Rapid assessment of thermally coupled side columns

被引:11
作者
Finn, AJ
机构
[1] Costain Oil, Gas and Process Limited, Costain House, Manchester, M22 5WN, Styal Road
来源
GAS SEPARATION & PURIFICATION | 1996年 / 10卷 / 03期
关键词
distillation; exergy; integration;
D O I
10.1016/0950-4214(96)00015-1
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
Thermally coupled distillation is well-proven in low temperature gas processing where energy is relatively expensive. Although the thermodynamic efficiency of thermally coupled columns is similar to conventional columns, thermal coupling reduces energy flows. This can lead to attractive savings in both energy and capital cost. This paper shows that the conventional Fenske-Underwood-Gilliland method for short cut distillation design is as appropriate for thermally coupled columns as it is for conventional distillation. This enables comparisons of conventional and thermally coupled columns to be made easily, and should help to make thermal coupling a more accepted means of improving energy efficiency in distillation systems. Copyright (C) 1996 Elsevier Science Ltd
引用
收藏
页码:169 / 175
页数:7
相关论文
共 18 条
[1]  
[Anonymous], 1980, THERMODYNAMICS 2 LAW
[2]  
FINN AJ, 1987, ICHEME S SER, V105
[3]   MINIMUM VAPOR FLOWS IN A DISTILLATION COLUMN WITH A SIDESTREAM STRIPPER [J].
GLINOS, K ;
MALONE, MF .
INDUSTRIAL & ENGINEERING CHEMISTRY PROCESS DESIGN AND DEVELOPMENT, 1985, 24 (04) :1087-1090
[4]  
GLINOS K, 1988, CHEM ENG RES DES, V66, P229
[5]  
GRUNBERG JF, 1956, P 4 CRYOG ENG C
[6]  
Henley EJ, 1981, EQUILIBRIUM STAGE SE
[7]  
King C. J., 1980, SEPARATION PROCESSES
[8]  
LESTAK F, 1994, GAS PROC ASS EUR CHA
[9]   HEAT INTEGRATION OF DISTILLATION-COLUMNS INTO OVERALL PROCESSES [J].
LINNHOFF, B ;
DUNFORD, H ;
SMITH, R .
CHEMICAL ENGINEERING SCIENCE, 1983, 38 (08) :1175-1188
[10]  
LINNHOFF B, 1983, CHEM ENG RES DES, V61, P207