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Pressure gradient in SFC

For calculation of the pressure drop the relation after Darcy can be used, in which the constant Iir is fitted to experimentally determined pressure drops. [Pg.306]

The viscosity p and the superficial velocity w are dependent on pressure and density, respectively. Therefore, a new density has to be calculated for each pressure by means of an equation of state, e.g. for CO2 by the equation of Span and Wagner [60]  [Pg.306]

For calculation of the viscosity an approach of Chung can be used, the influence of pressure is taken into account by the method of Reichenberg [61]. The viscosity of a gas at low pressure and a temperature T Tc can be calculated after Chung by  [Pg.306]

Starting from the viscosity at low pressure, the influence of pressure can be calculated after Reichenberg by  [Pg.307]

Via the continuity equation, velocity and density are linked to each other  [Pg.307]


The density and therefore the solvating power of supercritical fluids varies according to the pressures to which they are submitted. As a consequence, a pressure gradient in SFC is equivalent to an elution gradient in HPLC, or a temperature gradient in GC. [Pg.129]

I 9 Modeling of Simulated Moving-bed Chromatography 9.4.2.6 Modeling of Pressure Gradient in SFC... [Pg.306]


See other pages where Pressure gradient in SFC is mentioned: [Pg.210]    [Pg.96]   
See also in sourсe #XX -- [ Pg.306 ]




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