MULTICOMPONENT BATCH DISTILLATION .2. COMPARISON OF ALTERNATIVE SLOP HANDLING AND OPERATING STRATEGIES

被引：23

作者：

QUINTEROMARMOL, E ^{[1
]}

LUYBEN, WL ^{[1
]}

机构：

[1] LEHIGH UNIV,CTR PROC MODELING & CONTROL,DEPT CHEM ENGN,MT TOP CAMPUS,BETHLEHEM,PA 18015

来源：

INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH | 1990年 / 29卷 / 09期

关键词：

D O I：

10.1021/ie00105a025

中图分类号：

TQ [化学工业];

学科分类号：

0817 ;

摘要：

In part 1, multicomponent batch distillation was analyzed when the operating strategy was recycle of all slop cuts to the next still pot charge. In this paper, several alternative schemes for handling slop cuts are explored. The results show 30-40% increases in capacity factor by segregating the slop cuts and performing binary batch distillations on each slop cut. © 1990, American Chemical Society. All rights reserved.

引用

页码：1915 / 1921

页数：7

共 9 条

[1]

*BERNOT C, 1989 AM I CHEM ENG A

[2] OPTIMAL DISTILLATE-RATE POLICY IN BATCH DISTILLATION [J].

CONVERSE, AO ;

GROSS, GD .

INDUSTRIAL & ENGINEERING CHEMISTRY FUNDAMENTALS, 1963, 2 (03) :217-&

[3] TIME-OPTIMAL PROBLEM IN BINARY BATCH DISTILLATION [J].

COWARD, I .

CHEMICAL ENGINEERING SCIENCE, 1967, 22 (04) :503-&

[4] PROFIT OF OPTIMUM CONTROL IN BATCH DISTILLATION [J].

KERKHOF, LHJ ;

VISSERS, HJM .

CHEMICAL ENGINEERING SCIENCE, 1978, 33 (07) :961-970

[5] MULTICOMPONENT BATCH DISTILLATION .1. TERNARY-SYSTEMS WITH SLOP RECYCLE [J].

LUYBEN, WL .

INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 1988, 27 (04) :642-647

[6] SOME PRACTICAL ASPECTS OF OPTIMAL BATCH DISTILLATION DESIGN [J].

LUYBEN, WL .

INDUSTRIAL & ENGINEERING CHEMISTRY PROCESS DESIGN AND DEVELOPMENT, 1971, 10 (01) :54-&

[7] OPTIMISATION OF BATCH DISTILLATION OPERATIONS [J].

ROBINSON, ER .

CHEMICAL ENGINEERING SCIENCE, 1969, 24 (11) :1661-&

[8] OPTIMAL CONTROL OF AN INDUSTRIAL BATCH DISTILLATION COLUMN [J].

ROBINSON, ER .

CHEMICAL ENGINEERING SCIENCE, 1970, 25 (06) :921-&

[9]

SUNDARAM S, 1989 AICHE ANN M SAN

← 1 →