Dear Mr. Ankur,
I write you from Ecuador (South America), I am member of Cheresources few time ago, I have read your work in this site. Days ago I see in your Topics the following question:
Posted 12 May 2014 - 03:10 AM
Does anyone have experience of using austenitic stainless steel "254" as a corrosion-resistant alloy specifically in environments susceptible to chloride stress corrosion cracking and hydrochloric acid acid-corrosion.
Would like to hear some opinion on this from members familiar with this material.
Regards,
Ankur.
If you need the information for design the overhead crude tower, my recommendation is:
You need to know the amount of salts (ptb) in your system, the recommendation is less 2 ptb. If you have over this value, you need to work firstly about the crude desalting after this the metallurgical choice is more easy.
About the austenitic stainless steel “254” I have read in the web, this can replace titanium or hastelloy!!!, but I don´t work with this alloy in our Refinery (3000 bpd). I attached you information about “254”.
http://www.langleyalloys.com/ALLOY254.php
http://www.nyk.co.jp/en/products/alloys/corrosion/254n.html
I hope the information will be useful for you.
Regards,
César Terán
Quito-Ecuador