CFP last date
20 January 2025
Call for Paper
February Edition
IJCA solicits high quality original research papers for the upcoming February edition of the journal. The last date of research paper submission is 20 January 2025

Submit your paper
Know more
The week's pick
Responsive image
SFLA-Based Line Balancing and Task Optimization in Master-Slave Controlled Hanger Transportation Systems for Garment Production

Duc Hoang Nguyen
Random Articles
Reseach Article

Pressure Swing Distillation Simulation and Optimization of Azeotropic IBA + IBAc Mixture

by A. M. Patwardhan, S. P. Shirsat, S. D. Dawande
journal cover thumbnail

International Journal of Computer Applications
Foundation of Computer Science (FCS), NY, USA
Volume 66 - Number 10
Year of Publication: 2013
Authors: A. M. Patwardhan, S. P. Shirsat, S. D. Dawande
10.5120/11118-6079

A. M. Patwardhan, S. P. Shirsat, S. D. Dawande . Pressure Swing Distillation Simulation and Optimization of Azeotropic IBA + IBAc Mixture. International Journal of Computer Applications. 66, 10 ( March 2013), 9-13. DOI=10.5120/11118-6079

@article{ 10.5120/11118-6079,
author = { A. M. Patwardhan, S. P. Shirsat, S. D. Dawande },
title = { Pressure Swing Distillation Simulation and Optimization of Azeotropic IBA + IBAc Mixture },
journal = { International Journal of Computer Applications },
issue_date = { March 2013 },
volume = { 66 },
number = { 10 },
month = { March },
year = { 2013 },
issn = { 0975-8887 },
pages = { 9-13 },
numpages = {9},
url = { https://ijcaonline.org/archives/volume66/number10/11118-6079/ },
doi = { 10.5120/11118-6079 },
publisher = {Foundation of Computer Science (FCS), NY, USA},
address = {New York, USA}
}
%0 Journal Article
%1 2024-02-06T21:21:59.402984+05:30
%A A. M. Patwardhan
%A S. P. Shirsat
%A S. D. Dawande
%T Pressure Swing Distillation Simulation and Optimization of Azeotropic IBA + IBAc Mixture
%J International Journal of Computer Applications
%@ 0975-8887
%V 66
%N 10
%P 9-13
%D 2013
%I Foundation of Computer Science (FCS), NY, USA
Abstract

The present work is to simulate and analyze pressure-swing distillation process for azeotropic IBA-IBAc separation using CHEMCAD simulation software. The total number of feed plates, reflux ratio in first column and total number of plates, operating pressure and the feed stream concentration of IBA for the second column are varied to find the optimum feed plate location, to get the desired output i. e. 99. 5 mol % IBAc and 98. 5 mol % IBA as bottoms from the first and second column respectively, which gives the minimum total heat duty.

References
  1. Mu˜noz, R. , Mont´on, J. B. , Burguet, M. C. , & Torre, J. de la. 2006. Separation of Isobutyl Alcohol and Isobutyl Acetate by Extractive Distillation and Pressure-Swing Distillation: Simulation and optimization. Separation and Purification Technology, 50, 175–183.
  2. Doherty, M. , & Malone, M. 2001. Conceptual Design of Distillation Systems, New York, McGraw-Hill.
  3. Lei, Z. , Li, C. , & Chen, B. 2003. Extractive Distillation: A Review. Separation and Purification Reviews. 32 (2), 121-213.
  4. Klein, A. 2008. Azeotropic Pressure Swing Distillation. Doctoral Thesis, Prozesswissenschaftender Technischen Universität Berlin.
  5. Maier, R. , Brennecke, J. , & Stadtherr, M. 2000. Reliable computation of reactive azeotropes. Comput. Chem. Eng. 24, 1851–1858.
  6. Fleming, H. 1992. Consider membrane pervaporation. Chem. Eng. Prog. 88 (7), 46–52.
  7. Frank, T. 1997. Break Azeotropes With Pressure Sensitive Distillation. Chem. Eng. Prog. 52–63.
  8. Ehrenmann, J. 2008. Synthesis of isobutyl acetate (cherry, raspberry, strawberry). Practical course in organic chemistry. D CHAB, ETH Zurich
  9. Hilmen, K. 2000. Separation of Azeotropic Mixtures: Tools for Analysis and Studies on Batch Distillation Operation. Doctoral Thesis, Norwegian University of Science and Technology.
  10. Mu˜noz R. , Mont´on J. B. , Burguet M. C. , & Torre, J. de la; 2005. Phase equilibria in the Ternary System isobutyl alcohol + isobutyl acetate + 1-hexanol and binary systems System isobutyl alcohol + 1-hexanol, System isobutyl acetate + 1-hexanol at 101. 3 KPa. Fluid Phase Equilibria, 235, 64–71.
Index Terms

Computer Science
Information Sciences

Keywords

Pressure-swing distillation Simulation azeotrope activity coefficient IBA (Isobutyl Alcohol) IBAc (Isobutyl Acetate)

Powered by PhDFocusTM