metboss
Petroleum
- Sep 12, 2012
- 152
Hello,
Our application is water injection well and we need to select the material for Wellhead equipment (API 6A). Can we use 13Cr (AISI 410) material in sea water application? We proposed 13Cr material; but our client says that 13Cr cannot be used due to NACE restrictions and potential pitting corrosion. Is there any cut off limit for chloride concentration as per NACE?
As per my interpretation of NACE MR-0175 (Table A.18), it reads as ”any combination of temperature & chloride concertation” is acceptable and only restriction is found for H2S i.e. 1.5 psi max.
a) What is the maximum chloride concentration (ppm) is acceptable for 13Cr material? What is the maximum H2S (psi) is acceptable for 13Cr material?
b)Another substitution is AISI 4130 material; but, it seems to be more corrosive than 13Cr in sea water service. Also, from cost & application perspective, we will not be able to use Monel and Inco alloys & also, it requires more lead time for procurement. Is there any other material, we can use for sea water application?
c)In one of our well data details, H2S concentration is mentioned as 18%. How to calculate it in psi for liquid system? As per NACE, annex C (C.2), first of all bubble point to be calculated. How to determine the bubble point pressure of liquid if working pressure is 5000 psi?
Thanks
Our application is water injection well and we need to select the material for Wellhead equipment (API 6A). Can we use 13Cr (AISI 410) material in sea water application? We proposed 13Cr material; but our client says that 13Cr cannot be used due to NACE restrictions and potential pitting corrosion. Is there any cut off limit for chloride concentration as per NACE?
As per my interpretation of NACE MR-0175 (Table A.18), it reads as ”any combination of temperature & chloride concertation” is acceptable and only restriction is found for H2S i.e. 1.5 psi max.
a) What is the maximum chloride concentration (ppm) is acceptable for 13Cr material? What is the maximum H2S (psi) is acceptable for 13Cr material?
b)Another substitution is AISI 4130 material; but, it seems to be more corrosive than 13Cr in sea water service. Also, from cost & application perspective, we will not be able to use Monel and Inco alloys & also, it requires more lead time for procurement. Is there any other material, we can use for sea water application?
c)In one of our well data details, H2S concentration is mentioned as 18%. How to calculate it in psi for liquid system? As per NACE, annex C (C.2), first of all bubble point to be calculated. How to determine the bubble point pressure of liquid if working pressure is 5000 psi?
Thanks