1
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On the differences between periodic domain and fluidized bed. Chem Eng Sci 2022. [DOI: 10.1016/j.ces.2022.118395] [Citation(s) in RCA: 0] [Impact Index Per Article: 0] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 12/24/2022]
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2
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3
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Yang Y, Zhang Q, Pan T, Qu Y, Liu X, Li X, Cheng Y, Wang L, Liu W. The hydrodynamics of low-density particles and optimization of the EMMS calculation process. POWDER TECHNOL 2022. [DOI: 10.1016/j.powtec.2022.117511] [Citation(s) in RCA: 0] [Impact Index Per Article: 0] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 10/18/2022]
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4
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Lu L, Gao X, Dietiker JF, Shahnam M, Rogers WA. Development of a Filtered CFD-DEM Drag Model with Multiscale Markers Using an Artificial Neural Network and Nonlinear Regression. Ind Eng Chem Res 2021. [DOI: 10.1021/acs.iecr.1c03644] [Citation(s) in RCA: 4] [Impact Index Per Article: 1.3] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 11/30/2022]
Affiliation(s)
- Liqiang Lu
- National Energy Technology Laboratory, 3610 Collins Ferry Road, Morgantown, West Virginia 26507, United States
- NETL Support Contractor, 3610 Collins Ferry Road, Morgantown, West Virginia 26507, United States
| | - Xi Gao
- Department of Chemical Engineering, Guangdong Technion-Israel Institute of Technology, 241 Daxue Road, Shantou, Guangdong 515063, China
| | - Jean-François Dietiker
- National Energy Technology Laboratory, 3610 Collins Ferry Road, Morgantown, West Virginia 26507, United States
- NETL Support Contractor, 3610 Collins Ferry Road, Morgantown, West Virginia 26507, United States
| | - Mehrdad Shahnam
- National Energy Technology Laboratory, 3610 Collins Ferry Road, Morgantown, West Virginia 26507, United States
| | - William A. Rogers
- National Energy Technology Laboratory, 3610 Collins Ferry Road, Morgantown, West Virginia 26507, United States
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5
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6
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Xie L, Wang D, Wang H. Effective drag coefficient correlation for coarse coal particle fluidization in transitional flow regime. Chem Eng Res Des 2021. [DOI: 10.1016/j.cherd.2021.06.005] [Citation(s) in RCA: 3] [Impact Index Per Article: 1.0] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 10/21/2022]
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7
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Zhu L, Ouyang B, Lei H, Luo Z. Conventional and
data‐driven
modeling of filtered drag, heat transfer, and reaction rate in
gas–particle
flows. AIChE J 2021. [DOI: 10.1002/aic.17299] [Citation(s) in RCA: 14] [Impact Index Per Article: 4.7] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 01/06/2023]
Affiliation(s)
- Li‐Tao Zhu
- Department of Chemical Engineering, School of Chemistry and Chemical Engineering, State Key Laboratory of Metal Matrix Composites Shanghai Jiao Tong University Shanghai People's Republic of China
| | - Bo Ouyang
- Department of Chemical Engineering, School of Chemistry and Chemical Engineering, State Key Laboratory of Metal Matrix Composites Shanghai Jiao Tong University Shanghai People's Republic of China
| | - He Lei
- Department of Chemical Engineering, School of Chemistry and Chemical Engineering, State Key Laboratory of Metal Matrix Composites Shanghai Jiao Tong University Shanghai People's Republic of China
| | - Zheng‐Hong Luo
- Department of Chemical Engineering, School of Chemistry and Chemical Engineering, State Key Laboratory of Metal Matrix Composites Shanghai Jiao Tong University Shanghai People's Republic of China
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8
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Micale D, Uglietti R, Bracconi M, Maestri M. Coupling Euler-Euler and Microkinetic Modeling for the Simulation of Fluidized Bed Reactors: an Application to the Oxidative Coupling of Methane. Ind Eng Chem Res 2021; 60:6687-6697. [PMID: 34054213 PMCID: PMC8154421 DOI: 10.1021/acs.iecr.0c05845] [Citation(s) in RCA: 6] [Impact Index Per Article: 2.0] [Reference Citation Analysis] [Abstract] [Track Full Text] [Download PDF] [Figures] [Journal Information] [Subscribe] [Scholar Register] [Received: 11/27/2020] [Revised: 02/02/2021] [Accepted: 02/04/2021] [Indexed: 11/28/2022]
Abstract
We propose a numerical methodology to combine detailed microkinetic modeling and Eulerian-Eulerian methods for the simulation of industrial fluidized bed reactors. An operator splitting-based approach has been applied to solve the detailed kinetics coupled with the solution of multiphase gas-solid flows. Lab and industrial reactor configurations are simulated to assess the capability and the accuracy of the method by using the oxidative coupling of methane as a showcase. A good agreement with lab-scale experimental data (deviations below 10%) is obtained. Moreover, in this specific case, the proposed framework provides a 4-fold reduction of the computational cost required to reach the steady-state when compared to the approach of linearizing the chemical source term. As a whole, the work paves the way to the incorporation of detailed kinetics in the simulation of industrial fluidized reactors.
