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Gas permeation models, for perovskite

In Section 14.3 we concentrate our attention on the formulation of equations for modeling gas semipermeation within perovskite membranes for high-tem-perature CO2 capture applications. In such derivations, we assume that external diffusion at both the feed/membrane and permeate/membrane sides of the membrane (steps 1 and 2, respectively) can be neglected. In such a situation, bulk diffusion (step 3) and surface exchange kinetics (steps 2 and 4) are expected to contribute only to the permeation process. [Pg.314]


See other pages where Gas permeation models, for perovskite is mentioned: [Pg.315]    [Pg.315]    [Pg.317]    [Pg.319]    [Pg.321]    [Pg.325]    [Pg.327]    [Pg.315]    [Pg.315]    [Pg.317]    [Pg.319]    [Pg.321]    [Pg.325]    [Pg.327]    [Pg.107]    [Pg.129]    [Pg.314]    [Pg.329]    [Pg.51]   


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Gas permeation models, for perovskite membranes

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