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Thermochemical Analysis of a Packed-Bed Reactor Using Finite Elements with FlexPDE and COMSOL Multiphysics. Processes (Basel) 2022. [DOI: 10.3390/pr10061144] [Citation(s) in RCA: 1] [Impact Index Per Article: 0.5] [Reference Citation Analysis] [Abstract] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 02/04/2023] Open
Abstract
This work presents the thermochemical analysis of a packed-bed reactor via multi-dimensional CFD modeling using FlexPDE and COMSOL Multiphysics. The temperature, concentration, and reaction rate profiles for methane production following the Fischer–Tropsch (F-T) synthesis were studied. To this end, stationary and dynamic differential equations for mass and heat transfer were solved via the finite element technique. The transport equations for 1-D and 2-D models using FlexPDE consider dispersion models, where the fluid and the catalyst can be treated as either homogeneous or heterogenous systems depending on the gradient extents. On the other hand, the 3-D model obtained in COMSOL deems the transport equations incorporated in the Porous Media module. The aim was to compare the FlexPDE and COMSOL models, and to validate them with experimental data from literature. As a result, all models were in good agreement with experimental data, especially for the 2-D and 3-D dynamic models. In terms of kinetics, the predicted reaction rate profiles from the COMSOL model and the 2-D dynamic model followed the temperature trend, thus reflecting the temperature dependence of the reaction. Based on these findings, it was demonstrated that applying different approaches for the CFD modeling of F-T processes conducts reliable results.
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Ountaksinkul K, Sripinun S, Bumphenkiattikul P, Bubphacharoen S, Vongachariya A, Jantharasuk A, Praserthdam P, Assabumrungrat S. Characterization of single-phase flow hydrodynamics in a Berty reactor using computational fluid dynamics (CFD). REACT CHEM ENG 2022. [DOI: 10.1039/d1re00390a] [Citation(s) in RCA: 1] [Impact Index Per Article: 0.5] [Reference Citation Analysis] [Abstract] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 11/21/2022]
Abstract
This work studies the flow characteristics in a Berty reactor, a gradientless reactor for kinetic studies, using three-dimensional (3D) computational fluid dynamics (CFD), and a non-ideal continuous stirred tank reactor (CSTR) model.
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Affiliation(s)
- Khunnawat Ountaksinkul
- Center of Excellence on Catalysis and Catalytic Reaction Engineering, Department of Chemical Engineering, Faculty of Engineering, Chulalongkorn University, Bangkok 10330, Thailand
| | - Sirada Sripinun
- Center of Excellence on Catalysis and Catalytic Reaction Engineering, Department of Chemical Engineering, Faculty of Engineering, Chulalongkorn University, Bangkok 10330, Thailand
| | - Panut Bumphenkiattikul
- Advanced Process Modeling, Digital Manufacturing Technology Group, Olefins and Operations Technology, Chemicals Business, SCG, Thailand
- The Thai Institute of Chemical Engineering and Applied Chemistry, SCG Chemicals, Co., Ltd., 1 Siam Cement Road, Bang sue, Bangkok 10800, Thailand
| | | | - Arthit Vongachariya
- Advanced Process Modeling, Digital Manufacturing Technology Group, Olefins and Operations Technology, Chemicals Business, SCG, Thailand
- The Thai Institute of Chemical Engineering and Applied Chemistry, SCG Chemicals, Co., Ltd., 1 Siam Cement Road, Bang sue, Bangkok 10800, Thailand
| | - Amnart Jantharasuk
- SCG Chemicals, Co., Ltd., 1 Siam Cement Road, Bang sue, Bangkok 10800, Thailand
| | - Piyasan Praserthdam
- Center of Excellence on Catalysis and Catalytic Reaction Engineering, Department of Chemical Engineering, Faculty of Engineering, Chulalongkorn University, Bangkok 10330, Thailand
| | - Suttichai Assabumrungrat
- Center of Excellence on Catalysis and Catalytic Reaction Engineering, Department of Chemical Engineering, Faculty of Engineering, Chulalongkorn University, Bangkok 10330, Thailand
- Bio-Circular-Green-economy Technology & Engineering Center, BCGeTEC, Department of Chemical Engineering, Faculty of Engineering, Chulalongkorn University, Bangkok 10330, Thailand
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Cordero-Lanzac T, Aguayo AT, Castaño P, Bilbao J. Kinetics and reactor modeling of the conversion of n-pentane using HZSM-5 catalysts with different Si/Al ratios. REACT CHEM ENG 2019. [DOI: 10.1039/c9re00222g] [Citation(s) in RCA: 9] [Impact Index Per Article: 1.8] [Reference Citation Analysis] [Abstract] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 11/21/2022]
Abstract
The production of olefins and aromatics from n-pentane using two ZSM-5 catalysts is faithfully predicted by a versatile kinetic model.
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Affiliation(s)
- Tomás Cordero-Lanzac
- Department of Chemical Engineering
- University of the Basque Country (UPV/EHU)
- Bilbao
- Spain
| | - Andrés T. Aguayo
- Department of Chemical Engineering
- University of the Basque Country (UPV/EHU)
- Bilbao
- Spain
| | - Pedro Castaño
- Department of Chemical Engineering
- University of the Basque Country (UPV/EHU)
- Bilbao
- Spain
- Multiscale Reaction Engineering
| | - Javier Bilbao
- Department of Chemical Engineering
- University of the Basque Country (UPV/EHU)
- Bilbao
- Spain
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