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1
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Zhang Q, Liu Y, Xu P, Wang Y. Rigorous design and control of thermally integrated pressure‐swing reactive distillation process for isobutyl acetate production considering the effect of column pressures. CAN J CHEM ENG 2020. [DOI: 10.1002/cjce.23823] [Citation(s) in RCA: 1] [Impact Index Per Article: 0.3] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 11/07/2022]
Affiliation(s)
- Qingrui Zhang
- College of Chemical Engineering Qingdao University of Science and Technology Qingdao China
| | - Yan Liu
- College of Chemical Engineering Qingdao University of Science and Technology Qingdao China
| | - Pengfei Xu
- College of Chemical Engineering Qingdao University of Science and Technology Qingdao China
| | - Yujun Wang
- College of Chemical Engineering Qingdao University of Science and Technology Qingdao China
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2
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Decision making scheme of integration design and control under uncertainty for enhancing the economic performance of chemical processes with multiplicity behaviors. Chem Eng Res Des 2019. [DOI: 10.1016/j.cherd.2019.07.019] [Citation(s) in RCA: 2] [Impact Index Per Article: 0.4] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 11/17/2022]
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3
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Comparison of the Steady-State Performances of
$$2 \times 2$$
2
×
2
Regulatory Control Structures for Fluid Catalytic Cracking Unit. ARABIAN JOURNAL FOR SCIENCE AND ENGINEERING 2019. [DOI: 10.1007/s13369-019-03782-1] [Citation(s) in RCA: 0] [Impact Index Per Article: 0] [Reference Citation Analysis] [Track Full Text] [Subscribe] [Scholar Register] [Indexed: 10/27/2022]
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4
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Li J, Ding H, Xiang W, Tao M, Liu C. Hydraulic performance of Winpak-C modular catalytic structured packing. CAN J CHEM ENG 2016. [DOI: 10.1002/cjce.22398] [Citation(s) in RCA: 4] [Impact Index Per Article: 0.5] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 11/09/2022]
Affiliation(s)
- Jinming Li
- School of Chemical Engineering and Technology; Tianjin University; Tianjin 300072 China
- State Key Laboratory of Chemical Engineering; Tianjin University; Tianjin 300072 China
- Collaborative Innovation Center of Chemical Science and Engineering (Tianjin); Tianjin University; Tianjin 300072 China
| | - Huidian Ding
- Research Institute of Petroleum Processing; SINOPEC; Beijing 100083 China
| | - Wenyu Xiang
- School of Chemical Engineering and Technology; Tianjin University; Tianjin 300072 China
- State Key Laboratory of Chemical Engineering; Tianjin University; Tianjin 300072 China
- Collaborative Innovation Center of Chemical Science and Engineering (Tianjin); Tianjin University; Tianjin 300072 China
| | - Min Tao
- School of Chemical Engineering and Technology; Tianjin University; Tianjin 300072 China
- State Key Laboratory of Chemical Engineering; Tianjin University; Tianjin 300072 China
- Collaborative Innovation Center of Chemical Science and Engineering (Tianjin); Tianjin University; Tianjin 300072 China
| | - Chunjiang Liu
- School of Chemical Engineering and Technology; Tianjin University; Tianjin 300072 China
- State Key Laboratory of Chemical Engineering; Tianjin University; Tianjin 300072 China
- Collaborative Innovation Center of Chemical Science and Engineering (Tianjin); Tianjin University; Tianjin 300072 China
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5
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6
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Lim KT, Matsumoto H, Yamaki T, Matsuda K. A Framework for Application of Genetic Algorithm to Model-Based Design of Reactive Distillation Process. JOURNAL OF CHEMICAL ENGINEERING OF JAPAN 2014. [DOI: 10.1252/jcej.13we119] [Citation(s) in RCA: 4] [Impact Index Per Article: 0.4] [Reference Citation Analysis] [Track Full Text] [Subscribe] [Scholar Register] [Indexed: 11/11/2022]
Affiliation(s)
- Kai Tun Lim
- Department of Chemical Engineering, Tokyo Institute of Technology
| | | | - Takehiro Yamaki
- Department of Organic Materials Engineering, Yamagata University
| | - Keigo Matsuda
- Department of Chemistry and Chemical Engineering, Yamagata University
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7
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Purohit JL, Mahajani SM, Patwardhan SC. Analysis of Steady-State Multiplicity in Reactive Distillation Columns. Ind Eng Chem Res 2013. [DOI: 10.1021/ie400288r] [Citation(s) in RCA: 12] [Impact Index Per Article: 1.1] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 11/30/2022]
