Mechapower
Mechanical
- Oct 13, 2010
- 2
Dear All
I am having a question from my client whether i need to take consideration of galvanic corrosion between CS and Duplex.
Front channel(tubeside) of HExchanger is CS and tubesheet-tube & shell is 31803. Water is thorugh tubes & front channel and H2S gas is on shell.
There is a gasket between tubeside flange and tubesheet.
Should i consider the galvanic corrosion.
According to NACE CORROSION ENGINEER'S REFERENCE BOOK (3 edition) Galvanic cooriosn happens with two dissimilar materials with corrosive electrolyte.
In this case H2O is the electrolyte which has contact with both CS and duplex and H2O is not corrosive. The H2S doesnt contact CS.
If yes, what shall i can do to prevent it.
Please advice.
thanks
I am having a question from my client whether i need to take consideration of galvanic corrosion between CS and Duplex.
Front channel(tubeside) of HExchanger is CS and tubesheet-tube & shell is 31803. Water is thorugh tubes & front channel and H2S gas is on shell.
There is a gasket between tubeside flange and tubesheet.
Should i consider the galvanic corrosion.
According to NACE CORROSION ENGINEER'S REFERENCE BOOK (3 edition) Galvanic cooriosn happens with two dissimilar materials with corrosive electrolyte.
In this case H2O is the electrolyte which has contact with both CS and duplex and H2O is not corrosive. The H2S doesnt contact CS.
If yes, what shall i can do to prevent it.
Please advice.
thanks