
Originally Posted by
gasengineer+
Normally the extraction plants of LNG are attached to plants of fractionation, where are extracted the c3, c4, c5+, separately, in this way could obtain part of the flow of c3 for refrigeracion,if this is not truth, could add a tower depropanizer to the process, although i do not think that is very feasible, is preferable to have a plant fractionation complete.
Although i am just a student of engineering of gas, would be good the opinion of a professional with experience.
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