“…This conclusion also follows from Eqs. (19) and (25) in which the sep aration factor increases with increasing Q B /W ratio. Figure 7 presents experimental and calculated val ues of the separation factor for the case of germane cleaning of phosphine.…”
Section: Experimental Determination Of the Efficiency Of Gas Cleaningmentioning
confidence: 98%
“…In this case, a p = 1, b р = 0, and d р = 0 in Eq. (19) and we obtain from Eq. (26) that (27) where L in and L 1out (mol/s) are the flow rates of the mixture at the membrane module inlet and the outlet of the high pressure side, respectively.…”
Section: Mathematical Model Of Gas Cleaning Process In Radial Membranmentioning
confidence: 99%
“…It can be used both indepen dently and in combination with other separation methods. For example, Asahara and Taneda [19] described a scheme for producing helium containing less than 10 -3 vol % impurities, in which the processes of diffusion through a polymeric membrane and pres sure swing adsorption are combined. The production of hydrogen and helium with a total impurity concen tration less than 10 -2 vol % using the polymer mem branes alone was proposed in [20].…”
Physicochemical principles of membrane separation as applied to high purification of gases have been surveyed. The influence of impurity concentration in the feed gas and the membrane material on the separation factor and the role of sorption effects in the membrane material on the permeability and selectivity (separation factor) have been discussed. A mathematical model for the process of high gas purification in a radial membrane module has been developed. The efficiency of gas purification in the radial membrane mod ule has been experimentally determined. The effect of longitudinal mixing in the membrane module on the purification efficiency has been theoretically and experimentally studied. The processes of high gas purifica tion by membrane gas separation with recycle have been considered.
“…This conclusion also follows from Eqs. (19) and (25) in which the sep aration factor increases with increasing Q B /W ratio. Figure 7 presents experimental and calculated val ues of the separation factor for the case of germane cleaning of phosphine.…”
Section: Experimental Determination Of the Efficiency Of Gas Cleaningmentioning
confidence: 98%
“…In this case, a p = 1, b р = 0, and d р = 0 in Eq. (19) and we obtain from Eq. (26) that (27) where L in and L 1out (mol/s) are the flow rates of the mixture at the membrane module inlet and the outlet of the high pressure side, respectively.…”
Section: Mathematical Model Of Gas Cleaning Process In Radial Membranmentioning
confidence: 99%
“…It can be used both indepen dently and in combination with other separation methods. For example, Asahara and Taneda [19] described a scheme for producing helium containing less than 10 -3 vol % impurities, in which the processes of diffusion through a polymeric membrane and pres sure swing adsorption are combined. The production of hydrogen and helium with a total impurity concen tration less than 10 -2 vol % using the polymer mem branes alone was proposed in [20].…”
Physicochemical principles of membrane separation as applied to high purification of gases have been surveyed. The influence of impurity concentration in the feed gas and the membrane material on the separation factor and the role of sorption effects in the membrane material on the permeability and selectivity (separation factor) have been discussed. A mathematical model for the process of high gas purification in a radial membrane module has been developed. The efficiency of gas purification in the radial membrane mod ule has been experimentally determined. The effect of longitudinal mixing in the membrane module on the purification efficiency has been theoretically and experimentally studied. The processes of high gas purifica tion by membrane gas separation with recycle have been considered.
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