Control of new energy‐intensified triple column extractive distillation using feed split technique

Author:

Kong Zong Yang1ORCID,Wang Qin2,Yang Ao34,Qin Zhongjian5,Heah Joo Yee6,Sunarso Jaka6

Affiliation:

1. Department of Engineering, School of Engineering and Technology Sunway University Bandar Sunway Malaysia

2. School of Chemistry and Chemical Engineering Chongqing University of Science & Technology Chongqing People's Republic of China

3. College of Safety Engineering Chongqing University of Science & Technology Chongqing People's Republic of China

4. Beijing Institute of Technology Chongqing Innovation Center Chongqing People's Republic of China

5. Appraisal Center for Environment & Engineering of Chongqing Chongqing People's Republic of China

6. Research Centre for Sustainable Technologies, Faculty of Engineering, Computing and Science Swinburne University of Technology Kuching Malaysia

Abstract

AbstractBACKGROUNDHere, we investigated the control performance of extractive distillation intensified with ‘feed split’ (FS) technique – a process intensification technique that has not been widely applied to extractive distillation. Today, only a handful of studies have been reported on this topic, with only one focusing on the control performance and reporting the significant trade‐off between the steady‐state and dynamic performances. Nonetheless, the previous control study was based on the complex double column FS configuration. Recently, a new triple column FS configuration was reported (Sep. Purif. Technol. 2022 (297) 121467), but its control performance was not investigated. Hypothetically, the triple column FS configuration is less complex and does not involve any column integration and thus, may demonstrate a better dynamic performance. This study analyzed the control performances of the triple column FS configuration and the conventional configuration for the binary azeotropic separation of tetrahydrofuran and ethanol.RESULTSTwo types of control structures were examined for both configurations, i.e., the basic temperature control structure and the different feed forward temperature control schemes. The best control structure from each configuration is compared and findings showed that the conventional configuration provides better controllability performance.CONCLUSIONOur results suggested that the conventional configuration can bring the product qualities closer to their setpoint, while providing a lower transient deviation. © 2023 Society of Chemical Industry (SCI).

Funder

Natural Science Foundation of Chongqing

Publisher

Wiley

Subject

Inorganic Chemistry,Organic Chemistry,Pollution,Waste Management and Disposal,Fuel Technology,Renewable Energy, Sustainability and the Environment,General Chemical Engineering,Biotechnology

Cited by 1 articles. 订阅此论文施引文献 订阅此论文施引文献,注册后可以免费订阅5篇论文的施引文献,订阅后可以查看论文全部施引文献

1. An Alternative Control Structure for the Naphtha Distillation Plant Based on Multivariable Model Predictive Control;2023 5th International Conference on Control Systems, Mathematical Modeling, Automation and Energy Efficiency (SUMMA);2023-11-08

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