Development of a mass transfer model for the rate-based simulation of a batch distillation column-Reference-Cited by-同舟云学术

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Development of a mass transfer model for the rate-based simulation of a batch distillation column

Published:2020-09 Issue: Volume:140 Page:106981
ISSN:0098-1354
Container-title:Computers & Chemical Engineering
language:en
Short-container-title:Computers & Chemical Engineering

Author:

May-Vázquez Mayra Margarita,Rodríguez-Ángeles Mario Alberto,Gómez-Castro Fernando Israel,Espinoza-Zamora Jesús,Murrieta-Luna Edilberto

Funder

CONACYT

Publisher

Elsevier BV

Subject

Computer Science Applications,General Chemical Engineering

Reference41 articles.

1. Estimation of mass transfer coefficient in a packed distillation column using batch mode;Al-Hemiri;J. Chem. Pet. Eng.,2011

2. Hybrid separation processes-combination of reactive distillation with membrane separation;Buchaly;Chem. Eng. Process.,2007

3. Modelling methanol recovery in wine distillation stills with packing columns;Carvallo;Food Control,2011

4. Prediction of point efficiencies on sieve trays. 1. binary systems;Chan;Ind. Eng. Chem. Process Des. Dev.,1984

5. Prediction of point efficiencies on sieve trays. 2. multicomponent systems;Chan;Ind. Eng. Chem. Process Des. Dev.,1984

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3. Optimal control of a rate-based modelled batch distillation column: Initialization strategy;Computers & Chemical Engineering;2022-06

4. Towards a comprehensive approach to optimal control of non-ideal binary batch distillation;Optimization and Engineering;2022-05-30

5. Experimentation and dynamic modeling of batch packed distillation for star anise essential oil purification;Separation Science and Technology;2021-12-07

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