection procedures (written, approved, available on-site)
  • Equipment calibration certificates and maintenance logs
  • Individual inspection reports with findings, measurements, and photographs
  • Defect mapping and corrective action tracking
  • Trending database of historical measurements and condition changes
  • Personnel qualification records and training documentation
  • Management of Change documentation for modifications affecting inspection requirements
  • Risk assessment and criticality ratings supporting inspection frequency decisions

Common Industry Applications

Oil & Gas Processing

Pressure vessels, heat exchangers, and piping systems operating at elevated temperatures and pressures. Corrosion monitoring and weld examination are critical. Equipment typically inspected every 2-5 years with trending of wall thickness.

Chemical Processing

Reactors, distillation columns, and specialized equipment handling corrosive or hazardous materials. Coating integrity and stress corrosion cracking (SCC) assessment are common focus areas.

Power Generation

Boilers, turbines, and steam systems with complex inspection requirements due to high temperatures, pressures, and cyclic stresses. In-service inspection of ferritic steels is critical due to hydrogen attack and creep damage risk.

Aerospace and Aviation

Structural components, pressure vessels, and rotating equipment with stringent defect size limits. Automated inspection systems and advanced analysis techniques are standard practice.

Manufacturing and Fabrication

Production facilities fabricating equipment to code standards require inspection of welds, castings, and assemblies before shipment and commissioning.

Compliance Tips and Best Practices

1. Develop a comprehensive inspection strategy: Map all equipment covered by the standard, document inspection history, establish baseline measurements, and develop risk-based inspection intervals.

2. Invest in qualified personnel: Ensure Level II and III inspectors available on staff or through qualified contractors. Maintain current certifications and training records.

3. Implement trending programs: Systematic collection and analysis of measurement data across inspection cycles enables early detection of accelerating degradation and supports remaining life predictions.

4. Keep equipment calibrated and maintained: Inspection instruments require regular calibration against traceable standards. Maintenance logs should be readily available during audits.

5. Document everything: Detailed records demonstrate due diligence and support defensibility in case of regulatory audit or incident investigation.

6. Stay current on revisions: Standards are regularly updated. Subscribe to update notifications, participate in industry associations, and implement changes promptly.

7. Use internal links to resources: Consider consulting services for complex assessment projects, training programs for personnel qualification, or ASNT certification courses to maintain staff qualifications. The NDT method selector tool helps identify optimal inspection approaches for specific applications.

Related Standards and Integration

This standard often works in conjunction with other codes:

  • ASME Section VIII: Pressure vessel design and fabrication requirements
  • API 510/570/575: In-service inspection of pressure vessels, piping, and tanks
  • ASTM Standards: Specific NDE method standards and acceptance criteria
  • ISO Standards: International equivalents and global recognition standards
  • AWS Standards: Welding and weld inspection requirements
  • Company-specific Standards: Many organizations implement requirements more stringent than the base standard based on corporate risk tolerance

Professionals must understand how ASME B31.3 integrates with other applicable codes to ensure comprehensive, coordinated compliance.

Frequently Asked Questions (FAQs)

Q1: How do I know if my equipment is covered by ASME B31.3?

A: Review the standard's scope section carefully. Key factors: equipment type, material, operating pressure/temperature, and facility location/regulatory jurisdiction. When in doubt, contact the regulatory authority having jurisdiction (API, ASME, OSHA, state inspector, etc.). Most companies document equipment coverage in their Pressure Equipment Management System (PEMS) or equivalent database.

Q2: What's the difference between ASME B31.3 and other related standards?

A: Each standard serves a specific purpose. Some define manufacturing requirements (ASME Section VIII), others define in-service inspection (API 510), and others specify NDE methods (ASTM). Your equipment may be subject to multiple standards simultaneously. Integration is your responsibility. Work with a consultant if scope is unclear.

Q3: How often must inspections occur under ASME B31.3?

A: Inspection frequency depends on risk assessment, operating history, material type, and service conditions. Common intervals: annual for high-risk items, 2-5 year cycles for moderate risk, 10-year or longer for low-risk items. The standard provides guidance; your organization determines specific intervals based on documented risk evaluation.

Q4: Can I use alternative NDE methods not specifically mentioned in ASME B31.3?

A: Possibly, but this requires documented engineering justification and regulatory authority approval. Demonstrate that the alternative method provides equivalent or superior sensitivity and that data interpretation is reliable. Advanced methods like phased array UT, automated systems, and emerging technologies often require such justification.

Q5: What qualifications do my inspection staff need?