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Affiliation(s)
- Daniele Micale
- Laboratory of Catalysis and Catalytic Processes, Dipartimento di Energia, Politecnico di Milano, via La Masa 34, 20156 Milano, Italy
| | - Riccardo Uglietti
- Laboratory of Catalysis and Catalytic Processes, Dipartimento di Energia, Politecnico di Milano, via La Masa 34, 20156 Milano, Italy
| | - Mauro Bracconi
- Laboratory of Catalysis and Catalytic Processes, Dipartimento di Energia, Politecnico di Milano, via La Masa 34, 20156 Milano, Italy
| | - Matteo Maestri
- Laboratory of Catalysis and Catalytic Processes, Dipartimento di Energia, Politecnico di Milano, via La Masa 34, 20156 Milano, Italy
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9
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Ouyang B, Zhu L, Luo Z. Data‐driven modeling of mesoscale solids stress closures for filtered two‐fluid model in gas–particle flows. AIChE J 2021. [DOI: 10.1002/aic.17290] [Citation(s) in RCA: 9] [Impact Index Per Article: 3.0] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 01/03/2023]
Affiliation(s)
- Bo Ouyang
- Department of Chemical Engineering, School of Chemistry and Chemical Engineering, State Key Laboratory of Metal Matrix Composites Shanghai Jiao Tong University Shanghai PR China
| | - Li‐Tao Zhu
- Department of Chemical Engineering, School of Chemistry and Chemical Engineering, State Key Laboratory of Metal Matrix Composites Shanghai Jiao Tong University Shanghai PR China
| | - Zheng‐Hong Luo
- Department of Chemical Engineering, School of Chemistry and Chemical Engineering, State Key Laboratory of Metal Matrix Composites Shanghai Jiao Tong University Shanghai PR China
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10
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Li JS, Zhu LT, Yan WC, Rashid TAB, Xu QJ, Luo ZH. Coarse-grid simulations of full-loop gas-solid flows using a hybrid drag model: Investigations on turbulence models. POWDER TECHNOL 2021. [DOI: 10.1016/j.powtec.2020.10.052] [Citation(s) in RCA: 13] [Impact Index Per Article: 4.3] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 11/16/2022]
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11
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Analysis and development of homogeneous drag closure for filtered mesoscale modeling of fluidized gas-particle flows. Chem Eng Sci 2021. [DOI: 10.1016/j.ces.2020.116147] [Citation(s) in RCA: 13] [Impact Index Per Article: 4.3] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 01/03/2023]
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12
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Xie L, Zhu J, Jiang C. Quantitative study of mixing/segregation behaviors of binary-mixture particles in pilot-scale fluidized bed reactor. POWDER TECHNOL 2021. [DOI: 10.1016/j.powtec.2020.08.069] [Citation(s) in RCA: 11] [Impact Index Per Article: 3.7] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 11/26/2022]
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13
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Numerical exploration of hydrodynamic features in a methanol-to-olefins fluidized bed reactor with two parallel reaction zones. POWDER TECHNOL 2020. [DOI: 10.1016/j.powtec.2020.06.010] [Citation(s) in RCA: 6] [Impact Index Per Article: 1.5] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 11/19/2022]
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14
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Comparative analysis of numerically derived drag models for development of bed expansion ratio correlation in a bubbling fluidized bed. ADV POWDER TECHNOL 2020. [DOI: 10.1016/j.apt.2020.04.036] [Citation(s) in RCA: 6] [Impact Index Per Article: 1.5] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 01/03/2023]
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15
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16
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Zhu L, Tang J, Luo Z. Machine learning to assist filtered two‐fluid model development for dense gas–particle flows. AIChE J 2020. [DOI: 10.1002/aic.16973] [Citation(s) in RCA: 45] [Impact Index Per Article: 11.3] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 01/03/2023]
Affiliation(s)
- Li‐Tao Zhu
- Department of Chemical EngineeringSchool of Chemistry and Chemical Engineering, State Key Laboratory of Metal Matrix Composites, Shanghai Jiao Tong University Shanghai China
| | - Jia‐Xun Tang
- Department of Computer Science and TechnologySchool of Electronic and Electrical Engineering, Shanghai University of Engineering Science Shanghai China
| | - Zheng‐Hong Luo
- Department of Chemical EngineeringSchool of Chemistry and Chemical Engineering, State Key Laboratory of Metal Matrix Composites, Shanghai Jiao Tong University Shanghai China
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17
