Views: 3 Author: Monica Publish Time: 2026-05-25 Origin: Site
To select the right nickel alloy pipe for offshore oil and gas, you must first characterize the service environment (temperature, chloride content, H2S partial pressure, CO2, and pH), then match those conditions to the alloy family (Inconel, Hastelloy, Monel, or Alloy 825/20), verify compliance with the applicable codes (NACE MR0175, ASME B31.3, DNV-ST-F101, API 5CRA), and confirm traceability through mill test reports. Inconel 625 is the most versatile all-rounder; Hastelloy C-276 is the benchmark for acid-chloride extremes; Alloy 825 is the preferred cost-effective solution for NACE-qualified sour service. |
Offshore oil and gas environments are among the most demanding on earth for metallic materials. A platform operating in the North Sea, Gulf of Mexico, or Southeast Asian waters simultaneously exposes piping systems to salt-laden air, chloride-rich seawater, hydrogen sulfide (H2S), carbon dioxide (CO2), high pressures, cyclic mechanical loads, and temperatures that can swing from sub-zero to over 150 degrees C — sometimes within the same system.
Carbon steel corrodes rapidly in these conditions. Even premium duplex and super-duplex stainless steels reach their limits in hot seawater above 35 degrees C, concentrated acid streams, or high-pressure sour gas wells where H2S partial pressures exceed 0.05 psia.
Specifying the correct nickel alloy pipe is the lowest-cost option over the field's lifetime.
Selecting a nickel alloy pipe is not a single decision — it is a structured engineering process. Follow these six steps in order. Skipping any step increases the risk of under-specification (premature failure) or over-specification (unnecessary cost).
Before opening any alloy catalogue, document every relevant parameter of the service environment. These parameters drive every subsequent decision:
• Operating temperature range (minimum and maximum, including upset conditions)
• Chloride ion concentration in the fluid or surrounding environment (ppm)
• H2S partial pressure (psia) — critical for NACE MR0175 qualification
• CO2 partial pressure (psia) — affects pH and carbonic acid corrosion rate
• pH of produced fluids (low pH accelerates corrosion dramatically)
• Oxygen content — even trace dissolved O2 dramatically accelerates chloride pitting
• Flow velocity — erosion-corrosion threshold must be evaluated
• Cyclic loading — fatigue resistance is critical for risers and flexible joints
• External environment — splash zone, submerged, buried, or atmospheric
Engineering Rule: If any of the following conditions apply, standard duplex stainless steel is insufficient and a nickel alloy must be evaluated: H2S partial pressure above 0.05 psia; chloride concentration above 150,000 ppm at temperatures above 60 degrees C; pH below 3.5; or the presence of free sulfur or strong reducing acids. |
The Pitting Resistance Equivalent Number (PREN) is a calculated index that predicts an alloy's resistance to pitting corrosion in chloride environments. The formula is:
PREN = %Cr + 3.3 x %Mo + 16 x %N
As a practical guide: a PREN above 40 is required for continuous seawater immersion; above 50 for hot seawater or concentrated chloride brine; and the best nickel alloys (Hastelloy C-22) exceed PREN 65, placing them beyond the reach of any standard stainless steel.
However, PREN alone is not sufficient for nickel alloys because their corrosion performance in complex mixed-acid environments (where both chloride pitting and general acid attack occur simultaneously) is better evaluated through published isocorrosion charts and laboratory coupon testing. Use PREN as a first filter, then validate with corrosion engineering data.
Different service conditions cause different forms of corrosion attack. Identifying the dominant failure mode guides alloy selection more accurately than PREN alone:
Pitting corrosion: driven by chlorides. Requires high Cr + Mo content. Inconel 625, Hastelloy C-276 are primary choices.
Crevice corrosion: occurs under gaskets, at flanged joints, or in stagnant zones. Super-alloys with high Mo (>13%) resist this. Alloy C-22 excels.
Stress Corrosion Cracking (SCC): triggered by tensile stress + chlorides at elevated temperature. Austenitic stainless steels are highly susceptible; nickel alloys with >30% Ni are immune.
Hydrogen Induced Cracking (HIC) / Sulfide SCC: driven by H2S. Governed by NACE MR0175 / ISO 15156. Alloy 825 and 625 are qualified.
Erosion-Corrosion: high-velocity fluids carrying sand particles. High-strength alloys (Inconel 718, Alloy 625) with good hardness resist this mode.