A: At minimum: ASNT SNT-TC-1A Level II certification in relevant NDE methods for personnel who sign inspection reports. For complex assessments or as Level III: ASNT Level III, ISO 9712 Level 3, or equivalent. API-certified instructors for training programs. Document all qualifications and maintain training records for audit purposes.

Q6: How long must I keep inspection records?

A: Minimum: As specified in ASME B31.3, typically 5-10 years minimum. Many organizations retain records for equipment lifespan plus 10 years. Digital archives enable long-term retention. Trending analysis requires access to historical baseline data, so retention beyond minimum is recommended for risk-critical equipment.

Q7: What happens if inspection finds a defect exceeding acceptance criteria?

A: The equipment typically must be taken out of service until repaired. For some defects, engineering evaluation may justify continued operation with: Reduced operating parameters (pressure, temperature), Increased inspection frequency, Repair/replacement timeline. This requires documented fitness-for-service assessment, regulatory approval, and management sign-off. API 579 provides guidance for such evaluations.

Q8: How does ASME B31.3 address emerging inspection technologies?

A: Standards committees continuously evaluate new technologies (AI-assisted defect detection, drone-based inspections, advanced NDT methods). Current standards provide a baseline; new methods require documented validation before industry acceptance. Industry working groups and committee meetings (ASME, API, ASTM) are where technology transitions are formally evaluated and adopted.

Conclusion

ASME B31.3 is fundamental to safe, compliant operation of critical equipment. Understanding its requirements, implementing systematic inspection programs, maintaining qualified personnel, and staying current with updates ensures your organization manages risk effectively and meets regulatory expectations. Whether you're operating, maintaining, or designing equipment subject to this standard, ongoing education, professional development, and engagement with industry best practices are essential for success.

Next Steps: Review your equipment inventory against ASME B31.3 scope, audit your current inspection program for compliance gaps, engage qualified personnel to fill training or qualification gaps, and implement systematic trending analysis for better risk management. Professional consulting services can accelerate your compliance journey and optimize inspection investments.

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ASME B31.3 after start-up: where API 570 takes over

ASME B31.3 governs process piping until it enters service: design, materials, fabrication, examination and the leak test. API 570 governs the same piping afterwards: in-service inspection, rating, repair, alteration and re-rating. The two codes hand off rather than compete. API 570 says it is not a substitute for original construction requirements, and in-service repairs follow the principles of B31.3 (or the original construction code) as far as practical, with API 570 covering what B31.3 cannot.

The examination and leak-test sections above cover B31.3 during construction. This section covers the questions operating plants ask once the line is running. Which document do you open? Can B31.3 radiography criteria be applied to old welds? Does B31.3 set a minimum distance between welds? What does "B31.3 compliant" mean on a component datasheet? How do OSHA PSM and Canadian regulators fit in? ASME lists the 2024 edition of B31.3 as current, and API 570 is in its fifth edition (February 2024). Requirements below are paraphrased, not quoted. Confirm wording against licensed current copies.

The lifecycle handoff: who governs what

Design, fabrication, construction examination and the initial leak test are B31.3. Inspection planning, thickness monitoring, intervals, fitness decisions, repairs, alterations and re-rating of in-service piping are API 570, which points back to B31.3 principles for the technical details of new welds and replacement components.

ActivityGoverning documentHow the other code is involved
Pressure design, wall thickness, material selectionASME B31.3API 570 uses the B31.3 pressure-design approach to calculate required thickness and maximum allowable working pressure in service
Welding procedure and welder qualificationASME B31.3 (with ASME Section IX)API 570 repairs require qualified procedures and welders, consistent with the construction code
Construction examination (VT, RT/UT, PT/MT)ASME B31.3, by fluid service categoryNone. API 570 does not alter construction examination of new systems
Initial hydrostatic or pneumatic leak testASME B31.3When API 570 calls for a pressure test after repair or alteration, the test follows B31.3 requirements
Inspection classes, CMLs, intervalsAPI 570 (with API RP 574 practices)None. B31.3 has no in-service inspection interval rules
Corrosion rate, remaining life, next inspection dateAPI 570Minimum required thickness still comes from the B31.3 pressure-design calculation (plus structural minimums)
Repairs and alterationsAPI 570Follow the principles of B31.3 or the original code to the extent practical
Re-ratingAPI 570Calculations per the construction code or latest applicable edition
Evaluation of in-service weld flawsAPI 570 and engineering assessmentB31.3 construction acceptance criteria are not intended for this purpose

A useful rule of thumb: if the question is about how piping should be built, B31.3 answers it. If the question is about how long it can keep running, how often to look at it, or what to do when you find damage, API 570 answers it, borrowing B31.3's engineering where needed.

