Direct answer: In an H2S or CO2 environment the question is not “how strong is the coupling?” but “will this material resist cracking and corrosion in this chemistry?” H2S can cause sulphide stress cracking (SSC) in hard, high-strength steels, while CO2 drives sweet corrosion whose rate depends on partial pressure, temperature and free water. The governing framework is ISO 15156 / NACE MR0175, which sets environmental limits and material requirements, including a hardness ceiling for low-alloy steels. Evaluating compatibility means matching the material to the measured partial pressures and hardness limits, then proving it with documentation. A higher grade is not automatically more suitable; in sour service it is often less suitable.
H2S introduces hydrogen into the steel, and in a susceptible material under stress that hydrogen can initiate cracking. The resistance depends on chemistry, microstructure and — critically — hardness: harder steels crack more readily, which is why sour-service grades are hardness-controlled. CO2, by contrast, causes electrochemical sweet corrosion that thins the metal and can undermine the connection; its severity rises with partial pressure, temperature and the presence of free water. The two gases can occur together, and then the material must satisfy both the cracking resistance of the H2S requirement and the corrosion resistance of the CO2 requirement.
ISO 15156 (published in the US as NACE MR0175) defines how materials may be used in H2S-containing oil and gas production. For carbon and low-alloy steels it sets a maximum hardness — commonly cited as 22 HRC — and constrains the environment by partial pressure of H2S, pH, temperature and chloride content. Importantly, compliance is environmental: a material “acceptable” under the standard is acceptable only within the limits stated for that material. Beyond those limits, a more resistant alloy or a different grade is required. This is why the standard should be applied to the actual well condition, not quoted as a blanket approval.
| Material type | H2S (sour) suitability | CO2 / corrosion note |
|---|---|---|
| Plain carbon grades (e.g. J55, N80, P110) | Generally limited; hardness must be controlled | Corrode readily; often need inhibition or coating |
| Hardness-controlled low-alloy (e.g. L80 type 1) | Suitable within ISO 15156 limits | Moderate corrosion resistance |
| Modified / higher-Cr (e.g. L80 9Cr, 13Cr) | Improved resistance | Better CO2 resistance; check limits |
| CRA / stainless (13Cr, duplex) | Depends on grade and environment | Strong CO2 resistance; careful make-up (galling-prone) |
The values above are orientation only. The definitive limits for any grade come from the current editions of ISO 15156 / NACE MR0175 and from the mill's material certificate; they must be checked against your measured partial pressures and temperature. For reference, our catalogue lists couplings offered for sour gas service, such as an API 5B 7 5/8 in BTC M65 casing coupling (NACE MR0175) and an API 8 5/8 in LTC L80 casing coupling (NACE MR0175). These listings describe the intended service; the material records for your order are what confirm it.
For buyers, the value of an oilfield couplings supplier in sour service lies less in the catalogue description than in the completeness of the material documentation that accompanies each batch. A listing that names a grade is a starting point; a hardness reading, a heat number and a traceable material certificate are what turn that name into a verified material. On corrosive wells it is worth treating the documentation as part of the product, because the documentation is what proves the product will behave as the standard requires.
For carbon and low-alloy oilfield couplings in sour service, hardness is the single most decisive property, because hardness correlates directly with susceptibility to sulphide stress cracking. A grade that looks ideal on strength can be disqualified by a single hardness reading above the permitted limit. That is why a sour-service order should always be accompanied by a measured hardness result for the batch, tied to the limit in ISO 15156 / NACE MR0175, and why a claim of sour suitability without hardness data is incomplete.
It does not approve a specific product. It defines the conditions under which a material may be used. A coupling complies only when its material meets the requirements and the service condition falls within the standard's stated limits for that material.
Usually not. Higher strength brings higher hardness, which increases SSC susceptibility. Hardness-controlled grades are chosen precisely because strength is not the deciding factor in sour service.
The H2S and CO2 partial pressures, the temperature, the chloride level and the pH. Without those numbers, no material can be properly assessed against ISO 15156.
Coatings and inhibitors can reduce corrosion, but they are not a substitute for correct material selection in a highly corrosive environment. Where corrosion is severe, the material itself should carry the resistance.
Assemble the well chemistry first, then select the lowest-cost material that satisfies the H2S and CO2 requirements under ISO 15156 / NACE MR0175, and insist on hardness data and material records for the batch. A complete range of oilfield couplings is shown on the Oilfield Couplings category page; send us your partial pressures and temperature and we will align the grade and documentation to the environment rather than to a generic label.