General acid attack: in streams containing HCl, H2SO4, or HF. Hastelloy grades are specifically engineered for acid service.
With the service environment characterized and dominant failure modes identified, use the decision matrix below to shortlist appropriate alloy families. The four main nickel alloy families for offshore service are:
Inconel alloys (Ni-Cr-Mo-Nb): excellent all-round performance; Inconel 625 is the default choice for most aggressive offshore piping applications.
Hastelloy alloys (Ni-Mo-Cr): engineered for acid and mixed-acid environments; Hastelloy C276 and C22 are the industry benchmarks.
Monel alloys (Ni-Cu): exceptional in seawater and hydrofluoric acid; Monel 400 is the standard for saltwater cooling systems and brine handling.
Alloy 825 / Alloy 20 (Ni-Cr-Mo-Cu): the most cost-effective nickel alloys for sour-gas wells and general offshore process piping qualifying under NACE MR0175.
Nickel Alloy Grade Comparison: Offshore Service Properties
The table below presents standardized mechanical and corrosion data for the eight nickel alloys most commonly specified for offshore oil and gas service. All minimum values reflect ASTM/EN standards.
Alloy (UNS) | Min. UTS | Corr. Resistance | PREN | Primary Offshore Application |
Inconel 625 (N06625) | 760 MPa | Exceptional | >50 | Risers, subsea jumpers, topsides in aggressive chloride environments |
Inconel 718 (N07718) | 1034 MPa | Good | ~35 | High-strength fasteners, downhole components, wellhead equipment |
Hastelloy C-276 (N10276) | 690 MPa | Superior | >44 | FGD systems, sour gas pipelines, HCl-rich process streams |
Hastelloy C-22 (N06022) | 690 MPa | Exceptional | >48 | Mixed-acid environments, wet chlorine, flue-gas scrubbers |
Monel 400 (N04400) | 517 MPa | Very Good | ~20 | Seawater cooling lines, brine systems, hydrofluoric acid service |
Alloy 825 (N08825) | 586 MPa | Excellent | ~32 | Sour-gas wells (NACE MR0175), heat exchangers, pickling equipment |
Alloy 20 (N08020) | 551 MPa | Excellent | ~26 | Sulfuric acid piping, food-grade chemical plants |
Alloy 31 (N08031) | 650 MPa | Superior | >40 | Hot concentrated chloride, H2SO4/HCl mixed acid, FGD scrubbers |
Sources: ASTM B444, B622, B725, B163; ASME Section II Part B; NACE MR0175 / ISO 15156. PREN values are nominal based on typical composition; certified heat chemistry must be verified. UTS = Ultimate Tensile Strength at room temperature.
Environment-to-Alloy Decision Matrix: Which Grade for Which System?
Use the matrix below to map your specific offshore service environment to the most appropriate alloy shortlist. Cross-reference with your PREN calculation and failure mode analysis from Steps 2 and 3.
Service Environment | Key Corrosive Factor | Recommended Alloy(s) | Key Standard |
Open seawater (ambient T) | Chloride: 19,000+ ppm | Monel 400, Alloy 625, Alloy C-276 | ASME B31.3; DNV-ST-F101 |
Sour gas (H2S present) | H2S + CO2 + chloride | Alloy 825, Alloy C-276, Alloy 625 | NACE MR0175 / ISO 15156 |
Hot brine injection | Cl- > 50,000 ppm, T > 80 degC | Alloy 625, Alloy C-22 | API 5CRA; NACE MR0175 |
Topsides process piping | H2S + CO2 + O2 | Alloy 625, Alloy C-276 | ASME B31.3; ISO 15156 |
Subsea umbilical (small OD) | Seawater + cyclic load | Alloy 625 (seamless) | DNV-ST-F101; API 17E |
Flue gas desulfurization | SO2 + HCl + wet Cl- | Alloy C-276, Alloy 31, Alloy C-22 | ASTM B619 / B622 |
Downhole tubing (sour well) | H2S > 0.05 psia partial press. | Alloy 825, Alloy C-276 | NACE MR0175 HRC 40 max |
Cryogenic / LNG transfer | Temp down to -196 degC | Alloy 625, Alloy 718 (FCC structure) | ASTM B444; ASME VIII Div.1 |
* Alloy selections are primary recommendations. Final selection must be confirmed through corrosion engineering review, isocorrosion chart analysis, and verification against applicable project specifications and operator standards.
