Corroneer
Mechanical
- Jan 13, 2006
- 63
Hi Everyone,
We are designing a new gas vessel (it will separate liquids from the gas).
The partial pressure of H2S is > 100 KPa.
We do not have proper pH values, but the optimum working pH for the vessel is between 6 and 7. The operator confirmed that the pH can go lower than this (again no clear pH values given).
The temperature is between 200 to 300 F.
The current vessel had suffered severe cracking, but minor corrosion pitting.
We have selected a cladded CS for this because of the very high probability of SSC cracking and HIC (both were experienced in the old vessel), but the owner argues that if the equipment is manufactured from HIC resistant CS that is qualified for NACE MR0175, no cracking (neither SSC nor HIC) is expected.
Unfortunately, NACE MR0175 is unclear about the limits and the applicability/inapplicability of CS.
I am still not convinced that CS will withstand this as the equipment will be exposed to severe environment (high H2S, water content, temperature) during operation (dehydration units upstream are inefficient and gas with significant water content can reach this vessel during operation).
Any help is welcome!
Regards,
Corroneer
We are designing a new gas vessel (it will separate liquids from the gas).
The partial pressure of H2S is > 100 KPa.
We do not have proper pH values, but the optimum working pH for the vessel is between 6 and 7. The operator confirmed that the pH can go lower than this (again no clear pH values given).
The temperature is between 200 to 300 F.
The current vessel had suffered severe cracking, but minor corrosion pitting.
We have selected a cladded CS for this because of the very high probability of SSC cracking and HIC (both were experienced in the old vessel), but the owner argues that if the equipment is manufactured from HIC resistant CS that is qualified for NACE MR0175, no cracking (neither SSC nor HIC) is expected.
Unfortunately, NACE MR0175 is unclear about the limits and the applicability/inapplicability of CS.
I am still not convinced that CS will withstand this as the equipment will be exposed to severe environment (high H2S, water content, temperature) during operation (dehydration units upstream are inefficient and gas with significant water content can reach this vessel during operation).
Any help is welcome!
Regards,
Corroneer