1
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Du C, Han C, Yang Z, Wu H, Luo H, Niedzwiecki L, Lu B, Wang W. Multiscale CFD Simulation of an Industrial Diameter-Transformed Fluidized Bed Reactor with Artificial Neural Network Analysis of EMMS Drag Markers. Ind Eng Chem Res 2022. [DOI: 10.1021/acs.iecr.2c00396] [Citation(s) in RCA: 1] [Impact Index Per Article: 0.5] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 11/29/2022]
Affiliation(s)
- Chengzhe Du
- 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
| | - Caixia Han
- 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
| | - Zhuo Yang
- 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
| | - Hao Wu
- University of Chinese Academy of Sciences, Beijing 100049, China
- Department of Chemical and Biochemical Engineering, Technical University of Denmark, 2800 Kongens Lyngby, Denmark
| | - Hao Luo
- School of Chemistry and Chemical Engineering, Wuhan University of Science and Technology, Wuhan, Hubei 430081, China
| | - Lukasz Niedzwiecki
- Department of Mechanics, Machines, Devices and Energy Processes, Wrocław University of Science and Technology, Wrocław 50-370, Poland
| | - Bona Lu
- 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
- University of Chinese Academy of Sciences, Beijing 100049, China
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2
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Benzarti S, Mhiri H, Bournot P. Entrance effects on gas-solid hydrodynamics of turbulent fluidized beds filled with Geldart B particles. POWDER TECHNOL 2022. [DOI: 10.1016/j.powtec.2022.117337] [Citation(s) in RCA: 1] [Impact Index Per Article: 0.5] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 11/30/2022]
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3
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Effects of drag and subgrid-scale turbulence modeling on gas–solid hydrodynamics of a pilot-scale circulating fluidized bed. Chem Eng Sci 2022. [DOI: 10.1016/j.ces.2021.117093] [Citation(s) in RCA: 1] [Impact Index Per Article: 0.5] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 11/20/2022]
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4
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Tu Q, Wang H, Ocone R. Application of three-dimensional full-loop CFD simulation in circulating fluidized bed combustion reactors – A review. POWDER TECHNOL 2022. [DOI: 10.1016/j.powtec.2022.117181] [Citation(s) in RCA: 1] [Impact Index Per Article: 0.5] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 10/19/2022]
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5
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Numerical exploration of the flow regime transition of a novel catalytic cracking reactor and operation mode analysis. POWDER TECHNOL 2022. [DOI: 10.1016/j.powtec.2022.117137] [Citation(s) in RCA: 2] [Impact Index Per Article: 1.0] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 11/17/2022]
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6
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Gas-solid-liquid reactive CFD simulation of an industrial RFCC riser with investigation of feed injection. Chem Eng Sci 2021. [DOI: 10.1016/j.ces.2021.116740] [Citation(s) in RCA: 6] [Impact Index Per Article: 2.0] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 11/20/2022]
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7
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Zhao B, Wang J. Statistical foundation of EMMS-based two-fluid models for heterogeneous gas-solid flow. Chem Eng Sci 2021. [DOI: 10.1016/j.ces.2021.116678] [Citation(s) in RCA: 2] [Impact Index Per Article: 0.7] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 11/29/2022]
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8
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Li S, Shen Y. CFD study of nonuniformity of gas-solid flow through a chemical looping combustion system with symmetrical series loops. POWDER TECHNOL 2021. [DOI: 10.1016/j.powtec.2021.04.008] [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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9
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Guo Q, Padash A, Boyce CM. A two fluid modeling study of bubble collapse due to bubble interaction in a fluidized bed. Chem Eng Sci 2021. [DOI: 10.1016/j.ces.2020.116377] [Citation(s) in RCA: 5] [Impact Index Per Article: 1.7] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 10/22/2022]
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10
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Predicting cold gas-solid flow in a pilot-scale dual-circulating fluidized bed: Validation of computational particle fluid dynamics model. POWDER TECHNOL 2021. [DOI: 10.1016/j.powtec.2020.11.070] [Citation(s) in RCA: 9] [Impact Index Per Article: 3.0] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 11/19/2022]
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11
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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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12
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Lungu M, Siame J, Mukosha L. Comparison of CFD-DEM and TFM approaches for the simulation of the small scale challenge problem 1. POWDER TECHNOL 2021. [DOI: 10.1016/j.powtec.2020.09.071] [Citation(s) in RCA: 19] [Impact Index Per Article: 6.3] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 11/28/2022]
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13
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Liu Y, Huo P, Li X, Qi H. Numerical analysis of the operating characteristics of a large‐scale
CFB
coal‐gasification reactor with the
QC‐EMMS
drag model. CAN J CHEM ENG 2020. [DOI: 10.1002/cjce.23911] [Citation(s) in RCA: 1] [Impact Index Per Article: 0.3] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 11/08/2022]
Affiliation(s)
- Yang Liu
- Key Laboratory for Thermal Science & Power Engineering of Ministry of Education, Tsinghua University Beijing China
| | - Pengju Huo
- Hydrocarbon High‐efficiency Utilization Technology Research Center, Shaanxi Yanchang Petroleum Co. Ltd. Xi'an China