Repairs, alterations and re-rating: "the principles of B31.3"

API 570 tells you to follow ASME B31.3, or the code the piping was built to, to the extent practical for in-service repairs and alterations. Where B31.3 cannot be followed because it was written for new construction, the inspector or piping engineer uses API 570.

This phrase does a lot of work. It means a replacement spool should meet B31.3 material, welding and examination expectations, and a new branch connection should be reinforced to B31.3 rules. It also accepts that some things are impossible in an operating plant: you may not be able to hydrotest a tie-in weld without taking a whole unit down, or you may be welding onto pipe that is thinner than its original nominal wall. API 570 provides the in-service alternatives, such as when a pressure test can be replaced by other NDE on a closure weld and what engineering approval is needed, and these decisions belong to the owner/user's piping engineer and authorized piping inspector.

Re-rating works the same way. A line can be re-rated to a new pressure or temperature when calculations are performed to the code the piping was built to or the latest edition of the applicable code. The maximum allowable working pressure formula in API 570's annex uses the B31.3 pressure design equation with corroded thickness. The thickness inputs come from in-service inspection data, which is why reliable UT thickness readings matter so much.

Repair organisation, authorization and documentation requirements sit in API 570. The construction code does not know who your authorized inspector is; API 570 does.

The radiography trap: B31.3 acceptance criteria are not in-service criteria

B31.3's radiography acceptance criteria apply to a random sample of new welds to judge the probable quality of all welds in a lot. API 570 cautions that applying those workmanship criteria to in-service welds may not be appropriate. Flaws found in service should be evaluated for their actual significance.

This is the most common technical misunderstanding between the two codes. During construction, B31.3 requires a stated percentage of welds to be examined, and the acceptance criteria are workmanship standards. They show whether the welder and procedure are producing acceptable quality, and if a sample fails, more welds are examined. The examination extents by fluid service are summarised in the table earlier on this page.

That sampling logic has consequences. A plant that has been operating for twenty years has thousands of welds that were never radiographed. If an in-service radiograph of one of them shows a slag line that B31.3 would reject, the weld has not suddenly become dangerous. It has been there since construction and has carried pressure for twenty years. API 570 recognises this and directs that such findings be assessed for their effect on integrity, considering the service, any active damage mechanism and whether the indication is growing. Assessments of that kind may draw on fitness-for-service methods, an engineering evaluation the owner commissions.

The opposite mistake also happens. Some programmes treat a weld that "passed RT at construction" as immune to cracking in service. Construction RT says nothing about later environmental cracking such as wet H2S damage, chloride stress corrosion cracking or caustic cracking. In-service damage needs in-service methods: shear-wave UT, phased array, TOFD or wet fluorescent MT, chosen for the mechanism.

Fluid service categories vs API 570 piping classes

B31.3 classifies piping by fluid service (Normal, Category D, Category M, High Pressure, High Purity) to set construction rules. API 570 classifies in-service piping into Classes 1 to 4 by consequence of a leak to set inspection intervals. The two schemes overlap, but one does not convert directly into the other.

The construction category is fixed at design. API 570's scope list then decides whether the line is in the in-service programme at all. Process fluids, hydrocarbons, flammable and toxic services, hydrogen, fuel gas and flare systems, sour water, hazardous waste and cryogenic fluids are included. Several services are optional at the owner/user's discretion, including water, steam, steam condensate, boiler feed water and B31.3 Category D services. A Category D utility line built to B31.3 may or may not be in your API 570 programme, depending on what the owner decided and documented.

For piping in the programme, API 570 assigns a class. Class 1 covers the highest-consequence services, such as flammable services that can auto-refrigerate and cause brittle fracture. Class 2 covers most unit process piping. Class 3 covers flammable services that do not significantly vaporise and many off-site lines. Class 4 covers essentially nonflammable, nontoxic services. Each class has maximum intervals for thickness measurement and external visual inspection, and the thickness interval is also limited by remaining life. Owners may set intervals with RBI, which API 570 permits as an engineering programme they commission. Take the interval numbers from the current fifth edition, not from older copies circulating online. A Category M line is not automatically Class 1, and a Normal-service hydrocarbon line can be Class 1 or Class 3 depending on what happens if it leaks.

