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Differential permeation, with point

Differential Permeation with Point Permeate Withdrawal... [Pg.173]

Figure 5.1 Differential permeation with point permeate withdrawal. Figure 5.1 Differential permeation with point permeate withdrawal.
By analogy with Section 5.6 of Chapter 5, for differential permeation with point permeate withdrawal, the equation to be integrated is... [Pg.232]

Table A5.1 Excel Spreadsheet Designators and Formulas for Differential Permeation with Point Permeate Withdrawal Calculations... Table A5.1 Excel Spreadsheet Designators and Formulas for Differential Permeation with Point Permeate Withdrawal Calculations...
In differential permeation, the point compositions of the phases are considered to vary linearly with position along the surface(s) of the membrane. A steady state is assumed, so that the compositions are independent of time. [Pg.173]

Of special consideration is the investigation of the cell as a continuum, first with point withdrawal of the permeate, then in both concurrent and countercurrent flow for the permeate and the reject phases. For this treatment, differential permeation is the mode of attack. The differential... [Pg.18]

Although there are a number of materials with the desired pore structure, for instance silicone rubbers, hydrocarbon rubbers, polyesters, polycarbonates and others, their use for industrial applications is limited to polysulfones and cellulose acetates. While the latt have been used with good success for dehydration, technical gas separation relies exclusively on polysulfones which can be used up to approximately 70 °C (their melting point is around 200 °C) and at pressures between IS and 140 bar. The lowest pressure differential between the feed gas side and the permeate gas side is 3 1 and this differential pressure determines the wall thickness of the membranes. Figure 2.8 shows the design of a membrane element developed by Monsanto Company, USA and marketed by the name of Prism separator. Each of these elements or modules contains thousands of hollow fibres packed to a density of approximately 1(X) per cm. ... [Pg.56]

Chapters 9 to 11 deal with the dynamic analysis of a single particle exposed to a constant bulk environment. The method of differential adsorption bed discussed in Chapter 11 is suitable for the application of the single particle analysis. A permeation method called the time lag method is useful for characterisation of diffusional flow, viscous flow and surface flow of pure gas through a single pellet (Chapter 12). The diffusion cell method either in steady state mode or transient mode is useful to characterize binary diffusional systems (Chapter 13). All these methods evolve around the analysis of a single particle and they complement each other in the characterization of diffusion and adsorption characteristics of a system. From the stand point of system set-up, the time lag and diffusion cell methods require a careful mounting of a particle or particles between two chambers and extreme care is exercised to avoid any gas by-passing the particle. [Pg.775]


See other pages where Differential permeation, with point is mentioned: [Pg.689]    [Pg.182]    [Pg.271]    [Pg.61]    [Pg.193]    [Pg.326]    [Pg.239]    [Pg.271]    [Pg.284]    [Pg.621]    [Pg.266]    [Pg.455]    [Pg.52]    [Pg.291]    [Pg.322]    [Pg.53]    [Pg.8]    [Pg.384]    [Pg.472]    [Pg.159]    [Pg.20]    [Pg.326]    [Pg.298]    [Pg.847]   


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Differential permeation

Differential permeation, with

Differential permeation, with permeate

Differential permeation, with point permeate withdrawal

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