| | - Xiaohong Li
- Hydrocarbon High‐efficiency Utilization Technology Research Center, Shaanxi Yanchang Petroleum Co. Ltd. Xi'an China
| | - Haiying Qi
- Key Laboratory for Thermal Science & Power Engineering of Ministry of Education, Tsinghua University Beijing China
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14
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Cui Y, Zhong W, Liu X, Xiang J. Gas–Solid Hydrodynamics and Combustion Characteristics in a 600 MW Annular CFB Boiler for Supercritical CO 2 Cycles. Ind Eng Chem Res 2020. [DOI: 10.1021/acs.iecr.0c04131] [Citation(s) in RCA: 6] [Impact Index Per Article: 1.5] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 11/28/2022]
Affiliation(s)
- Ying Cui
- Key Laboratory of Energy Conversion and Process Measurement and Control, Ministry of Education, School of Energy and Environment, Southeast University, Xuanwu District, Nanjing, Jiangsu 210096, P. R. China
| | - Wenqi Zhong
- Key Laboratory of Energy Conversion and Process Measurement and Control, Ministry of Education, School of Energy and Environment, Southeast University, Xuanwu District, Nanjing, Jiangsu 210096, P. R. China
| | - Xuejiao Liu
- Key Laboratory of Energy Conversion and Process Measurement and Control, Ministry of Education, School of Energy and Environment, Southeast University, Xuanwu District, Nanjing, Jiangsu 210096, P. R. China
| | - Jun Xiang
- State Key Laboratory of Coal Combustion, Huazhong University of Science and Technology, Wuhan 430074, P. R. China
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15
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Hu S, Liu X. Development of a hydrodynamic model and the corresponding virtual software for dual-loop circulating fluidized beds. Front Chem Sci Eng 2020. [DOI: 10.1007/s11705-020-1953-6] [Citation(s) in RCA: 2] [Impact Index Per Article: 0.5] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 10/23/2022]
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16
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17
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Zhang H, Li W, Ma Q, Zhang Y, Lei F. Numerical study on influence of exit geometry in gas–solid flow hydrodynamics of HDCFB riser by CPFD. ADV POWDER TECHNOL 2020. [DOI: 10.1016/j.apt.2020.08.006] [Citation(s) in RCA: 8] [Impact Index Per Article: 2.0] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 12/01/2022]
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18
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Li S, Shen Y. Multi-fluid modelling of hydrodynamics in a dual circulating fluidized bed. ADV POWDER TECHNOL 2020. [DOI: 10.1016/j.apt.2020.05.010] [Citation(s) in RCA: 11] [Impact Index Per Article: 2.8] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 11/28/2022]
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19
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CFD-DEM coupled with thermochemical sub-models for biomass gasification: Validation and sensitivity analysis. Chem Eng Sci 2020. [DOI: 10.1016/j.ces.2020.115550] [Citation(s) in RCA: 64] [Impact Index Per Article: 16.0] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 11/18/2022]
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20
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21
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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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22
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Sharma V, Agarwal VK. Effect of process parameters on circulating fluidized bed coal gasification using 3D full‐loop CFD simulation. CAN J CHEM ENG 2020. [DOI: 10.1002/cjce.23733] [Citation(s) in RCA: 4] [Impact Index Per Article: 1.0] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 11/10/2022]
Affiliation(s)
- Vikrant Sharma
- Department of Chemical EngineeringIndian Institute of Technology Roorkee Roorkee India
| | - Vijay K. Agarwal
- Department of Chemical EngineeringIndian Institute of Technology Roorkee Roorkee India
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23
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Yang Y, Xu J, Liu Z, Guo Q, Ye M, Wang G, Gao J, Wang J, Shu Z, Ge W, Liu Z, Wang F, Li YW. Progress in coal chemical technologies of China. REV CHEM ENG 2019. [DOI: 10.1515/revce-2017-0026] [Citation(s) in RCA: 26] [Impact Index Per Article: 5.2] [Reference Citation Analysis] [Abstract] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 11/15/2022]
Abstract
Abstract
China’s unique energy reserve structure abundant in coal and scarce in crude oil and natural gas has promoted heavy investment on the research and development of clean coal chemical technologies during last two decades, which has turned China into a heartland for demonstrating, developing, and commercializing virtually every aspect of new coal chemical process technologies. Consequently, breakthroughs in coal gasification, indirect and direct coal-to-liquid (CTL) processes, and methanol-to-olefins (MTO) technologies are catching attention worldwide. Gasification technology for syngas production is the key to high plant availability and economic success for most coal chemical projects. During the past 20 years, both international and Chinese gasifier vendors have reaped great successes in licensing their technologies in the domestic market. Notably, the local vendors have been investing heavily on inventing and improving their technologies to suit the specific requirement of gasifying a variety of coals. The opposed multinozzle gasification technology from East China University of Science and Technology was taken as an example to demonstrate the recent development in this field. The coal chemical industry in China has witnessed several notable achievements in chemical engineering progress, namely CTL (indirect and direct) and MTO. Comprehensive reviews on topics such as catalysis, kinetics, and reactor design and process integration will be provided by leading scientists in related fields with firsthand information to showcase the contributions of Chinese researchers to chemical engineering science and technology.
