Hi
I found this article in this site with some information that may be interesting for you.
http://www.cheresour...ckle-lines?pg=1I'm also involved in a job designing an HCl scrubber for removing the HCl discharged from safety valves in a Process Unit. The safety valves discharge to the scrubber and the scrubber overhead vapor discharges to the flare system.
The scrubbing media used is water with 6% NaOH and the fluid to be scrubbed is a HC with a MW of 36.6 at 111 ºC and 1,000 ppm of HCl. The operating pressure varies between 0.3 - 0.9 barg. The scrubber is a packed tower with Intalox saddles and is made of Carbon Steel.
I lack the experience designing this kind of equipment, in the sense that I do not know the typical efficiencies and the HETP that should be considered for this design nor the safety factor or key points to note in the datasheet.
I´m currently modeling the tower with ASPEN, using the electrolytic NRTL and radfrac block design models.
Furthermore, our client is requesting an internal coating of the scrubber to avoid internal corrosion. Does anyone have any experience with internal coating in a packed tower? it seems to me that this might not be a good approach.
Any advice would be of great help.
Kind regards,
Edited by Art Montemayor, 29 June 2012 - 07:39 AM.