Dry gas desulfurization in catalytic cracking – Wet desulfurization
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I am simulating dry gas desulfurization in catalytic cracking, using MDEA to absorb hydrogen sulfide, but I don’t have enough data. I seek advice from those with experience in this area! Thank you!
Please send the relevant data over, and we’ll help you do the calculations
There are such examples in PROII, but they don’t converge very well
Have you used software to calculate whether the hydrocarbons in the solution at the bottom of the absorption tower are absorbed? I calculated that a considerable amount of hydrocarbons were absorbed at the bottom of the tower; does this not match the actual data? I would appreciate it if those in the know could tell me whether there are hydrocarbons at the bottom of the absorption tower and what their concentration is What is its proportion of total imported hydrocarbons?
Have you used software to calculate whether the hydrocarbons in the solution at the bottom of the absorption tower are absorbed? I calculated that a considerable amount of hydrocarbons were absorbed at the bottom of the tower; does this not match the actual data? I would appreciate it if those in the know could tell me whether there are hydrocarbons at the bottom of the absorption tower and what their concentration is What is its proportion of total imported hydrocarbons?