Volume 75
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Zhou, S., Li, J., Qiao, C., Liu, M., Lu, C., & Bai, Y. (2023). Modeling of pyridine synthesis process in a coupled fluidized bed reactor. Particuology, 75, 69-81. https://doi.org/10.1016/j.partic.2022.06.005
Modeling of pyridine synthesis process in a coupled fluidized bed reactor
Shuaishuai Zhou a b, Jing Li b, Congzhen Qiao a, Mengxi Liu c *, Chunxi Lu c *, Yan Bai a *
a College of Chemistry and Chemical Engineering, Henan University, Kaifeng, 475000, China
b Nanomaterial Engineering Research Center, Henan University, Kaifeng, 475000, China
c Department of State Key Laboratory of Heavy Oil Processing, China University of Petroleum, Beijing, 102249, China
10.1016/j.partic.2022.06.005
Volume 75, April 2023, Pages 69-81
Received 9 May 2022, Revised 1 June 2022, Accepted 15 June 2022, Available online 28 June 2022, Version of Record 14 July 2022.
E-mail: qiaocongzhen@163.com; lcx725@sina.com; baiyan@henu.edu.cn

Highlights

• Reactor model for pyridine synthesis process is constructed.

• A regression program is proposed to obtain the model parameters.

• Optimal operating conditions are given based on prediction results.


Abstract

To obtain the optimal operating conditions of a coupled reactor for pyridine synthesis, reactor modeling process is carried out in this paper. During the modeling process, the flow hydrodynamics, heat transfer behavior, inter-phase mass transfer behavior and reaction kinetics were taken into consideration consequently. Further, a regression program based on least square method was proposed to regress the model parameters. The prediction results agreed well with the experimental results with an average deviation of 5.9%. Finally, by setting suitable aim function, the optimal operating conditions of the coupled reactor for pyridine synthesis were determined.

Graphical abstract
Keywords
Reactor modeling; Pyridine synthesis; Inter-phase mass transfer; Optimal operating conditions