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da Cruz FE, Manousiouthakis VI. Process Intensification of Multipressure Reactive Distillation Networks Using Infinite Dimensional State-Space (IDEAS). Ind Eng Chem Res 2019. [DOI: 10.1021/acs.iecr.8b04262] [Citation(s) in RCA: 9] [Impact Index Per Article: 1.8] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 11/28/2022]
Affiliation(s)
- Flavio Eduardo da Cruz
- Department of Chemical and Biomolecular Engineering, University of California, Los Angeles, Los Angeles, California 90095, United States
| | - Vasilios I. Manousiouthakis
- Department of Chemical and Biomolecular Engineering, University of California, Los Angeles, Los Angeles, California 90095, United States
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2
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Intensification of Reactive Distillation for TAME Synthesis Based on the Analysis of Multiple Steady-State Conditions. Processes (Basel) 2018. [DOI: 10.3390/pr6120241] [Citation(s) in RCA: 2] [Impact Index Per Article: 0.3] [Reference Citation Analysis] [Abstract] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 11/16/2022] Open
Abstract
Our previous study reported that operation in multiple steady states contributes to an improvement in reaction conversion, making it possible to reduce the energy consumption of the reactive distillation process for tert-amyl methyl ether (TAME) synthesis. This study clarified the factors responsible for an improvement in the reaction conversion for operation in the multiple steady states of the reactive distillation column used in TAME synthesis. The column profiles for those conditions, in which multiple steady states existed and those in which they did not exist, were compared. The vapor and liquid flow rates with the multiple steady states were larger than those when the multiple steady states did not exist. The effect of the duty of the intermediate condenser, which was introduced at the top of the reactive section, on the liquid flow rate for a reflux ratio of 1 was examined. The amount of TAME production increased from 55.2 to 72.1 kmol/h when the intermediate condenser was operated at 0 to −5 MW. Furthermore, the effect of the intermediate reboiler duty on the reaction performance was evaluated. The results revealed that the liquid and vapor flow rates influenced the reaction and separation performances, respectively.
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3
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Interpreting the dynamic effect of internal heat integration on reactive distillation columns. Chin J Chem Eng 2017. [DOI: 10.1016/j.cjche.2016.07.002] [Citation(s) in RCA: 1] [Impact Index Per Article: 0.1] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 11/23/2022]
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4
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Li G, Gao D, Shi J. A New Stripping Column Process and Optimization of Its Operation. Chem Eng Technol 2016. [DOI: 10.1002/ceat.201500683] [Citation(s) in RCA: 2] [Impact Index Per Article: 0.3] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 11/09/2022]
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5
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Li H, Wu Y, Li X, Gao X. State-of-the-Art of Advanced Distillation Technologies in China. Chem Eng Technol 2016. [DOI: 10.1002/ceat.201500656] [Citation(s) in RCA: 32] [Impact Index Per Article: 4.0] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 11/06/2022]
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6
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Demirel B, Kaymak DB. Control of Quaternary Reactive Distillation Columns: Effects of Number and Location of Temperature Loops. Ind Eng Chem Res 2013. [DOI: 10.1021/ie3032789] [Citation(s) in RCA: 5] [Impact Index Per Article: 0.5] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 11/28/2022]
Affiliation(s)
- Baris Demirel
- Department of Chemical Engineering, Istanbul Technical University, 34469, Maslak, Istanbul, Turkey
| | - Devrim B. Kaymak
- Department of Chemical Engineering, Istanbul Technical University, 34469, Maslak, Istanbul, Turkey
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7
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Murrieta-Dueñas R, Gutiérrez-Guerra R, Segovia-Hernández JG, Hernández S. Analysis of control properties of intensified distillation sequences: Reactive and extractive cases. Chem Eng Res Des 2011. [DOI: 10.1016/j.cherd.2011.02.021] [Citation(s) in RCA: 23] [Impact Index Per Article: 1.8] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 10/18/2022]
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8
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Wang Q, Ng D, Mannan MS. Study on the Reaction Mechanism and Kinetics of the Thermal Decomposition of Nitroethane. Ind Eng Chem Res 2009. [DOI: 10.1021/ie900849n] [Citation(s) in RCA: 35] [Impact Index Per Article: 2.3] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 12/31/2022]
Affiliation(s)
- Qingsheng Wang
- Mary Kay O’Connor Process Safety Center, Artie McFerrin Department of Chemical Engineering, Texas A&M University, College Station, Texas 77843-3122
| | - Dedy Ng
- Mary Kay O’Connor Process Safety Center, Artie McFerrin Department of Chemical Engineering, Texas A&M University, College Station, Texas 77843-3122
| | - M. Sam Mannan
- Mary Kay O’Connor Process Safety Center, Artie McFerrin Department of Chemical Engineering, Texas A&M University, College Station, Texas 77843-3122
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9
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Huang K, Zhu F, Ding W, Wang SJ. Control of a high-purity ethylene glycol reactive distillation column with insights of process dynamics. AIChE J 2009. [DOI: 10.1002/aic.11808] [Citation(s) in RCA: 11] [Impact Index Per Article: 0.7] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 11/12/2022]
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10
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Sun J, Huang K, Wang S. Deepening Internal Mass Integration in Design of Reactive Distillation Columns, 1: Principle and Procedure. Ind Eng Chem Res 2009. [DOI: 10.1021/ie801144n] [Citation(s) in RCA: 15] [Impact Index Per Article: 1.0] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 11/28/2022]
Affiliation(s)
- Jie Sun
- College of Information Science and Technology, Beijing University of Chemical Technology, Beijing 100029, People’s Republic of China
| | - Kejin Huang
- College of Information Science and Technology, Beijing University of Chemical Technology, Beijing 100029, People’s Republic of China
| | - Shaofeng Wang
- College of Information Science and Technology, Beijing University of Chemical Technology, Beijing 100029, People’s Republic of China
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11
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Kumar MVP, Kaistha N. Internal Heat Integration and Controllability of Double Feed Reactive Distillation Columns, 1. Effect of Feed Tray Location. Ind Eng Chem Res 2008. [DOI: 10.1021/ie071638n] [Citation(s) in RCA: 19] [Impact Index Per Article: 1.2] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 11/28/2022]
Affiliation(s)
- M. V. Pavan Kumar
- Department of Chemical Engineering, Indian Institute of Technology Kanpur, Kanpur 208016, India
| | - N. Kaistha
- Department of Chemical Engineering, Indian Institute of Technology Kanpur, Kanpur 208016, India
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12
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Chen CS, Yu CC. Effects of Relative Volatility Ranking on Design and Control of Reactive Distillation Systems with Ternary Decomposition Reactions. Ind Eng Chem Res 2008. [DOI: 10.1021/ie701787e] [Citation(s) in RCA: 19] [Impact Index Per Article: 1.2] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 11/28/2022]
Affiliation(s)
- Chin-Shih Chen
- Department of Chemical Engineering, National Taiwan University, Taipei 106-17, Taiwan
| | - Cheng-Ching Yu
- Department of Chemical Engineering, National Taiwan University, Taipei 106-17, Taiwan
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13
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Huang K, Wang SJ, Ding W. Towards further internal heat integration in design of reactive distillation columns—Part III: Application to a MTBE reactive distillation column. Chem Eng Sci 2008. [DOI: 10.1016/j.ces.2008.01.006] [Citation(s) in RCA: 20] [Impact Index Per Article: 1.3] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 11/29/2022]
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