Nickel alloy pipe for offshore service does not simply need to meet chemical composition requirements — it must comply with a comprehensive framework of international standards governing material qualification, design, fabrication, testing, and inspection. Non-compliance discovered during project review or third-party inspection can halt procurement, delay installation, and trigger contractual penalties.
Standard | Category | Scope | Offshore Relevance |
ASTM B444 | Pipe & tube | Inconel 625 seamless pipe and tube | Most widely cited for subsea applications |
ASTM B622 | Pipe & tube | Hastelloy C-276 / C-22 seamless pipe | Mandatory for FGD and aggressive acid service |
ASTM B619 | Welded pipe | Hastelloy welded pipe | Alternative to seamless in larger diameters |
ASTM B725 | Welded pipe | Alloy 825 / 20 welded pipe | Chemical and sour-gas service |
ASTM B163 | Tubing | Condenser and heat-exchanger tube (many nickel alloys) | Offshore heat exchangers |
ASME B31.3 | Piping code | Process piping design, testing, inspection | Governs topsides and offshore piping systems |
API 5CRA | Downhole tubulars | Corrosion-resistant alloy tubing for wells | Alloy 825, 625, 716 for sour wells |
NACE MR0175 | Material selection | Materials for sour-service H2S environments | Mandatory on virtually all offshore projects |
DNV-ST-F101 | Subsea pipelines | Submarine pipeline systems including CRA pipe | Required by most North Sea operators |
ISO 15156 | Material selection | International equivalent of NACE MR0175 | Globally accepted; required by many operators |
Standards listed are current editions as of 2025. Always verify the edition required by the specific project specification and operator engineering standards. Some operators (Shell DEP, ExxonMobil GP, BP GS, Equinor TR) impose additional requirements beyond the base standards listed.
Key Compliance Requirements by Application
Sour Service (H2S-containing environments)
Any nickel alloy pipe intended for sour service — defined as H2S partial pressure exceeding 0.05 psia (0.0003 MPa) in the gas phase — must be qualified to NACE MR0175 / ISO 15156. Key requirements include:
• Hardness: HRC 40 maximum for most nickel alloys in H2S environments (Alloy 718 has specific hardness limits)
• Heat treatment: solution-annealed condition required for Alloy 825 and 625; precipitation-hardened grades require specific qualification
• Cold work: limits on cold reduction after final heat treatment to control residual stress
• Full traceability: heat number, lot number, and certified material test report (CMTR) mandatory on all components
Subsea Pipeline Systems
Pipe for use in subsea corrosion-resistant alloy (CRA) linepipe systems must comply with DNV-ST-F101 (formerly DNV-OS-F101) and typically also with API 5CRA. Critical requirements include:
• Full-length ultrasonic testing (UT) of pipe body and weld seams
• Corrosion fatigue testing for cathodic protection compatibility (subsea CRA pipe must not be over-protected)
• Dimensional inspection per ISO 11960 or equivalent
• Factory acceptance testing (FAT) witnessed by third-party inspection agency
Topsides Process Piping
Nickel alloy piping for topsides process service is governed primarily by ASME B31.3 (Process Piping). Key requirements include pressure design calculations, weld procedure qualification (WPS/PQR) per ASME IX, NDE per ASME B31.3 Appendix, and positive material identification (PMI) on 100% of alloy components.
Once the alloy family and grade are confirmed and code compliance requirements are established, the final specification must define the exact pipe form and procurement requirements.
Seamless vs. Welded Nickel Alloy Pipe
Seamless pipe (ASTM B444, B622, B829): no longitudinal weld seam, superior pressure integrity, preferred for all critical and high-pressure applications. Readily available in sizes up to NPS 6"; larger sizes require extended lead times.
Welded pipe (ASTM B619, B725): economical for larger diameters (NPS 8" and above) and lower-pressure applications. Weld seam must be fully radiographed (Class 1) for pressure-critical service. Less suitable for corrosive environments where the weld HAZ is a preferential attack site.
