Minimum entrainer flows for extractive distillation: A bifurcation theoretic approach

Journal Article · Tue Feb 01 04:00:00 UTC 1994 · AIChE Journal (American Institute of Chemical Engineers); (United States)

DOI:https://doi.org/10.1002/aic.690400206· OSTI ID:7306061

Knapp, J P; Doherty, M F ^[1]

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1. Univ. of Massachusetts, Amherst, MA (United States). Dept. of Chemical Engineering

In addition to a minimum reflux, every extractive distillation exhibits a maximum reflux, above which the desired separation is impossible, and a minimum entrainer flow rate, below which the separation is also impossible. Both of these quantities correspond to bifurcations of the finite difference equations describing the middle section of the column and, given a VLE model, can be easily calculated knowing only information about the column feed and the desired product compositions, that is, prior to any column design calculations. Both maximum reflux and minimum entrainer flows have important implications for the design and operation of extractive distillations. By limiting the range of feasible operating reflux ratios, the maximum reflux affects the flexibility, operability and controllability of the column. Ranking a set of feasible extractive entrainers according to their minimum entrainer flows provides a simple effective method for identifying the most promising candidates. Near optimal design values of the entrainer flow can then be estimated using the heuristic presented.

• OSTI ID: 7306061
• Journal Information: AIChE Journal (American Institute of Chemical Engineers); (United States), Journal Name: AIChE Journal (American Institute of Chemical Engineers); (United States) Vol. 40:2; ISSN AICEAC; ISSN 0001-1541
• Country of Publication: United States
• Language: English

Related Subjects

02 PETROLEUM
020400* -- Petroleum-- Processing
CONTROL
DISTILLATION EQUIPMENT
ENTRAINMENT
EQUIPMENT
FLOW MODELS
FLUID MECHANICS
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MECHANICS
PROCESS CONTROL