ISSN : 0976-8505
Technological diagrams for obtaining high purity distillate have been examined. Base on the analysis, it has been suggested that to improve vapour mixture (distillate, condensate) or volatile mixture are as a result of boiling liquid carry –over in the vapour stream is possible. Expressions for finding add–mixture concentration in various number of distillers (Single to multiple distillers) as in the schemes and the ratio of the withdrawn product (from initial steam) has been determined. Analysis has been carried out for the derived and the optimal distribution of stream in a scheme. Base on the result, it has been fixed that the purity of a distillate reduces when the rate of product withdrawal increases
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