brimmer
Petroleum
- Mar 26, 2007
- 349
Dear experts,
Can anyone advise of a material resistant to HIC in a wet sour service environment? We have seen hydrogen blistering in the shell of a heat exchanger made of A-285-C and want to replace it with a better material. I would prefer a carbon steel to keep costs lower/materials consistent. Temperatures run to 350 degF and it is assumed the poison is from H2S. Operating design pressure of shell is 184 psig, heat exchanged rate 10.4 MBTU/HR. I was thinking of SA-516 70. Thanks in advance.
Can anyone advise of a material resistant to HIC in a wet sour service environment? We have seen hydrogen blistering in the shell of a heat exchanger made of A-285-C and want to replace it with a better material. I would prefer a carbon steel to keep costs lower/materials consistent. Temperatures run to 350 degF and it is assumed the poison is from H2S. Operating design pressure of shell is 184 psig, heat exchanged rate 10.4 MBTU/HR. I was thinking of SA-516 70. Thanks in advance.