I want to fist say that the information that is being dispersed on this forum is excellent. Let's keep it up!
I want to know if there is an issue that is associated with fluctuation of feed gas inlet to the absorber of a bulk H2S / CO2 removal unit using MDEA?
I think that with this fluctuation in feed temperature it will create a problem with the lean amine temperature to ensure the 5 degC delta is achieved. This delta is meant to prevent condensation of hydrocarbon...
Any thoughts anyone?
Edited by GasPro, 15 August 2010 - 08:10 AM.