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Yang S, Wang S. Shape Effect of the Riser Cross Section on the Full-Loop Hydrodynamics of a Three-Dimensional Circulating Fluidized Bed. ACS OMEGA 2020; 5:5784-5795. [PMID: 32226858 PMCID: PMC7097897 DOI: 10.1021/acsomega.9b03903] [Citation(s) in RCA: 1] [Impact Index Per Article: 0.3] [Reference Citation Analysis] [Abstract] [Track Full Text] [Subscribe] [Scholar Register] [Received: 11/15/2019] [Accepted: 03/02/2020] [Indexed: 05/12/2023]
Abstract
In this work, numerical simulation is carried out in a three-dimensional full-loop pilot-scale circulating fluidized bed to explore the shape effect of the riser cross section on the typical flow characteristics of the bed via the multiphase particle-in-cell (MP-PIC) method. The gas and solid phases are modeled with the large eddy simulation and Newton's law of motion in the Eulerian and Lagrangian frameworks, respectively. The proposed model has been well validated with experimental data, followed by evaluating the typical core-annulus structure and the nonuniformity of the solid phase distributed along the radial and axial directions of the riser. Then, the particle-scale information of the solid phase distributed in different parts of the system is explored. The results demonstrate that (i) the square riser gives rise to a higher solid inventory in the standpipe owing to the stronger circulation intensity; (ii) the thickness of the solid back-mixing layer reduces along the riser height; the solid back-mixing tends to concentrate in the four corners, while it is not obvious near the sidewalls of the square riser; and (iii) nonuniform distribution of the particle-scale information of the solid phase (e.g., mass, flux, drag force, and slip velocity) can be observed. The square riser gives rise to comparatively more uniform axial mass distribution, a larger rising solid flux, larger horizontal transportation velocity between the core and annulus regions, and a larger horizontal dispersion coefficient in the riser, as compared with the corresponding ones in the circular riser.
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Affiliation(s)
- Shiliang Yang
- State Key Laboratory of Complex Nonferrous Metal Resources Clean Utilization, Kunming University of Science and Technology, Kunming 650093, P. R. China
| | - Shuai Wang
- School of Chemical Engineering, University of New South Wales, Sydney, NSW 2052, Australia
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18
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Zhu LT, Yang YN, Pan DT, Luo ZH. Capability assessment of coarse-grid simulation of gas-particle riser flow using sub-grid drag closures. Chem Eng Sci 2020. [DOI: 10.1016/j.ces.2019.115410] [Citation(s) in RCA: 18] [Impact Index Per Article: 4.5] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 01/03/2023]
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19
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Effect of granular properties on hydrodynamics in coarse-grid riser flow simulation of Geldart A and B particles. POWDER TECHNOL 2020. [DOI: 10.1016/j.powtec.2019.09.060] [Citation(s) in RCA: 8] [Impact Index Per Article: 2.0] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 11/21/2022]
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20
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A material-property-dependent sub-grid drag model for coarse-grained simulation of 3D large-scale CFB risers. Chem Eng Sci 2019. [DOI: 10.1016/j.ces.2019.04.026] [Citation(s) in RCA: 45] [Impact Index Per Article: 9.0] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 11/18/2022]
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21
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Two- and three-dimensional hydrodynamic modeling of a pseudo-2D turbulent fluidized bed with Geldart B particle. POWDER TECHNOL 2019. [DOI: 10.1016/j.powtec.2019.04.028] [Citation(s) in RCA: 14] [Impact Index Per Article: 2.8] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 11/21/2022]
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22
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Zhu LT, Rashid TAB, Luo ZH. Comprehensive validation analysis of sub-grid drag and wall corrections for coarse-grid two-fluid modeling. Chem Eng Sci 2019. [DOI: 10.1016/j.ces.2018.11.026] [Citation(s) in RCA: 17] [Impact Index Per Article: 3.4] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 11/17/2022]
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23
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Lu B, Niu Y, Chen F, Ahmad N, Wang W, Li J. Energy-minimization multiscale based mesoscale modeling and applications in gas-fluidized catalytic reactors. REV CHEM ENG 2019. [DOI: 10.1515/revce-2017-0023] [Citation(s) in RCA: 19] [Impact Index Per Article: 3.8] [Reference Citation Analysis] [Abstract] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 11/15/2022]
Abstract
Abstract
