Optimal design and operation of a multi-product batch distillation column using dynamic model
- 31 January 1999
- journal article
- Published by Elsevier in Chemical Engineering and Processing - Process Intensification
- Vol. 38 (1) , 61-72
- https://doi.org/10.1016/s0255-2701(98)00065-8
Abstract
No abstract availableKeywords
This publication has 27 references indexed in Scilit:
- Short-Cut Design Procedure for Batch DistillationsIndustrial & Engineering Chemistry Research, 1997
- An efficient design method for binary, azeotropic, batch distillation columnsAIChE Journal, 1991
- Multicomponent batch distillation column designIndustrial & Engineering Chemistry Research, 1991
- Multicomponent batch distillation. 3. Shortcut design of batch distillation columnsIndustrial & Engineering Chemistry Research, 1991
- Optimization of multiple‐fraction batch distillation by nonlinear programmingAIChE Journal, 1990
- Optimal reflux rate policy determination for multicomponent batch distillation columnsComputers & Chemical Engineering, 1987
- Performance of Various Methods in Computing Optimal Control PoliciesThe Chemical Engineering Journal, 1980
- Variational optimization in control and time domainsThe Canadian Journal of Chemical Engineering, 1974
- Optimal operation of a batch packed distillation columnThe Canadian Journal of Chemical Engineering, 1971
- Optimal Distillate-Rate Policy in Batch DistillationIndustrial & Engineering Chemistry Fundamentals, 1963