Abstract
Separation of gases or vapors by barriers (both porous and nonporous membranes) results from the preferential permeation of the light component out of a gaseous mixture. Calculations of enrichment in a single stage were first presented by Weller and Steiner (1) for nonporous membranes. Also, similar calculations were reported by Naylor and Backer (2) for a porous membrane. However, these results can be applied interchangeably to porous and nonporous membranes if a proper separation factor is used. The mathematical forms of these two approaches appear to be entirely different. Therefore, the aim of the present paper is to show that Eq. (15) in Weller and Steiner's paper (1) reduces to Eq. (24) of Naylor and Backer's paper (2) when the pressure of the undiffused stream becomes zero. These equations permit one to calculate the concentration of the diffused stream when the concentration of the undiffused stream, the separation factor, and the “cut” are known quantities. Both equations are derived based on the nonmixing model.

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