YungPlantEng
Chemical
- Jan 19, 2022
- 84
This is a more general question since process info is variable. We utilize a spray nozzle of c276 with a cast CW2M low pluggage spray nozzle to quench a so2+n2 (0-3% o2) from 2300 F to 225 F). The quenchant is sulfurous water from a downstream unit laden with chlorides with a pH of 4-6 at 124 F.
At a very primitive level what materials are evaluated when HT corrosion, dew point corrosion, Chloride and sulfide stress cracking and pitting, weak sulphuric acid pitting, and HAZ dealloying are in play?
This question is probably silly but our site doesn't have SME experts and the OEM, corrosion lab, existing literature, and previous trials have all turned up dead ends.
At a very primitive level what materials are evaluated when HT corrosion, dew point corrosion, Chloride and sulfide stress cracking and pitting, weak sulphuric acid pitting, and HAZ dealloying are in play?
This question is probably silly but our site doesn't have SME experts and the OEM, corrosion lab, existing literature, and previous trials have all turned up dead ends.