Best Practice: For offshore critical service — risers, subsea flowlines, downhole tubing, and high-pressure process piping — always specify seamless pipe. Reserve welded pipe for low-pressure utility systems (firewater, cooling water, HVAC) or large-diameter topsides headers where seamless is unavailable. |
Pipe Dimensions and Schedule
Nickel alloy pipe is dimensioned per ASME B36.19M (stainless and nickel alloy pipe) or ASME B36.10M (carbon steel pipe, sometimes referenced for nominal sizes). Key points:
• Nominal Pipe Size (NPS) from 1/4" to 24" and above are available; confirm manufacturer stock sizes
• Wall thickness (Schedule): SCH 10S, 40S, 80S for thin-to-heavy wall; SCH 160 and XXS available in smaller sizes
• Tolerance: outer diameter (OD) tolerance per ASTM standard is typically +/-1% for NPS 1.5" and above
• Surface finish: specify ID surface finish for process piping (Ra 3.2 um is typical for chemical service); OD finish for visual inspection acceptance
Mandatory Testing and Inspection Requirements
The following tests should be specified for all offshore-grade nickel alloy pipe procurement. Confirm which are mandatory per your applicable code and which are supplementary:
1. Chemical composition analysis (per applicable ASTM standard, on each heat)
2. Mechanical property testing: UTS, yield strength, elongation (on each heat/lot)
3. Hardness testing (mandatory for sour service NACE MR0175 qualification)
4. Hydrostatic pressure test (per ASTM standard; alternative: NDE with UT or RT)
5. Non-destructive examination: 100% UT (pipe body) + 100% RT (welds for welded pipe)
6. Intergranular corrosion test (ASTM A262 Practice E for austenitic grades; confirms sensitization-free condition)
7. Positive Material Identification (PMI): 100% of alloy pipe and fittings using XRF or OES
8. Dimensional inspection: OD, wall thickness (WT), straightness, end squareness
Nickel alloys carry a significant cost premium over stainless steel — typically 3x to 15x the cost per kilogram depending on the grade. However, the correct comparison is not initial material cost but total lifecycle cost over the field's design life (typically 25-30 years for offshore installations).
Alloy / Grade | Relative Cost | Corrosion Perf. | Expected Service Life | When to Use It |
316L Stainless | Low | Moderate | 5-10 years | General utility piping only; not for sour or hot seawater |
Duplex 2205 | Low-Medium | Good | 10-20 years | General offshore piping; not for hot concentrated chloride |
Super Duplex 2507 | Medium | Very Good | 15-25 years | Seawater systems; avoid HCl or high-temp strong acids |
Alloy 825 | Medium-High | Excellent | 20-30 years | Sour-gas wells; excellent value for NACE-qualified service |
Alloy 625 | High | Exceptional | 25+ years | Best all-rounder for aggressive offshore environments |
Hastelloy C-276 | High | Superior | 25+ years | Acid/chloride extremes; replace 625 where SO2 is present |
Hastelloy C-22 | Very High | Exceptional+ | 30+ years | Absolute worst-case mixed-acid or wet-chlorine service |
Relative cost is indicative, based on 2024-2025 global nickel alloy market pricing. Actual pricing varies by product form, size, quantity, and market conditions. Expected service life is indicative for the stated application; actual life depends on operating parameters, maintenance practice, and inspection regime.
When evaluating cost, consider these lifecycle cost elements beyond initial material price:
• Inspection and maintenance cost: higher-grade alloys require significantly less frequent inspection, reducing operational expenditure
• Replacement and intervention cost: offshore pipe replacement typically costs 10x to 50x the original material value due to mobilization, installation, and production deferral costs
• Risk cost: the consequence of a piping failure (production loss, environmental penalty, safety incident) must be quantified in the material selection risk assessment
• Insurance premium impact: premium alloy piping systems may attract lower insurance premiums due to reduced failure probability
Lifecycle Cost Principle: A field producing 30,000 barrels of oil per day earns approximately 2.1 million USD per day at 70 USD/bbl. A 10-day production shutdown caused by a piping failure costs 21 million USD in lost revenue alone — far exceeding the total cost of specifying Inconel 625 instead of duplex steel for every critical system on the platform. |
Use the following checklist when preparing a purchase order or material requisition for offshore nickel alloy pipe. All items should be confirmed in writing with the manufacturer before order placement.
