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- W19709504 abstract "Distillative processes for natural gas sweetening appear to have advantages over more traditional treating methods in some applications. Commercial consideration is currently being given to distillative treating for gases containing large proportions of carbon dioxide and/or hydrogen sulfide. Fractionation, without the use of additives, has an application for the removal of bulk quantitities of these acid gases. While the production of high purity products is difficult and costly, bulk removal is relatively easy and cost effective. Bulk removal can serve to reduce the capital and operating costs of traditional sweetening processes so that combination processes often look advantageous. The application to enhanced oil recovery projects will take much individual study so that all of the economic factors are taken into consideration. For those projects where high purity CO/sub 2/ is required, extractive distillative processes will be very competitive with solvent processes; however, non-extractive distillation will probably not be competitive, especially when H/sub 2/S is a component in the feed. Bulk fractionation schemes have a definite application when high purity streams are not required. The simulation of distillative sweetening processes should not represent a problem to the engineer familiar with process flow sheet simulation in general. As with any engineering calculation, more » however, the results must be checked to be sure they are accurate. « less" @default.
- W19709504 created "2016-06-24" @default.
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- W19709504 date "1983-04-01" @default.
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- W19709504 title "Fundamentals of acid gas fractionation" @default.
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