AndreChE:
Marcelo Picciotti was one excellent advisor/consultant by the times we started up our plant, he used to work for Technipetrol.
The paper we wrote was about our experience, and actually it was publicized in the Oil and Gas Journal Magazine, maybe 1982/83's, not in the HP. I was confused due to the paper from Marcelo you've found. I remember it very well.
Our scrubber has two stacked stages in one scrubber/column.
We were cracking ethane, and due to different contaminants we experienced some foaming problems in the scrubber. This caused problems with the levels in the tower, obviously. Sometimes we needed to add a liquid antifoam, a dimethyl polisiloxane from Dow Corning. Later on, we changed, because the antifoam agent was difficult to use, and sometimes, dosing a little excess of the chemical, the results were opposite to what you expected! But I don't remember the supplier. If you have this problem, maybe you need to request the help from Coastal or Oakite, among others.
As the cracked gas from the scrubber feeds the last stage of the cracked gas compressor, we had some caustic carry over and damage in its laberinthyc seals, made in aluminum. We simply change them to stainless steel.
For removal of caustic the scrubber had a wire mesh in the top (outlet of cracked gas) sprayed with demin water, very low flow to avoid the dilution of the caustic (20% at the top).
We were lucky that the ethane we fed was very low in CO2 concentration, as the scrubber was undersized by our techonogist. Nowadays, I think that other methods are preferrable to caustic scrubbing.
It's all I can remember -not to much, maybe- I will revise my papers and, if I found something of interest, I will rewrite...
Good luck.
J. Alvarez