NOTICE

Forums are temporarily disabled while we are working on a new login procedure.

When migrating the old forums over to our new forums we were unable to retain the identity of the authors, so the old posts will show up as "anonymous". All NEW posts will show up credited to their authors. So please participate and share knowledge just as you have in the past.

You must log in if you are an existing user or register if you are a new user in order to contribute to the discussions.

Discussion Forums - The Hendrix Group
HomeHomeDiscussionsDiscussionsMaterial Select...Material Select...Material for anhydrous HClMaterial for anhydrous HCl
Previous
 
Next
New Post
1/3/2006 9:00 AM
 
According to your experience, what material should be used for piping with anhydrous HCl? Process conditions are: Temp: -35 to 50 °C ( -31 to 122 F) Press: FullVacuum to 45 bar. Thank you! Phil
 
New Post
1/8/2006 9:00 AM
 
If it is really and perfectly anhydrous it is Non-Corrosive and MOC selection may not be a critical issue. But in practical cases due to moisture ingress or otherwise some aquous can interfere and in that case it will be significantly corrosive and you have to select suitable materials which often are a costlier one. For example you have to select Hastealloy B-2 or Alloy C- 276 of suitable design. regards and if you do have any further alternate inputs pl. revert. DM
 
New Post
1/10/2006 9:00 AM
 
>If it is really and perfectly anhydrous it is Non-Corrosive >and MOC selection may not be a critical issue. But in >practical cases due to moisture ingress or otherwise some >aquous can interfere and in that case it will be >significantly corrosive and you have to select suitable >materials which often are a costlier one. For example you >have to select Hastealloy B-2 or Alloy C- 276 of suitable >design. > >regards and if you do have any further alternate inputs pl. >revert. > >DM Thank you for your reply. I'm aware of the suitability of materials like Hastelloy but I'm also aware of their cost! As you correctly state, I think that it would be somehow impractical to assume that moisture will never enter the system, so corrosion risk can't be totally eliminated. According to several sources ordinary carbon steel would perform well, showing even more resistance to wet corrosion (HCl + water) than stainless steel. The problem might be low operating temperatures. Any experience on this problem? Would you consider using low-temp carbon steel? Phil
 
New Post
1/10/2006 9:00 AM
 
Dear Phil, You are very much correct. For Hydrogen Chloride Gas ( Wet) Carbon steel can be used but @ proper design of T, P and aq. regards DM
 
Previous
 
Next
HomeHomeDiscussionsDiscussionsMaterial Select...Material Select...Material for anhydrous HClMaterial for anhydrous HCl


  

News

With a little delay, our Calculation of Ammonium Salt Deposition Temperatures...read more
Our sulfidic corrosion calculators are now available at hghouston.com/calcula...read more

Stay Current

Sign up for our quarterly newsletter

covering updates on corrosion

Sign Up