4.6 Article

Minimum reflux calculation for multicomponent distillation in multi-feed, multi-product columns: Mathematical model

期刊

AICHE JOURNAL
卷 68, 期 12, 页码 -

出版社

WILEY
DOI: 10.1002/aic.17929

关键词

minimum reflux ratio; multicomponent distillation; multi-feed distillation column; multi-product distillation column; shortcut model

资金

  1. Office of Energy Efficiency and Renewable Energy (EERE), U.S. Department of Energy [DE-EE0005768]

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This article presents an accurate shortcut-based algorithmic method to determine the minimum reflux condition for multi-feed, multi-product distillation columns. Unlike existing techniques, this method does not involve rigorous tray-by-tray calculations or guessing of key components. The article includes a mathematical model, constraints, and an illustrative example to demonstrate the effectiveness of the approach.
Multi-feed, multi-product distillation columns are ubiquitous in multicomponent distillation systems. The minimum reflux ratio of a distillation column is directly related to its energy consumption and capital cost. Thus, it is a key parameter for distillation systems design, operation, and comparison. In this series, we present the first accurate shortcut based algorithmic method to determine the minimum reflux condition for any general multi-feed, multi-product (MFMP) distillation column separating any ideal multicomponent mixture. The classic McCabe-Thiele or Underwood method is a special case of this general approach. Compared with existing techniques, this method does not involve any rigorous tray-by-tray calculation, nor does it require guessing of key components. In this first part of the series, we present the mathematical model for a general MFMP column, derive constraints for feasible separation and minimum reflux condition, discuss their geometric interpretations, and present an illustrative example to demonstrate the effectiveness of our approach.

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