Pressure testing after repairs: B31.3 rules, API 570 judgement

B31.3 requires a leak test before new piping enters service. API 570 says pressure tests are not normally part of routine in-service inspection. When one is performed after a repair or alteration it follows B31.3, and the inspector decides whether one is needed at all.

This is one of the most useful practical differences between the codes. A tie-in weld on a live unit often cannot be hydrotested without taking down far more than the repaired spool. API 570 provides a documented route for accepting certain closure welds on NDE instead. That usually means full volumetric examination plus surface examination, with engineering review and the conditions set out in the code. B31.3 alone does not offer that route for in-service work, because it was written for systems that can be tested before start-up. When the owner's inspector does call for a pressure test after repair, the test pressure, medium and hold follow the B31.3 rules described earlier on this page.

Minimum distance between welds in ASME B31.3

ASME B31.3 does not set a general minimum distance between adjacent girth welds. ASME answered this in a published interpretation: apart from the branch-connection reinforcement rules, the code has no such requirement. Spacing limits found on projects come from owner or EPC specifications.

This question comes up constantly. Shop and site supervisors are told to keep welds a certain distance apart, assume the rule comes from the code, and cannot find it in B31.3. The rule is usually in the project piping specification. Common reasons owners impose one:

  • Overlapping heat-affected zones. Two welds very close together put two weld thermal cycles and two residual-stress fields into the same short length of pipe, which some owners want to avoid in services where toughness or cracking resistance matters.
  • Examination access. UT, PAUT and radiography all need room. A pup piece shorter than the probe footprint or film coverage can make a weld impossible to examine properly, both at construction and decades later under API 570.
  • Reinforcement zones. Branch connections need reinforcement within a defined zone, and welds crowded into that zone complicate the calculation. This is the one area where the code itself constrains proximity.
  • Fit-up and distortion. Very short spools are hard to align and may distort.

Rules of thumb such as a multiple of the pipe diameter, or a fixed minimum length for pup pieces, are company and project choices. If your specification has one, it governs your job, but it is not a B31.3 requirement. For in-service piping, weld proximity matters for a different reason: a repair sleeve or replacement spool welded close to an old weld creates exactly the access problem that makes later CML readings and crack examination unreliable. Plan repairs with the next inspection in mind, and ask us to review examination access before a spool is fabricated. (The interpretation is reported in secondary sources; check it in ASME's interpretation index for your edition.)

What "B31.3 compliant" means for filters, strainers and other components

A component is acceptable under B31.3 either because it is a listed component made to a standard the code accepts, or because it is an unlisted component whose pressure design has been qualified by a method the code permits. "B31.3 compliant" on a datasheet should tell you which route applies.

Inline filters, strainers, sight glasses, flexible hoses and special fittings are frequent sources of confusion. For a listed component, the manufacturer should cite the product standard and pressure-temperature rating. For an unlisted component, ask for the design basis: calculation, proof test or experience-based qualification as the code allows, plus materials and rating. Some larger filter housings are designed as pressure vessels under ASME Section VIII instead. That changes the governing construction code, and later the in-service code too, because the vessel then falls under the owner's API 510 programme rather than API 570. ASME's change list for B31.3 2024 includes unlisted valves, so check the current edition when buying. In service, these components often become the weak point: thin bodies, dissimilar metals and dead spaces where corrosion concentrates. Include them in the CML plan rather than assuming they match the line.

NDE methods on each side of the handoff

Construction NDE under B31.3 is about weld quality: VT, RT or UT of a defined sample, and MT or PT where required. In-service NDE under API 570 is about damage: UT thickness at CMLs, profile radiography, corrosion mapping, guided wave screening, and crack detection methods chosen for the damage mechanism.

PurposeTypical methodsWhat it findsLimits
B31.3 construction examinationVT, RT, UT (including PAUT/TOFD where specified), MT, PTWelding defects against workmanship criteriaSampling: only examined welds are known
API 570 thickness monitoringUT thickness at CMLs, profile RTGeneral wall loss, corrosion rateSpot readings can miss localised loss
Localised corrosion, erosionCorrosion mapping, PAUT, profile RTPitting, erosion patterns, injection-point damageAccess, surface condition, insulation removal
Long runs, limited accessGuided wave testingScreening for metal loss over distanceScreening only; prove up with UT
Environmental crackingShear-wave UT, PAUT, TOFD, WFMTHIC, SOHIC, SCC, fatigue cracksNeeds a qualified procedure and a defined mechanism
Corrosion under insulationVT with stripping, profile RT, pulsed eddy current screeningExternal wall loss under insulationScreening methods need verification

API 570 also identifies certain in-service ultrasonic shear-wave applications where examiners should have passed a performance demonstration. Check your edition and owner specification for when this applies. For in-service piping see the API 570 piping inspection guide and piping circuit CML inspection.

