Summary
This paper presents an interactive M-file algorithm capable of running in a MATLAB environment, which
can estimate the number of theoretical plates a distillation column ought to contain at total reflux to
efficiently separate a multicomponent mixture into their individual components. Fenske’s model was used to
achieve the estimation at total reflux, and six feed variations for the multicomponent mixture of propane,
iso-butane, n-butane, iso-pentane and n-pentane were used as case studies. The first three feed variation
have iso-butane and n-butane as the light and heavy key respectively while the last three feed variation have
iso-pentane and n-pentane as the light and heavy key respectively. 2.324, 2.321, 2.321, 2.775, 2.718 and
2.691 average relative volatilities, condenser temperatures of 324K, 325K, 325K, 357K, 359K and 360K,
reboiler temperatures of 369K, 371K, 372K, 387K, 387K and 387K obtained for the six feed variations
respectively when applied in Fenske’s model, gave a minimum of 6.62, 6.66, 6.63, 6.57, 6.72 and 6.77 plates
as the number of theoretical plates required by the column for optimum separation of the components in
each feed variation. This method is simple, robust and saves time.
Index Terms
M-file Algorithm Fenske’s model Plates Feed variation Total refluxHow to cite this article
- Published: November 30, 2016
- Volume/Issue: Volume 1, Issue 2
- Pages: 1-12
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