Mathematical modeling and numerical integration of multicomponent batch distillation equations
- 1 January 1968
- journal article
- research article
- Published by Wiley in AIChE Journal
- Vol. 14 (1), 190-199
- https://doi.org/10.1002/aic.690140132
Abstract
No abstract availableKeywords
This publication has 17 references indexed in Scilit:
- Transient response and feed‐forward control of a distillation tower subject to a sequence of upsetsAIChE Journal, 1967
- Exponential DifferencesMathematics of Computation, 1966
- A Method for the Numerical Integration of Coupled First-Order Differential Equations with Greatly Different Time ConstantsMathematics of Computation, 1966
- Stability Properties of Adams-Moulton Type MethodsMathematics of Computation, 1965
- Stabilizing Predictors for Weakly Unstable CorrectorsMathematics of Computation, 1965
- A Modified Multistep Method for the Numerical Integration of Ordinary Differential EquationsJournal of the ACM, 1965
- Experimental transient response of a pilot‐plant distillation column: Part IV. Response of a ten‐tray columnAIChE Journal, 1964
- Stability Properties of Predictor-Corrector Methods for Ordinary Differential EquationsJournal of the ACM, 1962
- Calculation procedures for binary batch rectificationAIChE Journal, 1960
- The Use of Exponential Sums in Step by Step IntegrationMathematical Tables and Other Aids to Computation, 1952