JustAnotherChemE
Chemical
- Jun 21, 2007
- 11
Hi, I'm trying to decide if my company needs to step up to 316 grade stainless from 304 for our future direct gas fired heating system.
The system will be operating at 170-190 deg F with city water that has a variable 100-150 ppm chloride content (lake/stream versus well water seasonally)
I understand that 304 would be stable with this chloride count below 140 deg F, but some tank manufacturers have been warning us that we'll need to use 316 to avoid nasty things like stress corrosion cracking etc.
I'm mostly concerned about the 20,000 gallon storage tank we'll be using to store waste heat from other process equipment... during the day the water will be fairly stagnant which will affect the corrosion kinetics / diffusion, correct?
Any help would be appreciated. I'm the only engineer here so it's fallen upon me to nitpick details like this plus I'm fairly ignorant when it comes to corrosion, but I'm picking it up!
Thanks.
The system will be operating at 170-190 deg F with city water that has a variable 100-150 ppm chloride content (lake/stream versus well water seasonally)
I understand that 304 would be stable with this chloride count below 140 deg F, but some tank manufacturers have been warning us that we'll need to use 316 to avoid nasty things like stress corrosion cracking etc.
I'm mostly concerned about the 20,000 gallon storage tank we'll be using to store waste heat from other process equipment... during the day the water will be fairly stagnant which will affect the corrosion kinetics / diffusion, correct?
Any help would be appreciated. I'm the only engineer here so it's fallen upon me to nitpick details like this plus I'm fairly ignorant when it comes to corrosion, but I'm picking it up!
Thanks.