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Feasible Ranges of Distillate Composition and Reflux Ratio

5 Feasible Ranges oe Distillate Composition and Bottoms Rate [Pg.230]

The following applications illustrate some of the factors considered in the validation of a column design using graphical representation. [Pg.231]

A distillation column is designed for separating methanol from a methanol-water mixture containing 60% mole methanol. The overhead methanol product must have a purity of 98% mole, and the methanol in the bottoms should not exceed a concentration of 4% mole. The column operating pressure is 100 kPa, with the feed entering the column at its bubble point. It is proposed to design the column at a reflux ratio of 1.0, or an /.,/ / ratio of 0.5. [Pg.231]

FIGURE 6,9 (a) Methanol dehydration, (h) Solving the methanol—water column on the H-X [Pg.232]

The next step in the column design is to decide on a column diameter that [Pg.232]


Feasible Ranges of Distillate Composition and Reflux Ratio... [Pg.178]




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Composition ranges

Distillation range

Distillation ratios

Distillation reflux ratio

Feasible

Feasible distillates

Reflux ratio

Reflux, distillation

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