Process gas volumes

Because of extremes in gas volume processed (turn-down ratio), the desige basis in (his case represents only half (be anticipated peak volume. A second distillation plant will be required. With membraues, however, additional membrane capecity at the from end can be added as needed withom additional equipment required in (he distillation section. Aanlyses of sevami associated ges forecasts indicate the exit ges from lhe first stage of membranes lo be remarkably stable in composition and flow rate. This flexibility is not shown in a single case economic comparison,"... 

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See also in sourсe #XX -- [ ]

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