I'm working on a co2 recovery plant with MEA amine solvent. I want to know if having an intercooler in absorber can be practically effective for decreasing amine flow rate?
for example: there are a 69 m3/h rich amine flow at 77 C and 1.6 bar , also a sidestream of 10 m3/h from tray9 (absorber have 10 id tray)which cooled and recycled to some trays above.
Is this method common in amine plants or not? is there any specific reccomendations about this method?in which tray this cooled stream is better to feed? is it practically possible to feed it to feed tray with a temoperature below feed temperature?
According to Gas Purification book "A modification that has been used successfully to increase the acid gas loading of the rich amine (and thereby decrease the required solution flow rate) is the installation of a side cooler
(or intercooler) to reduce the temperature inside the absorber. The concept has proved particularly useful for DGA plants operating in Saudi Arabia where air cooling is used (Huval and van de Venne, 1981). The optimum location for a side cooler is reported to be the point where half the absorption occurs above and half below the cooler, which results in a location near the bottom of the column (Thompson and King, 1987)."
Thank you all
regards
Cruam
Edited by cruam, 02 May 2010 - 04:23 AM.

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