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AMSIM for calculating liquefied gas and dry gas desulfurization problems

2016-03-27View Original

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1 Is AMSIM a reliable tool for calculating dry gas desulfurization in liquefied gas? Does it belong to the electrolyte system? Why aren’t ions displayed among the defined components? How to display ions? Products containing sulfur and products containing hydrogen sulfide are not the same thing, right? 2 How does one convert the units in calculations to the unit system of mass flow rate? In other words, how many t/h of MDEA is required to process a certain amount of liquefied gas per t/h? 3 After setting the operating conditions for feeding and the tower, is there anything else that needs to be set? I seek guidance from the experts in amine removal~~ Extremely grateful~
Reply #22016-03-30
Generally, the H2S loading in rich amine solutions is 0.3 kmol H2S/kmol MDEA

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