Gas-solid fluidization is intrinsically dynamic and manifests mesoscale structures spanning a wide range of length and timescales. When involved with reactions, more complex phenomena emerge and thus pose bigger challenges for modeling. As the mesoscale is critical to understand multiphase reactive flows, which the conventional two-fluid model without mesoscale modeling may be inadequate to resolve even using extremely fine grids, this review attempts to demonstrate that the energy-minimization multiscale (EMMS) model could be a starting point to develop such mesoscale modeling. Then, the EMMS-based mesoscale modeling with emphasis on formulation of drag coefficients for different fluidization regimes, modification of mass transfer coefficient, and other extensions are discussed in an attempt to resolve the emerging challenges. Its applications with examples of development of novel fluid catalytic cracking and methanol-to-olefins processes prove that the mesoscale modeling plays a remarkable role in improving the predictions in hydrodynamic behaviors and overall reaction rate. However, the product content primarily depends on the chemical kinetic model itself, suggesting the necessity of an effective coupling between chemical kinetics and flow characteristics. The mesoscale modeling can be believed to accelerate the traditional experimental-based scale-up process with much lower cost in the future.
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Affiliation(s)
- Bona Lu
- State Key Laboratory of Multiphase Complex Systems, Institute of Process Engineering , Chinese Academy of Sciences , Beijing 100190 , China
- Dalian National Laboratory for Clean Energy , Dalian 116023 , China
| | - Yan Niu
- State Key Laboratory of Multiphase Complex Systems, Institute of Process Engineering , Chinese Academy of Sciences , Beijing 100190 , China
- Sino-Danish College , University of Chinese Academy of Sciences , Beijing 100049 , China
| | - Feiguo Chen
- State Key Laboratory of Multiphase Complex Systems, Institute of Process Engineering , Chinese Academy of Sciences , Beijing 100190 , China
| | - Nouman Ahmad
- State Key Laboratory of Multiphase Complex Systems, Institute of Process Engineering , Chinese Academy of Sciences , Beijing 100190 , China
- University of Chinese Academy of Sciences , Beijing 100049 , China
| | - Wei Wang
- State Key Laboratory of Multiphase Complex Systems, Institute of Process Engineering , Chinese Academy of Sciences , Beijing 100190 , China
- Sino-Danish College , University of Chinese Academy of Sciences , Beijing 100049 , China
| | - Jinghai Li
- State Key Laboratory of Multiphase Complex Systems, Institute of Process Engineering , Chinese Academy of Sciences , Beijing 100190 , China
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24
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Zhu LT, Liu YX, Luo ZH. An effective three-marker drag model via sub-grid modeling for turbulent fluidization. Chem Eng Sci 2018. [DOI: 10.1016/j.ces.2018.08.026] [Citation(s) in RCA: 33] [Impact Index Per Article: 5.5] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 10/28/2022]
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25
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CFD-VOF-DPM simulations of bubble rising and coalescence in low hold-up particle-liquid suspension systems. POWDER TECHNOL 2018. [DOI: 10.1016/j.powtec.2018.08.041] [Citation(s) in RCA: 36] [Impact Index Per Article: 6.0] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 11/20/2022]
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26
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Zhu LT, Ma WY, Luo ZH. Influence of distributed pore size and porosity on MTO catalyst particle performance: Modeling and simulation. Chem Eng Res Des 2018. [DOI: 10.1016/j.cherd.2018.07.005] [Citation(s) in RCA: 11] [Impact Index Per Article: 1.8] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 11/24/2022]
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27
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Gao X, Li T, Rogers WA. Assessment of mesoscale solid stress in coarse‐grid TFM simulation of Geldart A particles in all fluidization regimes. AIChE J 2018. [DOI: 10.1002/aic.16341] [Citation(s) in RCA: 30] [Impact Index Per Article: 5.0] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 11/11/2022]
Affiliation(s)
- Xi Gao
- National Energy Technology Laboratory Morgantown WV, 26507
| | - Tingwen Li
- National Energy Technology Laboratory, Morgantown, WV, 26507 and AECOM Morgantown WV, 26505
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28
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Gao X, Li T, Sarkar A, Lu L, Rogers WA. Development and validation of an enhanced filtered drag model for simulating gas-solid fluidization of Geldart A particles in all flow regimes. Chem Eng Sci 2018. [DOI: 10.1016/j.ces.2018.03.038] [Citation(s) in RCA: 98] [Impact Index Per Article: 16.3] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 11/17/2022]
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29
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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: 3.0] [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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30
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Schneiderbauer S. Validation study on spatially averaged two‐fluid model for gas–solid flows: I.
