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Superheated solubility/phase

Calculation of the required condenser surface is not trivial. In contrast to the common applications where saturated vapors are condensed the permeate is a superheated vapor mixture. For design calculations the selection of appropriate heat-transfer coefficients has to consider the cooling to saturation conditions, the presence of noncondensable gases, and the partial condensation of the components along the respective dew lines. Total condensation of the more volatile components of the permeate vapor will often not be possible, but any losses of permeate vapor through the vacuum pump have to cope with the respective emission control regulations. An important factor is the solubility of the components of the permeate in the liquid phase. An additional condenser at the high-pressure side of the vacuum pump is a feasible option. [Pg.166]


See other pages where Superheated solubility/phase is mentioned: [Pg.394]    [Pg.48]    [Pg.156]    [Pg.176]    [Pg.181]    [Pg.51]    [Pg.1525]    [Pg.146]    [Pg.173]    [Pg.267]    [Pg.610]    [Pg.2243]    [Pg.905]    [Pg.426]    [Pg.1453]    [Pg.20]   
See also in sourсe #XX -- [ Pg.325 ]




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Superheating

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