A nonequilibrium stage model of multicomponent separation processes-V. Computational methods for solving the model equations

Computers and Chemical Engineering

Volumn 12, Issue 12, 1988, Pages 1229-1241

  Powers, M F ^a   Vickeryt, D J ^a   Arehole, A ^a   Taylor, R ^a  

^a CLARKSON UNIVERSITY   (United States)

Author keywords

[No Author keywords available]

Indexed keywords

EID: 0000202869     PISSN: 00981354     EISSN: None     Source Type: Journal    
DOI: 10.1016/0098-1354(88)85073-7     Document Type: Article

References (32)

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5. Reduced order steady state and dynamic models for separation processes
6. Flexible method for the solution of distillation design problems using the Newton—Raphson technique
7. Heterogeneous azeotropic distillation—homotopy-continuation methods
8. Heterogeneous azeotropic distillation—experimental and simulation results
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13. A nonequilibrium stage model of multicomponent separation processes: II. Comparison with experiment
14. A nonequilibrium stage model of multicomponent separation processes: III. The influence of unequal component efficiencies in process design problems
15. Simulation of packed distillation and absorption columns
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19. Simulation Sciences
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25. An efficient continuation method for solving difficult equilibrium stage separation process problems
26. Continuation methods for solving difficult separation process problems
27. Algorithms for the solution of material balance equations for nonconventional multistage operations
28. Solutions of systems of interlinked distillation columns by differential homotopy-continuation methods