jvs3
Chemical
- Feb 13, 2003
- 4
I have a brine concentrator and am evaluating an increase in the chloride concentration by a change in operation. Specifically I am trying to quantify what increase in corrosion to expect.
The brine is brackish water with 2200 ppm chlorides at 100 degrees C.
Existing materials include titanium (which I'm not real concerned about), 316l welded with 317l filler, 316l welded with 316l filler and plain 316 welded with 316.
We have experienced SCC of the 316l stainless and pitting attack on the sub 317l filler welds.
I'm interested in the how the general corrosion rate of the different metals increases as I increase the chlorides to around 11,000 ppm. Using that information I'll determine the maximum acceptable chloride level versus corrosion rate and operate there.
Any online references would be preferred but any references at all appreciated.
The brine is brackish water with 2200 ppm chlorides at 100 degrees C.
Existing materials include titanium (which I'm not real concerned about), 316l welded with 317l filler, 316l welded with 316l filler and plain 316 welded with 316.
We have experienced SCC of the 316l stainless and pitting attack on the sub 317l filler welds.
I'm interested in the how the general corrosion rate of the different metals increases as I increase the chlorides to around 11,000 ppm. Using that information I'll determine the maximum acceptable chloride level versus corrosion rate and operate there.
Any online references would be preferred but any references at all appreciated.