Direct answer: In an H2S or CO2 environment the question is not “how strong is the coupling?” but “will this material resist cracking and corrosion in this chemistry?” H2S can cause sulphide stress cracking (SSC) in hard, high-strength steels, while CO2 drives sweet corrosion whose rate depends on partial pressure, temperature and free water. The governing framework is ISO 15156 / NACE MR0175, which sets environmental limits and material requirements, including a hardness ceiling for low-alloy steels. Evaluating compatibility means matching the material to the measured partial pressures and hardness limits, then proving it with documentation. A higher grade is not automatically more suitable; in sour service it is often less suitable.
H2S introduces hydrogen into the steel, and in a susceptible material under stress that hydrogen can initiate cracking. The resistance depends on chemistry, microstructure and — critically — hardness: harder steels crack more readily, which is why sour-service grades are hardness-controlled. CO2, by contrast, causes electrochemical sweet corrosion that thins the metal and can undermine the connection; its severity rises with partial pressure, temperature and the presence of free water. The two gases can occur together, and then the material must satisfy both the cracking resistance of the H2S requirement and the corrosion resistance of the CO2 requirement.
ISO 15156 (published in the US as NACE MR0175) defines how materials may be used in H2S-containing oil and gas production. For carbon and low-alloy steels it sets a maximum hardness — commonly cited as 22 HRC — and constrains the environment by partial pressure of H2S, pH, temperature and chloride content. Importantly, compliance is environmental: a material “acceptable” under the standard is acceptable only within the limits stated for that material. Beyond those limits, a more resistant alloy or a different grade is required. This is why the standard should be applied to the actual well condition, not quoted as a blanket approval.
| Material type | H2S (sour) suitability | CO2 / corrosion note |
|---|---|---|
| Plain carbon grades (e.g. J55, N80, P110) | Generally limited; hardness must be controlled | Corrode readily; often need inhibition or coating |
| Hardness-controlled low-alloy (e.g. L80 type 1) | Suitable within ISO 15156 limits | Moderate corrosion resistance |
| Modified / higher-Cr (e.g. L80 9Cr, 13Cr) | Improved resistance | Better CO2 resistance; check limits |
| CRA / stainless (13Cr, duplex) | Depends on grade and environment | Strong CO2 resistance; careful make-up (galling-prone) |
The values above are orientation only. The definitive limits for any grade come from the current editions of ISO 15156 / NACE MR0175 and from the mill's material certificate; they must be checked against your measured partial pressures and temperature. For reference, our catalogue lists couplings offered for sour gas service, such as an API 5B 7 5/8 in BTC M65 casing coupling (NACE MR0175) and an API 8 5/8 in LTC L80 casing coupling (NACE MR0175). These listings describe the intended service; the material records for your order are what confirm it.
For buyers, the value of an oilfield couplings supplier in sour service lies less in the catalogue description than in the completeness of the material documentation that accompanies each batch. A listing that names a grade is a starting point; a hardness reading, a heat number and a traceable material certificate are what turn that name into a verified material. On corrosive wells it is worth treating the documentation as part of the product, because the documentation is what proves the product will behave as the standard requires.
For carbon and low-alloy oilfield couplings in sour service, hardness is the single most decisive property, because hardness correlates directly with susceptibility to sulphide stress cracking. A grade that looks ideal on strength can be disqualified by a single hardness reading above the permitted limit. That is why a sour-service order should always be accompanied by a measured hardness result for the batch, tied to the limit in ISO 15156 / NACE MR0175, and why a claim of sour suitability without hardness data is incomplete.
It does not approve a specific product. It defines the conditions under which a material may be used. A coupling complies only when its material meets the requirements and the service condition falls within the standard's stated limits for that material.
Usually not. Higher strength brings higher hardness, which increases SSC susceptibility. Hardness-controlled grades are chosen precisely because strength is not the deciding factor in sour service.
The H2S and CO2 partial pressures, the temperature, the chloride level and the pH. Without those numbers, no material can be properly assessed against ISO 15156.
Coatings and inhibitors can reduce corrosion, but they are not a substitute for correct material selection in a highly corrosive environment. Where corrosion is severe, the material itself should carry the resistance.
Assemble the well chemistry first, then select the lowest-cost material that satisfies the H2S and CO2 requirements under ISO 15156 / NACE MR0175, and insist on hardness data and material records for the batch. A complete range of oilfield couplings is shown on the Oilfield Couplings category page; send us your partial pressures and temperature and we will align the grade and documentation to the environment rather than to a generic label.