THE CONSTANT HEAT-TRANSPORT MODEL AND DESIGN OF DISTILLATION-COLUMNS WITH ONE SINGLE DISTRIBUTING COMPONENT

被引:8
作者
REV, E
机构
[1] Department of Chemical Engineering, University of Technical Sciences, Budapest
关键词
D O I
10.1021/ie00105a028
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
The model approximation of constant molar overflow (CMO) is relaxed to constant heat transport (CHT) along distillation column sections assuming ideal mixtures with constant relative volatilities and constant molar latent heats. A formal analogy can be perfectly derived between CMO and CHT models in the sense that all the formulas and numerical and graphical procedures adequate for use with the CMO model remain valid under the CHT model after simple transformation of the variables. A model of only one distributing component or nondistributing key components is developed. Analytical formulas are derived to calculate the limiting flow rates of such columns. The limiting flow rates of Petlyuk systems are also determined in this way. © 1990, American Chemical Society. All rights reserved.
引用
收藏
页码:1935 / 1943
页数:9
相关论文
共 9 条
[1]  
FIDKOWSKI Z, 1986, AICHE J, V32, P537, DOI 10.1002/aic.690320403
[2]   MINIMUM ENERGY-REQUIREMENTS OF THERMALLY COUPLED DISTILLATION SYSTEMS [J].
FIDKOWSKI, Z ;
KROLIKOWSKI, L .
AICHE JOURNAL, 1987, 33 (04) :643-653
[3]  
KING CJ, 1980, MCGRAW HILL CHEM ENG, P309
[4]   DESIGN AND SYNTHESIS OF HOMOGENEOUS AZEOTROPIC DISTILLATIONS .2. MINIMUM REFLUX CALCULATIONS FOR NONIDEAL AND AZEOTROPIC COLUMNS [J].
LEVY, SG ;
VANDONGEN, DB ;
DOHERTY, MF .
INDUSTRIAL & ENGINEERING CHEMISTRY FUNDAMENTALS, 1985, 24 (04) :463-474
[5]   CALCULATION OF MINIMUM REFLUX IN DISTILLATION COLUMNS [J].
SHIRAS, RN ;
HANSON, DN ;
GIBSON, CH .
INDUSTRIAL AND ENGINEERING CHEMISTRY, 1950, 42 (05) :871-876
[6]  
Underwood A. J. V., 1945, J I PETROL, V31, P111
[7]  
UNDERWOOD AJV, 1946, J I PET, V32, P598
[8]  
Underwood AJV., 1946, J I PETROL, V32, P614
[9]  
WHTIE RR, 1953, PET PROCESS, V8, P539