On the Purchase Order / Material Requisition
• Alloy grade with full UNS designation (e.g., UNS N06625, not just 'Inconel 625')
• Applicable ASTM/EN product standard (e.g., ASTM B444 Grade 2)
• Nominal pipe size (NPS) and nominal wall thickness (or schedule designation)
• Pipe end condition: plain end (PE), beveled end (BE), or threaded (TE)
• Quantity in linear meters or pieces, with length tolerance
• Heat treatment condition: solution annealed and quenched (state temper if applicable)
• NACE MR0175 / ISO 15156 compliance: state required if for sour service
• Supplementary testing requirements: IG corrosion test, PMI, third-party inspection
• Documentation requirements: EN 10204 Type 3.1 or 3.2 certificate; radiographic reports
• Country of manufacture and mill qualification: require approved mill list compliance if applicable
At Mill Test Report (MTR) Review
• Confirm UNS number and product standard match the purchase order exactly
• Verify all elemental chemistry values are within specified limits for the grade
• Confirm heat number traceability connects raw material to finished pipe
• Check hardness values meet NACE MR0175 limits for sour service (HRC 40 max)
• Verify tensile, yield, and elongation values meet or exceed ASTM minimums
• Confirm heat treatment condition and temperature are documented
• For welded pipe: confirm 100% RT acceptance on all weld seams
• Verify PMI results are present and match nominal composition
• Check inspector certification and accreditation body (SGS, BV, Lloyds, TUV)
Mistake 1: Specifying Grade by Name Without the UNS Number
'Inconel 625' is a trade name, not an engineering specification. Different manufacturers produce 625 with chemical compositions at different points within the allowed range, which affects PREN, weld ability, and corrosion performance. Always specify the UNS designation (N06625) and the ASTM product standard (ASTM B444). This binds the supplier to a legally verifiable specification.
Mistake 2: Ignoring the Heat-Affected Zone (HAZ) in Welded Systems
In nickel alloy welded pipe, the HAZ adjacent to the weld seam may have different grain structure, residual stress, and local composition compared to the base metal. For corrosive offshore service, the HAZ is often the first location to fail. Always specify: post-weld solution annealing for sensitization-prone grades; HAZ hardness limits for NACE service; and full radiographic or ultrasonic examination of weld seams and the HAZ width.
Mistake 3: Confusing Nominal PREN with Certified PREN
Published PREN values are calculated from the nominal (midpoint) composition of the alloy. The actual PREN of a specific heat of material depends on the certified chemistry in the MTR. For critical offshore service, calculate PREN from the actual heat chemistry, not the nominal. A heat of Alloy 625 at the low end of the Cr and Mo specification ranges can have a PREN 3-5 points below the nominal value — which may matter in hot seawater service.
Mistake 4: Applying NACE MR0175 Without Reading the Fine Print
NACE MR0175 / ISO 15156 is not a blanket approval document. It lists qualified materials with specific conditions: maximum hardness limits, maximum yield strength limits, heat treatment requirements, and in some cases, limits on cold work and testing protocols. Alloy 625 and 825 are listed in Part 3 — but the listing applies only when specific conditions are met. Review the applicable table in Part 3 carefully and verify that your pipe specification meets all listed conditions.
Mistake 5: Using a Generic Filler Metal for Dissimilar Metal Welds
Offshore systems frequently involve dissimilar metal welds — for example, a nickel alloy pipe welded to a duplex stainless steel fitting, or a CRA overlay on a carbon steel pipe. Using an incorrect filler metal can create a galvanic couple, reduce weld toughness, or produce a HAZ that is susceptible to SCC or HIC. For all dissimilar metal welds, obtain a welding engineering review and specify the filler metal by AWS/SFA classification (e.g., AWS ERNiCrMo-3 for Inconel 625 to duplex welds).
What is the most versatile nickel alloy for offshore piping?
Inconel 625 (UNS N06625) is widely considered the most versatile nickel alloy for offshore service. It offers a PREN above 50, excellent resistance to both chloride pitting and crevice corrosion, qualification under NACE MR0175, outstanding fatigue resistance (critical for dynamic risers), and a well-established record of performance in the North Sea, Gulf of Mexico, and Asia-Pacific offshore environments. When in doubt on a new project, 625 is the conservative starting point from which deviations downward (to a less expensive alloy) must be justified.
What is the difference between Inconel 625 and Hastelloy C-276?
Both are nickel-chromium-molybdenum alloys with exceptional corrosion resistance, but they have different strengths. Inconel 625 has higher tensile strength (760 vs 690 MPa minimum UTS), higher niobium content for weld strength retention, and better fatigue performance — making it the preferred choice for structural piping, risers, and high-pressure systems. Hastelloy C-276 has higher molybdenum content (~16% vs ~9%) and lower carbon, giving it superior resistance to reducing acids (HCl, H2SO4), wet chlorine, and flue gas environments where sulfur compounds are present alongside chlorides. If the corrosive medium contains strong reducing acids, C-276 is the better choice. For general offshore seawater and sour-gas service, 625 is more cost-effective and mechanically superior.
Can nickel alloy pipe be welded in the field?
