Optimal Structure Synthesis of Internally Heat Integrated Distillation Column
Author:
Affiliation:
1. Division of Process Control and Process Systems Engineering, Department of Chemical Engineering, Kyoto University
Publisher
Society of Chemical Engineers, Japan
Subject
General Chemical Engineering,General Chemistry
Link
https://www.jstage.jst.go.jp/article/jcej/48/3/48_14we077/_pdf
Reference14 articles.
1. Alcántara-Avila, J., M. Kano and S. Hasebe; “Environmental and Economic Optimization of Distillation Structures to Produce Anhydrous Ethanol,” Comput. Aided Chem. Eng., 30, 712–716 (2012)
2. Drake, J. E. and V. Manousiouthakis; “IDEAS Approach to Process Network Synthesis: Minimum Plate Area for Complex Distillation Networks with Fixed Utility Cost,” Ind. Eng. Chem. Res., 41, 4984–4992 (2002a)
3. Drake, J. E. and V. Manousiouthakis; “IDEAS Approach to Process Network Synthesis: Minimum Utility Cost for Complex Distillation Networks,” Chem. Eng. Sci., 57, 3095–3106 (2002b)
4. Eldridge, R. B., A. F. Seibert and S. Robinson; Hybrid Separations/Distillation Technology: Research Opportunities for Energy and Emissions Reduction, Tech. Report April, The U.S. Department of Energy, Office of Energy Efficiency and Renewable Energy, Washington DC, U.S.A. (2005)
5. Harwardt, A. and W. Marquardt; “Heat-Integrated Distillation Columns: Vapor Recompression or Internal Heat Integration?” AIChE J., 58, 3740–3750 (2012)
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