The regulatory overlay: PSM, jurisdictions and Canada

In the US, OSHA PSM requires inspection and testing that follow RAGAGEP, and for in-service process piping most employers cite API 570 while citing B31.3 for design and construction. In Canada, provinces adopt construction codes through CSA B51 and provincial regulations and reference API 570 for in-service inspection.

Under 29 CFR 1910.119(j), piping systems including valves are covered equipment. Inspection and testing must follow recognized and generally accepted good engineering practices, at frequencies consistent with manufacturers' recommendations and good engineering practice, and each inspection must be documented with the date, the person who performed it, an equipment identifier, a description of the test and the results. OSHA's RAGAGEP guidance treats "shall" provisions of a consensus code as mandatory and expects departures from "should" provisions to be documented. In practice, a facility's mechanical integrity programme cites B31.3 for new and modified piping and API 570 with API RP 574 for in-service inspection. For equipment designed to codes no longer in general use, the employer must document that it is designed, maintained, inspected, tested and operating safely.

US state boiler and pressure vessel laws generally focus on boilers and vessels rather than process piping, so the main legal driver for piping inspection is PSM (and EPA RMP where it applies). Confirm with your state if you are unsure.

In Canada, provincial regulators register and enforce pressure piping construction, typically referencing ASME B31.3 through CSA B51 and provincial pressure equipment legislation. For in-service work, Technical Safety BC lists API 570 among the codes referenced through its adoption of CSA B51, and Alberta applies API codes through ABSA's AB-506 owner-user requirements rather than adopting them directly. Ontario's TSSA framework has its own amendments. Requirements differ by province, so confirm with your provincial regulator.

How Atlantis supports both sides

Atlantis performs construction NDE to B31.3 (RT through licensed radiography crews where the work is, UT, phased array, TOFD, MT, PT and VT) and in-service NDE under the owner's API 570 programme: CML thickness surveys, profile RT, corrosion mapping and guided wave screening. Technicians are ASNT-certified under ASNT Level III oversight. Acceptance, interval and repair decisions stay with the owner's authorized piping inspector and engineer. We do not perform RBI or fitness-for-service assessments. Request a piping NDE quote; we reply within 24 hours.

More questions about B31.3 in operating plants

Is B31.3 used for in-service piping?

Not as an inspection code. In-service inspection, rating, repair and alteration fall under API 570 or the owner's equivalent RAGAGEP. B31.3 still matters in service: repairs follow its principles where practical, and its pressure-design equation supplies the required thickness used in remaining-life calculations.

What is the difference between API 570 and ASME B31.3?

B31.3 governs building new process piping; API 570 governs inspecting and maintaining that piping once in service. API 570 does not replace construction requirements, and B31.3 does not set inspection intervals. See also our B31.3 code overview.

Can I use B31.3 radiography acceptance criteria on in-service welds?

API 570 cautions that this may not be appropriate, because B31.3 criteria are workmanship standards applied to a sample of new welds. In-service indications should be evaluated for their effect on integrity by the owner's inspector and engineer. Ask about in-service weld examination.

Use this page as a requirements review checklist

For a project review, identify the adopted code edition, fluid service, piping scope, design basis, material specifications, examination plan, personnel qualifications and required records. Assign responsibility for checking each item against the licensed code and project documents. Do not infer a universal examination percentage or acceptance value from a general article.

For the wider framework, read the B31.3 code overview. ASME describes the scope on its official B31.3 page. Consulting support can help scope the document review.

ASME B31.3 scales weld examination to fluid service, not to pipe size. Normal Fluid Service requires random radiography or ultrasonic examination of at least 5% of circumferential butt and miter groove welds, with every welder represented. Category D requires visual examination only. Severe Cyclic Conditions requires 100% radiography of those welds plus 100% surface examination of fillet and socket welds.

Fluid service is decided in design, before any weld is made. Category D covers nonflammable, nontoxic fluid at design gauge pressure not exceeding 150 psi and design temperature between −20°F and 366°F. Category M covers fluid where a single exposure to a very small leaked quantity can cause serious irreversible harm. High Pressure Fluid Service is Chapter IX, invoked by the owner when pressure exceeds ASME B16.5 Class 2500 limits for that material and design temperature. Everything else is Normal Fluid Service. Under Normal Fluid Service the 5% random radiography sample must include work from every welder and welding operator, and in-process examination per para. 344.7 may be substituted where the engineering design specifies it. When a sampled weld fails, para. 341.3.4 progressive sampling requires two additional welds of the same kind by the same welder; if either fails, two more for each, until the extent of the deficient work is established.

