Minimum energy consumption in multicomponent distillation. 2. Three-product Petlyuk arrangements

被引:112
作者
Halvorsen, IJ [1 ]
Skogestad, S [1 ]
机构
[1] Norwegian Univ Sci & Technol, Dept Chem Engn, N-7491 Trondheim, Norway
关键词
D O I
10.1021/ie0108649
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
We show that the minimum energy requirement for separation of a multicomponent mixture in a three-product Petlyuk arrangement is equal to the minimum energy for the most difficult of the two separations (top/middle or middle/bottom product) in a conventional single column. In the V-min diagram (part 1 of this series), this is simply the highest peak. These results are based on an analytical solution for columns with an infinite number of stages, assuming constant relative volatilities and constant molar flows. The previous analytical results for the Petlyuk column are extended to include nonsharp separations, multicomponent feeds, and any feed quality.
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收藏
页码:605 / 615
页数:11
相关论文
共 19 条
[1]   Are thermally coupled distillation columns always thermodynamically more efficient for ternary distillations? [J].
Agrawal, R ;
Fidkowski, ZT .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 1998, 37 (08) :3444-3454
[2]   Rigorous comparative study of energy-integrated distillation schemes [J].
Annakou, O ;
Mizsey, P .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 1996, 35 (06) :1877-1885
[3]   TEMPERATURE HEAT DIAGRAMS FOR COMPLEX COLUMNS .2. UNDERWOODS METHOD FOR SIDE STRIPPERS AND ENRICHERS [J].
CARLBERG, NA ;
WESTERBERG, AW .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 1989, 28 (09) :1379-1386
[4]   TEMPERATURE HEAT DIAGRAMS FOR COMPLEX COLUMNS .3. UNDERWOODS METHOD FOR THE PETLYUK CONFIGURATION [J].
CARLBERG, NA ;
WESTERBERG, AW .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 1989, 28 (09) :1386-1397
[5]  
CHRISTIANSEN AC, 1997, AICHE ANN M LOS ANG
[6]  
CHRISTIANSEN AC, 1997, THESIS NORWEGIAN U S
[7]  
FIDKOWSKI Z, 1986, AICHE J, V32, P537, DOI 10.1002/aic.690320403
[8]   MINIMUM ENERGY-REQUIREMENTS OF THERMALLY COUPLED DISTILLATION SYSTEMS [J].
FIDKOWSKI, Z ;
KROLIKOWSKI, L .
AICHE JOURNAL, 1987, 33 (04) :643-653
[9]   NEW COMPLEX COLUMN ARRANGEMENTS FOR IDEAL DISTILLATION [J].
GLINOS, KN ;
NIKOLAIDES, IP ;
MALONE, MF .
INDUSTRIAL & ENGINEERING CHEMISTRY PROCESS DESIGN AND DEVELOPMENT, 1986, 25 (03) :694-699
[10]   Minimum energy consumption in multicomponent distillation.: 1.: Vmin diagram for a two-product column [J].
Halvorsen, IJ ;
Skogestad, S .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 2003, 42 (03) :596-604