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- In relation to this article, we declare that there is no conflict of interest.
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Received August 27, 2016
Accepted November 3, 2016
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This is an Open-Access article distributed under the terms of the Creative Commons Attribution Non-Commercial License (http://creativecommons.org/licenses/bync/3.0) which permits
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Copyright © KIChE. All rights reserved.
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Controllability of separate heat pump distillation for separating isopropanol-chlorobenzene mixture
College of Chemical Engineering, Qingdao University of Science and Technology, Qingdao 266042, China
Korean Journal of Chemical Engineering, March 2017, 34(3), 866-875(10), 10.1007/s11814-016-0313-1
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Abstract
The isopropanol-chlorobenzene mixture is separated via separate heat pump distillation (SHPD) to achieve significant energy savings. Rigorous steady state and dynamic characteristics for this SHPD process are simulated using Aspen Plus and Aspen Plus Dynamics. Optimized operation conditions including vapor flow rate to compressor are developed on the condition of minimum total annual cost. Two control strategies are proposed to solve feed disturbance issues and the improved structure with QRe/F (lower column reboiler duty/feed flow rate) ratio scheme can maintain the two product purities requirement with smaller transient deviation and shorter settling time.
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You XQ, Rodriguez-Donis I, Gerbaud V, Appl. Energy, 166, 128 (2016)
Wu YC, Lee HY, Huang HP, Chien IL, Ind. Eng. Chem. Res., 53(4), 1537 (2014)
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Li R, Ye Q, Suo XM, Dai X, Yu H, Feng SY, Xia H, Ind. Eng. Chem. Res., 55(22), 6454 (2016)
Li H, Cong H, Li X, Li X, Gao X, Appl. Therm. Eng., 105, 93 (2016)
Diez E, Langston P, Ovejero G, Romero MD, Appl. Therm. Eng., 29, 1216 (2009)
Zhu P, Feng X, Can. J. Chem. Eng., 82, 963 (2003)
Gao XX, Ma ZF, Yang LM, Ma JQ, Ind. Eng. Chem. Res., 52(33), 11695 (2013)
Wang YL, Zhang Z, Zhang H, Zhang Q, Ind. Eng. Chem. Res., 54(5), 1646 (2015)
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Wang YL, Zhang Z, Zhao YJ, Liang SS, Bu GL, Ind. Eng. Chem. Res., 54(34), 8533 (2015)
Wang YL, Liang SS, Bu GL, Liu W, Zhang Z, Zhu ZY, Ind. Eng. Chem. Res., 54(51), 12908 (2015)
Wang QY, Yu BR, Xu CJ, Ind. Eng. Chem. Res., 51(3), 1281 (2012)
Qin JW, Ye Q, Xiong XJ, Li N, Ind. Eng. Chem. Res., 52(31), 10754 (2013)
Yu H, Ye Q, Xu H, Zhang H, Dai X, Ind. Eng. Chem. Res., 54(13), 3384 (2015)
Muhrer CA, Collura MA, Luyben WL, Ind. Eng. Chem. Res., 29, 59 (1990)
Karami G, Amidpour M, Sheibani BH, Salehi GR, Chem. Eng. Process., 97, 23 (2015)
Jogwar SS, Daoutidis P, J. Process Control, 19(10), 1737 (2009)
Babu GUB, Jana AK, Appl. Therm. Eng., 62, 365 (2014)
Yu BR, Wang QY, Xu CJ, Ind. Eng. Chem. Res., 51(3), 1293 (2012)
Zhang H, Ye Q, Qin J, Xu H, Li N, Ind. Eng. Chem. Res., 53, 1189 (2013)
Dejoz A, Gonzalezalfaro V, Llopis FJ, Miguel PJ, Vazquez MI, Fluid Phase Equilib., 134(1-2), 151 (1997)
Turton R, Bailie RC, Whiting WB, Shaelwitz JA, Analysis, Synthesis and Design of Chemical Processes, 2nd Ed., Prentice Hall, Upper Saddle River, NJ (2008).
Luyben WL, Distillation design and control using Aspen simulation, Wiley (2013).
