Pipe material selection for chemical, marine and high-temperature service comes down to one question: what specific way will this service attack or stress the pipe, and which material actually resists that mechanism? It is not a matter of picking the “best” material in general terms, since the alloy that performs brilliantly against one failure mode can fail quickly against another. This article helps you make the decision, not an inventory of all the materials for pipes that exist in the world. What it provides is a decision-making process: find the corrosion mechanism or failure mechanism that predominates in your application and then select the class of material that is resistant to it. For the chemistry and mechanical properties of each material mentioned, we refer you to the product pages instead.
An assessment of corrosion in a piping system should be based on the specific mechanism of corrosion and not just on the term corrosion resistant. Uniform corrosion may be treated with corrosion allowance and occurs with a relatively uniform loss of wall thickness, whereas pitting results in localized severe corrosion, especially in chloride-rich areas. Crevice corrosion occurs in confined spaces, e.g., under gasket deposits; chloride stress corrosion cracking (SCC) can cause cracking in stressed austenitic stainless steels in hot chlorides. Sour service is when the hydrogen sulfide (H₂S) content is present and is subjected to the applicable NACE MR0175/ISO 15156 requirements. Galvanic corrosion takes place when two different metals are electrically joined to an electrolyte. These mechanisms are useful to identify appropriate materials for various piping services.
Under ASME B31.3, as the temperature increases, the allowable thickness decreases as well, meaning that a wall thickness sufficient to withstand a specific pressure at room temperature is not necessarily adequate at a higher temperature, even with the same material. That’s why temperature is never secondary in material selection; it affects the pressure capacity of the selected material. Our pipe thickness chart post discusses the ASME B31.3 formula and how allowable stress is part of the wall thickness calculation, and our pipe schedule post addresses how a pipe’s schedule relates to its pressure at a given size.
The weldability of materials is greatly different between families and in some cases, especially when the section thickness is large and the material is a particular alloy steel, post-weld heat treatment (PWHT) must be performed to reduce the residual stress and restore the mechanical properties following welding. Failure to perform a required PWHT step is not obvious right away; it becomes apparent when reduced toughness or unexpected cracking occurs in the line after it is placed in service; that is why it is better to specify the PWHT requirement as part of the material decision, rather than leaving it to the fabricator to figure out later. If solids are in the flow, then fatigue and abrasion resistance is also included in the material selection, because a material that might be appropriate for corrosion resistance may not necessarily be appropriate for abrasive service conditions. In our seamless vs welded steel pipe post, we will be looking at how the quality of the weld joints is a factor in the pressure design calculation.
Process piping is generally designed according to ASME B31.3. We have ASTM A312, A269 and A213 differences post covers for each material family, including stainless steel pipe, duplex, Inconel, and others, and follow the ASTM standards of each of the material families. NACE MR0175/ISO 15156 is an additional layer of material and hardness qualification requirements above and beyond the base material standard when hydrogen sulfide is present.
The lowest cost material at time of purchase is not the lowest cost material over the system’s life. It can be much less expensive to specify a lower cost material with a higher corrosion allowance, inspection more often, or a more realistic service life than it is to specify a higher alloy material correctly the first time. The true comparison is the lifecycle cost, not the price of the product.
Chemical Service Scenario | Dominant Mechanism | Material Shortlist |
General acid or alkali attack, moderate conditions | Uniform corrosion | Stainless steel 316/316L |
Strong or highly aggressive chemicals | Severe uniform attack, possible localized attack | Hastelloy, titanium |
Oxidizing acids and media | Oxidizing-environment attack | Titanium and certain stainless grades, verify against a compatibility chart |
Reducing acids and media | Reducing-environment attack | Nickel-molybdenum alloys such as Hastelloy B-type grades, verify against a compatibility chart |
Chloride-bearing chemical streams | Pitting, crevice corrosion, chloride SCC | Duplex or super duplex stainless steel, or 904L depending on severity |
Sour service (H2S present) | Sulfide stress cracking | Material qualified under NACE MR0175/ISO 15156 |
Pipe Material Selection Decision Table
Once you have identified the dominant mechanism your service will create, whether that is a corrosion mode, sour service, or a temperature-driven failure mode, this table gives a starting shortlist to work from.This is a starting shortlist for narrowing options, not a substitute for a full engineering material selection, compatibility check and standards review.
Failure mechanism or service condition | Material shortlist |
General corrosion, moderate chemical exposure | Stainless steel 316/316L |
Strong or highly aggressive chemicals | Hastelloy, titanium |
Chloride-bearing chemical or marine service, pitting/crevice risk | Duplex, super duplex stainless steel, 904L |
Sour service (H2S) | Material qualified under NACE MR0175/ISO 15156 |
Splash zone or subsea marine exposure | Super duplex, copper-nickel, Monel |
Moderate high temperature (creep not yet governing) | Carbon steel, standard alloy steel |
High temperature with creep as a governing factor | Chrome-moly alloy steel (P11, P22, P91-type) |
Severe high temperature, oxidizing or scaling conditions | Inconel and other nickel alloys |
Common Pipe Material Selection Mistakes to Avoid
The reasoning in this article narrows down a material family; turning that into an accurate quotation still depends on giving us the full service picture, not just a grade name. Send the following with any enquiry, so we can help confirm the right material quickly:
Optimal pipe material selection requires starting from the failure mechanism driven by your process environment—whether that is chloride pitting in seawater, creep deformation at elevated steam temperatures, or acid attack in chemical processing lines. Balancing mechanical properties, environmental resistance, and total lifecycle costs ensures long-term operational integrity and prevents costly unscheduled plant shutdowns. Whether you are specifying materials for a new EPC project or re-evaluating a severe-service piping loop, our technical specialists at Stellar Alloys Steel Pipes and Tubes are here to help. Request a quote or contact our metallurgy team today to discuss your project specifications.
Choose a material based on the service conditions, dominant corrosion mechanism, temperature, pressure, and applicable codes and standards.
Super duplex, copper-nickel, and Monel are commonly used for demanding seawater service, while 316L may suit less severe conditions.
The choice depends on temperature and service conditions. Alloy steel, chrome-moly steels, and nickel alloys are commonly used as temperature severity increases.
Yes, carbon steel can be used for mild chemical service with suitable corrosion allowance, but aggressive or highly corrosive chemicals may require stainless steel or higher-alloy materials.
NACE MR0175/ISO 15156 specifies material and hardness requirements for equipment used in sour service containing hydrogen sulfide (H₂S).
Duplex stainless steel generally provides higher strength and better chloride SCC resistance than standard austenitic stainless steel, making it suitable for demanding marine service.
Inconel is commonly selected for high-temperature and oxidizing conditions, while Hastelloy is often used for highly aggressive chemical and reducing environments.
Material selection often has a greater cost impact than changing the pipe schedule within the same material family.
