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Interphase transfer, separation direction

IV. SEPARATION OF MIXTURES BY CHANGING THE DIRECTION OF INTERPHASE TRANSFER... [Pg.49]

Another example in which change in the interphase transfer direction is made use of is provided by separation processes based on the dependence of selectivity and sorbability of polyfunctional ion exchangers upon the solution pH [33]. [Pg.56]

Membrane operation is a specific, but not exotic, operation. In fact it is a hybrid of classical heat and mass transfer processes (Figure 4.1). Direct contact mass transfer operations tend to reach equilibrium due to a difference of chemical potential between two phases that are put into contact. In the same way, temperature equilibrium is aimed at during heat transfer operations, for which driving force is a temperature gradient. In contrast, for membrane operations, by using the specific properties of separation of the thin layer material that constitutes the membrane, under the particular driving force that is applied, it is possible to deviate from the equilibrium that prevails at fluid-to-fluid interphase with classical direct contact mass exchange systems and to reorientate the mass transfer properties. In particular, this is the case with classical operations such as microfiltration (MF), ultrafiltration (UF), reverse osmosis (RO), gas separation (GS), pervaporation (PV), dialysis (DI) or electrodialysis (ED), for which a few characteristics are recalled in Table 4.1. [Pg.258]


See other pages where Interphase transfer, separation direction is mentioned: [Pg.50]    [Pg.51]    [Pg.342]    [Pg.142]    [Pg.47]    [Pg.40]    [Pg.10]    [Pg.313]    [Pg.235]    [Pg.142]    [Pg.1057]    [Pg.5834]    [Pg.246]    [Pg.24]    [Pg.547]    [Pg.210]    [Pg.1057]   
See also in sourсe #XX -- [ Pg.49 , Pg.50 , Pg.51 , Pg.52 , Pg.53 , Pg.54 , Pg.55 , Pg.56 , Pg.57 , Pg.58 , Pg.59 ]




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