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Molecular distillation thermal efficiency

Distillation processes may be operated continuously or batchwise. The operating pressure may be low (10 Pa-100 Pa), medium (10 Pa-0.1 Pa) or even high vacuum (0.1 Pa-10 Pa) (molecular distillation) to avoid thermal damage to the mixture, or to increase efficiency. Special types of distillation are equilibrium or flash distillation (flash evaporation) and carrier distillation processes. [Pg.102]

The thermal efficiency of a molecular distillation is low. Fawcett (Ref. 2) has given a heat balance on a unit distilling triolein at 240 C. with the condenser at 25°C. The data are summarized in the following table ... [Pg.401]

The maj ority of these new plants are corn dry-grind ethanol plants. Approximately 2.5-2.7 gal of ethanol, 17.5 lb of dried distiller s grain (DDG), and 17 lb of carbon dioxide are produced from each bushel of corn processed through a corn dry mill (2). Since 1980, process improvements in enzymes, thermal-tolerant yeasts, molecular sieves, and cogeneration have achieved a 50% reduction in the energy required to produce ethanol from corn (2). Further improvements in efficiencies and reductions in production costs can be expected in the future. [Pg.1140]


See other pages where Molecular distillation thermal efficiency is mentioned: [Pg.327]    [Pg.128]    [Pg.131]    [Pg.2211]    [Pg.144]    [Pg.583]    [Pg.322]    [Pg.1186]    [Pg.59]    [Pg.62]   
See also in sourсe #XX -- [ Pg.401 ]




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