Yes, but with stringent controls. Nickel alloys can be welded using GTAW (TIG), GMAW (MIG), SMAW, and SAW processes, but each requires a qualified welding procedure specification (WPS) and procedure qualification record (PQR) per ASME IX or equivalent. Key requirements: use matching or approved over-alloyed filler metals; control interpass temperature (maximum 150 degrees C for most nickel alloys); clean thoroughly before welding (no iron contamination); and perform post-weld PMI on filler and base metal to detect accidental substitution. For offshore site welding, specify an approved weld procedure and ensure welder qualification includes continuity records.
How do I compare nickel alloy pipe quotes from different suppliers?
Comparing nickel alloy pipe quotes requires more than price per kilogram. Verify: (1) Mill origin — request the specific mill name and confirm it is on your approved supplier list; (2) Product standard — ASTM B444 is not the same as an equivalent-grade pipe supplied to DIN or JIS; (3) Testing scope — some suppliers quote with hydrostatic test only, others include UT, RT, and IGC testing in the base price; (4) Certificate type — EN 10204 Type 3.1 (mill-certified) is the minimum for offshore; Type 3.2 (third-party witnessed) is required on many projects; (5) Lead time — premium nickel alloys in large quantities may have 12-20 week lead times; confirm before committing; (6) PMI — confirm that PMI is included and will be documented on the MTR.
What is the PREN threshold for seawater service?
As a general guideline: PREN above 40 is required for ambient-temperature seawater service; PREN above 50 for hot seawater above 35 degrees C or saline brine above 50,000 ppm chloride; PREN above 60 for concentrated hot brine at high temperatures. Super duplex 2507 has a PREN of approximately 42 — sufficient for ambient seawater but marginal for hot seawater. Inconel 625 has a PREN above 50 and Hastelloy C-276 above 65, making them the safe choices for any seawater temperature up to the alloy's maximum operating limit.
Selecting nickel alloy pipe for offshore oil and gas is one of the highest-stakes materials engineering decisions in the industry. The process requires characterizing the service environment with precision, understanding how each alloy family responds to the specific corrosive threats present, verifying compliance with the full matrix of applicable codes and standards, and procuring with documented traceability from mill to installation.
The six-step framework in this guide — environment characterization, PREN calculation, failure mode identification, alloy family matching, code compliance verification, and specification of pipe form and testing — provides a systematic path through a complex decision space. Applied consistently, it eliminates the most common selection errors and positions every project for long-term integrity and cost efficiency.
The tables, checklists, and decision matrices provided here are designed to be referenced throughout the procurement process — from initial feasibility studies through to final inspection and acceptance. Bookmark this guide. Share it with your procurement and quality teams. And when in doubt, consult a corrosion engineer before locking in a specification. The cost of expert advice is always lower than the cost of a failure.
Ready to Source? Our team specializes in nickel alloy and stainless steel pipe manufactured to ASTM B444 (Inconel 625), ASTM B622 (Hastelloy C-276), ASTM B725 (Alloy 825), and related standards, with full NACE MR0175 compliance, EN 10204 Type 3.1/3.2 certification, and third-party inspection support. Contact our sales team for datasheets, stock availability, and project-specific assistance. |
References and Applicable Standards
• ASTM B444 — Nickel-Chromium-Molybdenum-Columbium Alloy (UNS N06625) Seamless Pipe and Tube
• ASTM B622 — Seamless Pipe and Tube: Hastelloy C-276 (N10276), C-22 (N06022), B2 (N10665)
• ASTM B619 — Welded Nickel and Nickel-Cobalt Alloy Pipe
• ASTM B725 — Welded Nickel-Iron-Chromium Alloy Pipe (Alloy 825, Alloy 20)
• ASTM B163 — Seamless Nickel and Nickel Alloy Condenser and Heat-Exchanger Tubes
• ASME B31.3 — Process Piping
• ASME B36.19M — Stainless Steel Pipe (dimensions and schedules for nickel alloys)
• API 5CRA — Specification for Corrosion-Resistant Alloy Seamless Tubes for Use as Casing, Tubing, and Coupling Stock and Accessory Material for Wells in Corrosive Environments
• NACE MR0175 / ISO 15156 — Materials for Use in H2S-Containing Environments in Oil and Gas Production
• DNV-ST-F101 — Submarine Pipeline Systems
• ASME Section IX — Welding, Brazing, and Fusing Qualifications
• EN 10204 — Metallic Products — Types of Inspection Documents