Source: ASME B31.3 Process Piping (2022 edition; the 2024 edition, issued December 2024, is current — check paragraph changes) — para. 341.4 Extent of Required Examination, para. 341.3.4 Progressive Sampling for Examination, Table 341.3.2 Acceptance Criteria for Welds, para. 300.2 Definitions, and para. 345 Leak Tests.

Technically reviewed by Anoop Rayavarapu — ASNT NDT Level III (UT, RT, MT, PT, VT, ET)
ASME B31.3 examination and leak test by fluid service
Fluid serviceWeld examination minimumVisual examinationLeak testCode location
Category DNo radiography or ultrasonic examination requiredVisual examination per para. 344.2Initial service leak test permitted in place of hydrostaticpara. 341.4.2
Normal Fluid ServiceAt least 5% of circumferential butt and miter groove welds by random RT or UT, every welder representedAt least 5% of fabrication; 100% of longitudinal welds not made to a listed specificationHydrostatic at 1.5 × design pressure, corrected by the stress ratio at test temperaturepara. 341.4.1
Severe Cyclic Conditions100% radiography of circumferential butt and miter groove welds; 100% magnetic particle or penetrant on fillet, socket and branch welds100% of fabricationHydrostaticpara. 341.4
Category M (Chapter VIII)Chapter VIII raises the Normal Fluid Service requirement; visual coverage goes above the 5% sampleSet by Chapter VIII, above the Normal Fluid Service sampleSensitive leak test required in addition to the specified leak testChapter VIII, para. M341.4 with para. 345.1
High Pressure Fluid Service (Chapter IX)100% volumetric examination of welds by radiography or ultrasonics, plus 100% surface examination100%Hydrostatic per Chapter IXChapter IX, para. K341.4
These are code minimums. The engineering design, owner's specification or jurisdiction can raise any of them and frequently does; none of them can be lowered.

Does ASME B31.3 require 100% radiography of piping welds?

No. Only Severe Cyclic Conditions and Chapter IX High Pressure Fluid Service demand 100% volumetric examination. Normal Fluid Service stops at 5% random radiography or ultrasonics of circumferential butt and miter groove welds, and Category D needs no volumetric examination at all. Owners who want 100% on a Normal Fluid Service line buy it through the engineering design, not through the code.

What hydrostatic test pressure does ASME B31.3 require?

1.5 times design pressure. When test temperature differs from design temperature, the test pressure is multiplied by the ratio of allowable stress at test temperature to allowable stress at design temperature, capped so the test does not yield the piping. Pneumatic testing is the alternative when hydrostatic is impractical, run at a lower multiple of design pressure with a stepped pressurisation sequence.

Who is qualified to perform examinations under ASME B31.3?

Two separate roles. The examiner works under para. 342: qualified by training and experience under the employer's written practice, with ASNT SNT-TC-1A or ASME BPVC Section V Article 1 as the usual basis. The Owner's Inspector under para. 340.4 is a different person, requiring 10 years of experience in design, fabrication or inspection of industrial pressure piping, with engineering education creditable up to 5 of those years.

What happens when a randomly examined weld fails?

Progressive sampling under para. 341.3.4 takes over. Two additional welds of the same kind made by the same welder or operator must be examined by the same method. If either of those fails, two further welds are examined for each failure. The escalation continues until the extent of the deficient work is established, or the welder's work of that kind is fully examined and repaired.

When does ASME B31.3 require post-weld heat treatment?

Table 331.1.1 sets PWHT by base metal P-Number and nominal wall thickness. P-No. 1 carbon steel requires PWHT above 3/4 in. (19 mm) nominal thickness. Soak time is 1 hour per inch of thickness with a 15-minute minimum, at the metal temperature band listed for that P-Number, with heating and cooling rate limits and recorded thermocouple traces as the audit evidence.

How does ASME B31.3 differ from ASME B31.1?

B31.3 governs process piping in refineries, chemical plants and gas processing, and sets examination by fluid service category. B31.1 governs power piping and boiler external piping, is referenced by ASME BPVC Section I, and sets examination by pipe size, wall thickness and pressure class under state boiler-code jurisdiction. A plant with both a process unit and a steam plant runs both codes on the same site.