Heat-Integrated Hybrid Membrane Separation–Distillation Process for Energy-Efficient Isopropyl Alcohol Dehydration
Author:
Affiliation:
1. Research Institute for Chemical Process Technology, National Institute of Advanced Industrial Science and Technology (AIST)
Publisher
Society of Chemical Engineers, Japan
Subject
General Chemical Engineering,General Chemistry
Link
https://www.jstage.jst.go.jp/article/jcej/51/10/51_18we039/_pdf
Reference24 articles.
1. Arifin, S. and I. L. Chien; “Combined Preconcentrator/Recovery Column Design for Isopropyl Alcohol Dehydration Process,” Ind. Eng. Chem. Res., 46, 2535–2543 (2007)
2. Chang, W. T., C. T. Huang and S. H. Cheng; “Design and Control of a Complete Azeotropic Distillation System Incorporating Stripping Columns for Isopropyl Alcohol Dehydration,” Ind. Eng. Chem. Res., 51, 2997–3006 (2012)
3. Csefalvay, E., Z. Szitkai, P. Mizsey and Z. Fonyo; “Experimental Data based Modelling and Simulation of Isopropanol Dehydration by Pervaporation,” Desalication, 229, 94–108 (2008)
4. Fontalvo, J., P. Cuellar, J. M. K. Timmer, M. A. G. Vorstman, J. G. Wijers and J. T. F. Keurentjes; “Comparing Pervaporation and Vapor Permeation Hybrid Distillation Processes,” Ind. Eng. Chem. Res., 44, 5259–5266 (2005)
5. Harvianto, G. R., F. Ahmad, L. C. Nhien and M. Lee; “Vapor Permeation–Distillation Hybrid Processes for Cost-Effective Isopropanol Dehydration: Modeling, Simulation and Optimization,” J. Membr. Sci., 497, 108–119 (2016)
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