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High p-xylene selectivity in aluminum-based metal–organic framework with 1-D channels. J IND ENG CHEM 2022. [DOI: 10.1016/j.jiec.2022.10.021] [Citation(s) in RCA: 0] [Impact Index Per Article: 0] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 11/13/2022]
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Sumedha M, Bhartiya S. Dual Switch Simulated Moving Bed Chromatography: An optimal two-fraction yielding separation process. J Chromatogr A 2022; 1682:463449. [DOI: 10.1016/j.chroma.2022.463449] [Citation(s) in RCA: 0] [Impact Index Per Article: 0] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Received: 03/16/2022] [Revised: 08/19/2022] [Accepted: 08/23/2022] [Indexed: 11/25/2022]
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Geng Z, Yang Y, Yang S, Zhou J, Lyu H. Purification of rutin by supercritical fluid simulated moving bed chromatography. CAN J CHEM ENG 2022. [DOI: 10.1002/cjce.24237] [Citation(s) in RCA: 1] [Impact Index Per Article: 0.3] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 11/12/2022]
Affiliation(s)
- Zhongfeng Geng
- Key Laboratory for Green Chemical Technology of Ministry of Education, R&D Center for Petrochemical Technology Tianjin University Tianjin China
- Collaborative Innovation Center of Chemical Science and Engineering Tianjin China
| | - Yuzhu Yang
- Key Laboratory for Green Chemical Technology of Ministry of Education, R&D Center for Petrochemical Technology Tianjin University Tianjin China
- Collaborative Innovation Center of Chemical Science and Engineering Tianjin China
| | - Shuyuan Yang
- Key Laboratory for Green Chemical Technology of Ministry of Education, R&D Center for Petrochemical Technology Tianjin University Tianjin China
- Collaborative Innovation Center of Chemical Science and Engineering Tianjin China
| | - Jinyi Zhou
- Key Laboratory for Green Chemical Technology of Ministry of Education, R&D Center for Petrochemical Technology Tianjin University Tianjin China
- Collaborative Innovation Center of Chemical Science and Engineering Tianjin China
| | - Huisheng Lyu
- Key Laboratory for Green Chemical Technology of Ministry of Education, R&D Center for Petrochemical Technology Tianjin University Tianjin China
- Collaborative Innovation Center of Chemical Science and Engineering Tianjin China
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Kim Y, Kim T, Park C, Lee J, Cho H, Kim M, Moon I. Development of novel flow distribution apparatus for simulated moving bed to improve degree of mixing. Comput Chem Eng 2022. [DOI: 10.1016/j.compchemeng.2021.107553] [Citation(s) in RCA: 1] [Impact Index Per Article: 0.3] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 11/25/2022]
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Kim Y, Cho S, Jang K, Lee J, Kim M, Moon I. Effect of radial distribution of injected flow on simulated moving bed performance. J Chromatogr A 2021; 1662:462703. [PMID: 34906766 DOI: 10.1016/j.chroma.2021.462703] [Citation(s) in RCA: 0] [Impact Index Per Article: 0] [Reference Citation Analysis] [Abstract] [Key Words] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Received: 10/21/2021] [Revised: 11/19/2021] [Accepted: 11/21/2021] [Indexed: 11/30/2022]
Abstract
In the modeling of a simulated moving bed, several assumptions are considered, the key assumption is there are no radial concentration gradients based on perfect mixing. However, it is difficult to achieve perfect mixing because the injected flowrate of the bed is periodically changed in the process. In this study, the performance of the simulated moving bed process was analyzed when the injected flow such as the feed or desorbent stream was unevenly distributed. To this end, the distribution function of the injected flow was calculated and applied to the model. Two types of distribution functions were obtained using the experimental results of a previous study, and the simulation results were compared with classical modeling assuming perfect mixing. In the base case simulation, the purity was similar in all cases, the productivity was higher more than 5% in the even distribution case compared to the most uneven distribution case. The effect of distribution was analyzed through sensitivity analysis by changing the overall flow rate, switching time, bed length, and flow rate of sections 2 and 3. As a result, regardless of the distribution applied, the trends of the performance parameters were the same. However, the more uneven the distribution, the greater the difference in productivity, recovery, and desorbent consumption compared to the even distribution case. It was confirmed that the design that distributes the injected flow more evenly has a better performance.
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Affiliation(s)
- Youngjin Kim
- Department of Chemical and Biomolecular Engineering, Yonsei University, 50, Yonsei-ro, Seodaemun-gu, Seoul, 03722, Republic of Korea
| | - Sunghyun Cho
- Department of Chemical and Biomolecular Engineering, Yonsei University, 50, Yonsei-ro, Seodaemun-gu, Seoul, 03722, Republic of Korea
| | - Kyojin Jang
- Department of Chemical and Biomolecular Engineering, Yonsei University, 50, Yonsei-ro, Seodaemun-gu, Seoul, 03722, Republic of Korea
| | - Jaewon Lee
- Department of Chemical and Biomolecular Engineering, Yonsei University, 50, Yonsei-ro, Seodaemun-gu, Seoul, 03722, Republic of Korea
| | - Myungjun Kim
- Trishinn, 331, Dongmak-ro, Mapo-gu, Seoul, 04156, Republic of Korea
| | - Il Moon
- Department of Chemical and Biomolecular Engineering, Yonsei University, 50, Yonsei-ro, Seodaemun-gu, Seoul, 03722, Republic of Korea.
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Kim KM, Han KW, Kim SI, Bae YS. Simulated moving bed with a product column for improving the separation performance. J IND ENG CHEM 2020. [DOI: 10.1016/j.jiec.2020.04.032] [Citation(s) in RCA: 0] [Impact Index Per Article: 0] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 10/24/2022]
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