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Optimization strategies for chiral separation by true moving bed chromatography using Particles Swarm Optimization (PSO) and new Parallel PSO variant. Comput Chem Eng 2019. [DOI: 10.1016/j.compchemeng.2019.01.020] [Citation(s) in RCA: 25] [Impact Index Per Article: 4.2] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 11/18/2022]
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Yuan X, Li H, Ye M, Liu Z. Study of the coke distribution in MTO fluidized bed reactor with MP-PIC approach. CAN J CHEM ENG 2018. [DOI: 10.1002/cjce.23239] [Citation(s) in RCA: 18] [Impact Index Per Article: 2.6] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 11/11/2022]
Affiliation(s)
- Xiaoshuai Yuan
- Dalian National Laboratory for Clean Energy, National Engineering Laboratory for MTO, Dalian Institute of Chemical Physics, Chinese Academy of Sciences; Dalian 116023 China
- University of Chinese Academy of Sciences; Beijing 100049 China
| | - Hua Li
- Dalian National Laboratory for Clean Energy, National Engineering Laboratory for MTO, Dalian Institute of Chemical Physics, Chinese Academy of Sciences; Dalian 116023 China
| | - Mao Ye
- Dalian National Laboratory for Clean Energy, National Engineering Laboratory for MTO, Dalian Institute of Chemical Physics, Chinese Academy of Sciences; Dalian 116023 China
| | - Zhongmin Liu
- Dalian National Laboratory for Clean Energy, National Engineering Laboratory for MTO, Dalian Institute of Chemical Physics, Chinese Academy of Sciences; Dalian 116023 China
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Coelho LDS, Ayala HVH, Coelho AAR. Variable structure control optimized by differential evolution approach applied to continuous stirred tank reactor. Chem Eng Res Des 2015. [DOI: 10.1016/j.cherd.2015.05.020] [Citation(s) in RCA: 3] [Impact Index Per Article: 0.3] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 11/15/2022]
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Sun S, Li J. Kinetics of the Entire Methanol to Olefins Process over Sapo-34 Catalyst. PROGRESS IN REACTION KINETICS AND MECHANISM 2015. [DOI: 10.3184/146867815x14212355041079] [Citation(s) in RCA: 4] [Impact Index Per Article: 0.4] [Reference Citation Analysis] [Abstract] [Track Full Text] [Subscribe] [Scholar Register] [Indexed: 11/17/2022]
Abstract
The kinetics of the entire process of the SAPO-34 catalyst for the transformation of methanol into olefins in the 400–450 °C range has been established by using the experimental data obtained in an isothermal fixed bed reactor. The model considers the activity change of SAPO-34 zeolite with time on stream. The activity of the catalyst consists of two parts: the stabilisation activity (while methanol is fully transformed) and the deactivation activity (while methanol is not all transformed). According to the activity of the catalyst, this study measured the evolution of each olefin with time on stream respectively.
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Affiliation(s)
- Shiyuan Sun
- State Key Laboratory of Chemical Resource Engineering, Beijing University of Chemical Technology, No.15, Bei San Huan East Road, Beijing 100029, China
| | - Jianwei Li
- State Key Laboratory of Chemical Resource Engineering, Beijing University of Chemical Technology, No.15, Bei San Huan East Road, Beijing 100029, China
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