julieangel
Petroleum
- Jul 31, 2013
- 8
Hi,
I need some guidance in this matter! I received a water analysis for a water injection line operating at 700 psi, 50C. I need to determine if the fluid is sour and if it is compatible with 316L. The water contains:
CO2 Gas Analysis 18.12(%)
H2S Gas Analysis 0.2211(%)
Total H2Saq @ Standard Pressure and Temperature (STP) 7.09 (mgH2S/l)
pH (STP) 5.82
Cl- 125,930.73 (mg/l)
When trying to calculate partial pressures of H2S I am getting confused with H2S gas percent and Total H2S aqueous. Which one should I take into account? Both? Which one will drive the corrosion process? Any feedback will highly appreciate it!
Thanks.
I need some guidance in this matter! I received a water analysis for a water injection line operating at 700 psi, 50C. I need to determine if the fluid is sour and if it is compatible with 316L. The water contains:
CO2 Gas Analysis 18.12(%)
H2S Gas Analysis 0.2211(%)
Total H2Saq @ Standard Pressure and Temperature (STP) 7.09 (mgH2S/l)
pH (STP) 5.82
Cl- 125,930.73 (mg/l)
When trying to calculate partial pressures of H2S I am getting confused with H2S gas percent and Total H2S aqueous. Which one should I take into account? Both? Which one will drive the corrosion process? Any feedback will highly appreciate it!
Thanks.