A geometric design method for side-stream distillation columns

Industrial and Engineering Chemistry Research

Volumn 35, Issue 10, 1996, Pages 3653-3664

  Rooks, Raymond E ^a   Malone, Michael F ^a   Doherty, Michael F ^a  

^a University of Massachusetts   (United States)

Author keywords

[No Author keywords available]

Indexed keywords

AZEOTROPES; COST EFFECTIVENESS; ENERGY CONSERVATION; ESTIMATION; GEOMETRY;

DISTILLATION BOUNDARIES; INVESTMENT; NONIDEAL MIXTURES; SIDE STREAM DISTILLATION COLUMNS;

DISTILLATION COLUMNS;

DESIGN; DISTILLATION COLUMNS;

EID: 0030267255     PISSN: 08885885     EISSN: None     Source Type: Journal    
DOI: 10.1021/ie960036t     Document Type: Article

References (17)

1. d'Ávila, S. G.; Silva, R. S. F. Isothermal Vapor-Liquid Equilibrium Data by Total Pressure Method. J. Chem. Eng. Data 1970, 15, 421-424.
2. Fidkowski, Z. T.; Malone, M. F.; Doherty, M. F. Nonideal Multicomponent Distillation: Use of Bifurcation Theory for Design. AIChE J. 1991, 37, 1761-1779.
3. Fidkowski, Z. T.; Doherty, M. F.; Malone, M. F. Feasibility of Separations for Distillation of Nonideal Ternary Mixtures. AJChE J. 1993, 39, 1303-1321.
4. Glinos, K. N.; Malone, M. F. Design of Sidestream Distillation Columns. Ind. Eng. Chem. Process Des. Dev. 1985a, 24, 822-828.
5. Glinos, K. N.; Malone, M. F. Minimum Vapor Flows in a Distillation Column with a Sidestream Stripper. Ind. Eng. Chem. Process Des. Dev. 1985b, 24, 1087-1090.
6. Glinos, K.; Malone, M. F. Optimality Regions for Complex Column Alternatives in Distillation Systems. Chem. Eng. Res. Des. 1988, 24, 229-240.
7. Gmehling, J.; Onken, U.; Arlt, W. Vapor-Liquid Equilibrium Data Collection; DECHEMA Chemistry Data Series; DECHEMA: Frankfurt, 1978; Vol. I/2b.
8. Gmehling, J.; Onken, U.; Arlt, W. Vapor-Liquid Equilibrium Data Collection; DECHEMA Chemistry Data Series; DECHEMA: Frankfurt, 1981; Vol. I/1a.
9. Gmehling, J.; Onken, U.; Arlt, W. Vapor-Liquid Equilibrium Data Collection; DECHEMA Chemistry Data Series; DECHEMA: Frankfurt, 1981; Vol. I/1b.
10. Julka, V.; Doherty, M. F. Geometric Behavior and Minimum Flows for Nonideal Multicomponent Distillation. Chem. Eng. Sci. 1990, 45, 1801-1822.
11. Julka, V.; Doherty, M. F. Geometric Nonlinear Analysis of Multicomponent Nonideal Distillation: A Simple Computer-Aided Design Procedure. Chem. Eng. Sci. 1993, 48, 1367-1391.
12. Kohler, J.; Kuen, T.; Blass, E. Minimum Energy Demand for Distillations with Distributed Components and Side-Product Withdrawls. Chem. Eng. Sci. 1994, 49, 3325-3330.
13. Levy, S. G.; Van Dongen, D. B.; Doherty, M. F. Design and Synthesis of Homogenous Azoetropic Distillations. 2. Minimum Reflux Calculations for Nonideal and Azeotropic Columns. Ind. Eng. Chem. Fundam. 1985, 24, 463-474.
14. Nikolaides, I. P.; Malone, M. F. Approximate Design of MultipleFeed/Side-Stream Distillation Systems. Ind. Eng. Chem. Res. 1987, 26, 1839-1845.
15. Tedder, D. W.; Rudd, D. F. Parametric Studies in Industrial Distillation: Part 1. Design Comparisons. AIChE J. 1978, 24, 303-315.
16. Underwood, A. J. V. Fractional Distillation of Multi-component Mixtures-Calculation of Minimum Reflux Ratio. J. Inst. Petrol. 1946, 32, 614-626.
17. Underwood, A. J. V. Fractional Distillation of Multi-component Mixtures. Chem. Eng. Prog. 1948, 44, 603-614.