Variables indicating the cost of vapour-liquid equilibrium separation processes

Chemical Engineering Science

Volumn 51, Issue 21, 1996, Pages 4749-4757

  Jobson, Megan ^a   Hildebrandt, Diane ^b   Glasser, David ^b  

^a UNIVERSITY OF MANCHESTER   (United Kingdom)

^b NONE

Author keywords

[No Author keywords available]

Indexed keywords

CALCULATIONS; CONDENSATION; COST EFFECTIVENESS; DISTILLATION COLUMNS; ECONOMICS; HEURISTIC METHODS; LIQUIDS; PHASE EQUILIBRIA; VAPORIZATION; VAPORS;

CAPACITY VARIABLES; CAPITAL COSTS; ENERGY COSTS;

PHASE SEPARATION;

EID: 0030294005     PISSN: 00092509     EISSN: None     Source Type: Journal    
DOI: 10.1016/0009-2509(96)00259-X     Document Type: Article

References (19)

1. Douglas, J. M., 1988, Conceptual Design of Chemical Processes, pp. 178 and 461, McGraw-Hill, New York.
2. Doukas, N. and Luyben, W. L., 1978, Economics of alternative distillation configurations for the separation of ternary mixtures. Ind. Engng Chem. Proc. Des. Dev. 17, 272-281.
3. Fisher, W. R., Doherty, M. F. and Douglas, J. M., 1985, Evaluating significant economic trade-offs for process design and steady-state control optimization problems. A.I.Ch.E. J. 31, 1761-1779.
4. Flower, J. R. and Jackson, R., 1964, Energy requirements in the separation of mixtures by distillation. Trans. Instn. Chem. Engrs 54, T249-T258.
5. Ho, F. G. and Keller, G. E., 1987, Process integration, In Recent Developments in Chemical Process and Plant Design (Edited by Liu, Y. A., McGee, H. A. and Epperly, W. R.) pp. 71-87. Wiley Interscience, New York.
6. Jobson, M., Hildebrandt, D. and Glasser, D., 1995, Attainable products for the vapour-liquid separation of homogeneous ternary mixtures. The Chem. Engng J. 59, 51-70.
7. Jobson, M., 1996, Feasible products and cost indicators for vapour-liquid equilibrium separation processes. Ph.D. Thesis, University of the Witwatersrand, Johannesburg, South Africa.
8. Knight, J. R. and Doherty, M. F., 1989, Optimal design and synthesis of homogeneous azeotropic distillation sequences. Ind. Engng Chem. Res. 28, 564-572.
9. Koehler, J., Aguirre, P. and Blass, E, 1991, Minimum reflux calculations for nonideal mixtures using the reversible distillation model. Chem. Engng Sci. 46, 3007-3021.
10. Kokossis, A. C. and Floudas, C. A., 1991, Synthesis of isothermal reactor-separator-recycle systems. Chem. Engng Sci. 46, 1361-1383.
11. Laroche, L., Bekiaris, N., Andersen, H. W. and Morari, M., 1992, The curious behaviour of homogeneous azeotropic distillation - implications for entrainer selection. A.I.Ch.E. J. 38, 1309-1328.
12. Levy, S. G., Van Dongen, D. B. and Doherty, M. F., 1985, Design and synthesis of homogeneous azeotropic distillations 2. Minimum reflux calculations for non-ideal and azeotropic columns. Ind. Engng Chem. Fundam. 24, 463-474.
13. Linnhoff, B., Dunford, H. and Smith, R., 1983, Heat integration of distillation columns into overall processes. Chem. Engng Sci. 38, 1175-1188.
14. Malone, M. F., Glinos, K., Marquez, F. E. and Douglas, J. M., 1985, Simple, analytical criteria for the sequencing of distillation columns. A.I.Ch.E. J., 31, 683-689.
15. McCabe, W. L. and Smith, J. C., 1956, Unit Operations in Chemical Engineering, pp. 705-706. McGraw-Hill, New York.
16. Modi, A. K. and Westerberg, A. W., 1991, Distillation column sequencing using marginal price. A.I.Ch.E. J., 31, 839-848.
17. Nishimura, H. and Hiraizumi, Y., 1971, Optimal system pattern for multicomponent distillation systems. Int. Chem. Engng 11, 188-193.
18. Tedder, D. W. and Rudd, D. G., 1978a, Parametric studies in industrial distillation 1. Design comparisons. A.I.Ch.E. J. 24, 303-315.
19. Tedder, D. W. and Rudd, D. G., 1978b, Parametric studies in industrial distillation 2. Heuristic Optimization. A.I.Ch.E. J. 24, 316-323.