Affiliation(s)
- Jalesh L. Purohit
- Department of Chemical Engineering, Indian Institute of Technology, Bombay, Mumbai 400076,
India
| | - Sanjay M. Mahajani
- Department of Chemical Engineering, Indian Institute of Technology, Bombay, Mumbai 400076,
India
| | - Sachin C. Patwardhan
- Department of Chemical Engineering, Indian Institute of Technology, Bombay, Mumbai 400076,
India
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8
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Jaime-Leal JE, Bonilla-Petriciolet A, Segovia-Hernández JG, Hernández S, Hernández-Escoto H. Analysis and prediction of input multiplicity for the reactive flash separation using reaction-invariant composition variables. Chem Eng Res Des 2012. [DOI: 10.1016/j.cherd.2012.02.017] [Citation(s) in RCA: 2] [Impact Index Per Article: 0.2] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 11/17/2022]
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9
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Behroozsarand A, Shafiei S. Control of TAME reactive distillation using Non-Dominated Sorting Genetic Algorithm-II. J Loss Prev Process Ind 2012. [DOI: 10.1016/j.jlp.2011.06.019] [Citation(s) in RCA: 4] [Impact Index Per Article: 0.3] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 10/18/2022]
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10
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Kaymak DB, Yilmaz D, Gürer AZ. Inferential Temperature Control Structures for Different Types of Two-Reactant Reactive Distillation Systems. Ind Eng Chem Res 2011. [DOI: 10.1021/ie102333q] [Citation(s) in RCA: 11] [Impact Index Per Article: 0.8] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 11/29/2022]
Affiliation(s)
- Devrim B. Kaymak
- Department of Chemical Engineering, Istanbul Technical University, 34469, Maslak, Istanbul, Turkey
| | - Denizhan Yilmaz
- Department of Chemical Engineering, Istanbul Technical University, 34469, Maslak, Istanbul, Turkey
| | - Ahmet Z. Gürer
- Department of Chemical Engineering, Istanbul Technical University, 34469, Maslak, Istanbul, Turkey
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11
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Matsuda K, Ikoshi T, Yamaki T, Shishido M, Iwakabe K, Ohmori T, Nakaiwa M. Steady State Simulation of Reactive Distillation for TAME Synthesis. KAGAKU KOGAKU RONBUN 2011. [DOI: 10.1252/kakoronbunshu.37.104] [Citation(s) in RCA: 2] [Impact Index Per Article: 0.2] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 11/11/2022]
Affiliation(s)
- Keigo Matsuda
- Department of Chemistry and Chemical Engineering, Yamagata University
| | - Tatsuro Ikoshi
- Department of Chemistry and Chemical Engineering, Yamagata University
| | - Takehiro Yamaki
- Department of Chemistry and Chemical Engineering, Yamagata University
| | - Masahiro Shishido
- Department of Chemistry and Chemical Engineering, Yamagata University
| | | | - Takao Ohmori
- Research Institute for Innovation in Sustainable Chemistry, National Institute of Advanced Industrial Science and Technology (AIST)
| | - Masaru Nakaiwa
- Research Institute for Innovation in Sustainable Chemistry, National Institute of Advanced Industrial Science and Technology (AIST)
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12
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Controllable optimized designs of an ideal reactive distillation system using genetic algorithm. Chem Eng Sci 2009. [DOI: 10.1016/j.ces.2009.07.030] [Citation(s) in RCA: 13] [Impact Index Per Article: 0.9] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 11/19/2022]
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13
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Multiple steady states in a CSTR with total condenser: Comparison of equilibrium and nonequilibrium models. CHEMICAL PAPERS 2006. [DOI: 10.2478/s11696-006-0079-8] [Citation(s) in RCA: 3] [Impact Index Per Article: 0.2] [Reference Citation Analysis] [Abstract] [Track Full Text] [Subscribe] [Scholar Register] [Indexed: 11/20/2022]
Abstract
AbstractComparison of equilibrium and nonequilibrium models of a CSTR with total condenser focused on the multiple steady states and dynamic behaviour was carried out. The steady-state behaviour of the model system, MTBE synthesis from methanol and isobutene in a reactive distillation column, was studied in terms of the input parameters, i. e. feed flow rate of methanol or butenes, reflux ratio, and mass of catalyst. The dynamic behaviour of the system during the start-up was investigated and perturbations of manipulated variables were found to cause transitions between the parallel steady states.
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