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Metal working fluids flow rate

Next, a mathematical model that allows description of the separation and concentration of the components of a metallic mixture will be detailed the principal assumptions of the model are (1) convective mass transfer dominates diffusive mass transfer in the fluid flowing inside the HFs, (2) the resistance in the membrane dominates the overall mass transport resistance, therefore the overall mass transfer coefficient was set equal to the mass transfer coefficient across the membrane, and (3) chemical reactions between ionic species are sufficiently fast to ignore the contribution of the chemical reaction rates. Thus, the reacting species are present in equilibrium concentration at the interface everywhere [31,32,58,59]. For systems working under nonsteady state, it is also necessary to describe the change in the solute concentration with time both in the modules and in the reservoir tanks. The reservoir tanks will be modeled as ideal stirred tanks. [Pg.1025]


See other pages where Metal working fluids flow rate is mentioned: [Pg.506]    [Pg.1061]    [Pg.98]    [Pg.24]    [Pg.18]    [Pg.21]    [Pg.297]    [Pg.296]    [Pg.1090]    [Pg.1327]    [Pg.402]    [Pg.573]    [Pg.129]    [Pg.332]    [Pg.42]   
See also in sourсe #XX -- [ Pg.286 ]




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