A priori
analysis of wall bounded flows. AIChE J 2018. [DOI: 10.1002/aic.16142] [Citation(s) in RCA: 31] [Impact Index Per Article: 5.2] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 11/09/2022]
Affiliation(s)
- Simon Schneiderbauer
- Christian‐Doppler Laboratory for Multi‐scale Modelling of Multiphase ProcessesJohannes Kepler UniversityAltenbergerstr. 69, Linz Austria
- Dept. of Particulate Flow ModellingJohannes Kepler UniversityAltenbergerstr. 69, Linz Austria
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31
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Zhu LT, Pan H, Su YH, Luo ZH. Effect of Particle Polydispersity on Flow and Reaction Behaviors of Methanol-to-Olefins Fluidized Bed Reactors. Ind Eng Chem Res 2017. [DOI: 10.1021/acs.iecr.6b04026] [Citation(s) in RCA: 12] [Impact Index Per Article: 1.7] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 11/28/2022]
Affiliation(s)
- Li-Tao Zhu
- Department of Chemical Engineering,
College of Chemistry and Chemical Engineering, Shanghai Jiao Tong University, Shanghai 200240, P. R. China
| | - Hui Pan
- Department of Chemical Engineering,
College of Chemistry and Chemical Engineering, Shanghai Jiao Tong University, Shanghai 200240, P. R. China
| | - Yuan-Hai Su
- Department of Chemical Engineering,
College of Chemistry and Chemical Engineering, Shanghai Jiao Tong University, Shanghai 200240, P. R. China
| | - Zheng-Hong Luo
- Department of Chemical Engineering,
College of Chemistry and Chemical Engineering, Shanghai Jiao Tong University, Shanghai 200240, P. R. China
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32
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Jia Z, Zhang C, Cai D, Blair E, Qian W, Wei F. The analysis of hot spots in large scale fluidized bed reactors. RSC Adv 2017. [DOI: 10.1039/c6ra27750k] [Citation(s) in RCA: 2] [Impact Index Per Article: 0.3] [Reference Citation Analysis] [Abstract] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 11/21/2022] Open
Abstract
The fluidized Prater number, βf, is introduced into fluidized beds to estimate the temperature gradient.
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Affiliation(s)
- Zhao Jia
- Department of Chemical Engineering
- Tsinghua University
- Beijing
- China
| | - Chenxi Zhang
- Department of Chemical Engineering
- Tsinghua University
- Beijing
- China
| | - Dali Cai
- Department of Chemical Engineering
- Tsinghua University
- Beijing
- China
| | - Elena Blair
- Department of Chemical Engineering
- Tsinghua University
- Beijing
- China
| | - Weizhong Qian
- Department of Chemical Engineering
- Tsinghua University
- Beijing
- China
| | - Fei Wei
- Department of Chemical Engineering
- Tsinghua University
- Beijing
- China
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33
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34
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Zhu LT, Ye M, Luo ZH. Application of Filtered Model for Reacting Gas–Solid Flows and Optimization in a Large-Scale Methanol-to-Olefin Fluidized-Bed Reactor. Ind Eng Chem Res 2016. [DOI: 10.1021/acs.iecr.6b02819] [Citation(s) in RCA: 37] [Impact Index Per Article: 4.6] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 11/28/2022]
Affiliation(s)
- Li-Tao Zhu
- Department
of Chemical Engineering, College of Chemistry and Chemical Engineering, Shanghai Jiao Tong University, Shanghai 200240, People’s Republic of China
| | - Mao Ye
- Dalian
National Laboratory for Clean Energy, National Engineering Laboratory
for MTO, Dalian Institute of Chemical Physics, Chinese Academy of Sciences, 457 Zhongshan Road, Dalian 116023, People’s Republic of China
| | - Zheng-Hong Luo
- Department
of Chemical Engineering, College of Chemistry and Chemical Engineering, Shanghai Jiao Tong University, Shanghai 200240, People’s Republic of China
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35
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Computer virtual experiment on fluidized beds using a coarse-grained discrete particle method—EMMS-DPM. Chem Eng Sci 2016. [DOI: 10.1016/j.ces.2016.08.013] [Citation(s) in RCA: 77] [Impact Index Per Article: 9.6] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 11/24/2022]
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36
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