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Membrane contactors correlation

Other potential uses for hollow fiber contactors include membrane distillation where microporous membranes form a barrier to liquid water but allow vapor to pass. Studies of these modules have been so far limited to laboratory scale investigations. Extensive reviews of the mass transfer correlations and applications for hollow fiber contactors are given in the literature. [Pg.1263]

Various parameters in Equation 31.17 have been defined earlier. Danesi et al. [92] described a simple correlation between permeability coefficient in FSSLM and HFSLM configuration. At very large values of ( ) (as compared to 1), Equation 31.17 is transformed into the one used for FSSLM by Danesi et al. [92]. Hence, the smaller the value of ( ), the higher will be the negative value of the left-hand side of Equation 31.17, which suggests the higher rate of mass transfer. Later on, D Elia et al. [93] considered the resistance in series model where they have studied the mass transport across hollow-fiber contactors in NDSX mode. They showed that the overall mass transfer resistance is equal to the sum of individual mass transfer resistances across the aqueous boundary layer and membrane phase. Mathematically, it can be written as follows ... [Pg.804]


See other pages where Membrane contactors correlation is mentioned: [Pg.1051]    [Pg.1053]    [Pg.1537]    [Pg.163]    [Pg.165]    [Pg.375]    [Pg.111]    [Pg.224]    [Pg.303]    [Pg.309]    [Pg.668]    [Pg.103]    [Pg.115]   
See also in sourсe #XX -- [ Pg.63 ]




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