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24
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Sharma V, Agarwal VK. Three-Dimensional Full-Loop Hydrodynamic Simulation of a Circulating Fluidized-Bed Gasifier: A Quantitative Assessment of Drag Models. ARABIAN JOURNAL FOR SCIENCE AND ENGINEERING 2019. [DOI: 10.1007/s13369-019-04040-0] [Citation(s) in RCA: 0] [Impact Index Per Article: 0] [Reference Citation Analysis] [Track Full Text] [Subscribe] [Scholar Register] [Indexed: 11/28/2022]
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25
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An EMMS drag model for coarse grid simulation of polydisperse gas–solid flow in circulating fluidized bed risers. Chem Eng Sci 2019. [DOI: 10.1016/j.ces.2019.06.037] [Citation(s) in RCA: 26] [Impact Index Per Article: 5.2] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 11/18/2022]
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26
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27
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Sharma V, Agarwal VK. NUMERICAL SIMULATION OF COAL GASIFICATION IN A CIRCULATING FLUIDIZED BED GASIFIER. BRAZILIAN JOURNAL OF CHEMICAL ENGINEERING 2019. [DOI: 10.1590/0104-6632.20190363s20180423] [Citation(s) in RCA: 3] [Impact Index Per Article: 0.6] [Reference Citation Analysis] [Track Full Text] [Subscribe] [Scholar Register] [Indexed: 11/22/2022]
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28
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Ahmad N, Tong Y, Lu B, Wang W. Extending the EMMS-bubbling model to fluidization of binary particle mixture: Parameter analysis and model validation. Chem Eng Sci 2019. [DOI: 10.1016/j.ces.2019.02.016] [Citation(s) in RCA: 16] [Impact Index Per Article: 3.2] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 11/27/2022]
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29
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30
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CFD-DEM study of the effect of ring baffles on system performance of a full-loop circulating fluidized bed. Chem Eng Sci 2019. [DOI: 10.1016/j.ces.2018.10.056] [Citation(s) in RCA: 21] [Impact Index Per Article: 4.2] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 11/23/2022]
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31
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Wang M, Wu Y, Shi X, Lan X, Wang C, Gao J. Full‐Loop Simulation of Gas‐Solids Flow in a Pilot‐Scale Circulating Fluidized Bed. Chem Eng Technol 2019. [DOI: 10.1002/ceat.201800542] [Citation(s) in RCA: 6] [Impact Index Per Article: 1.2] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 11/09/2022]
Affiliation(s)
- Min Wang
- China University of PetroleumState Key Laboratory of Heavy Oil Processing Fuxue Road 18 102249 Beijing China
| | - Yingya Wu
- China University of PetroleumState Key Laboratory of Heavy Oil Processing Fuxue Road 18 102249 Beijing China
| | - Xiaogang Shi
- China University of PetroleumState Key Laboratory of Heavy Oil Processing Fuxue Road 18 102249 Beijing China
| | - Xingying Lan
- China University of PetroleumState Key Laboratory of Heavy Oil Processing Fuxue Road 18 102249 Beijing China
| | - Chengxiu Wang
- China University of PetroleumState Key Laboratory of Heavy Oil Processing Fuxue Road 18 102249 Beijing China
| | - Jinsen Gao
- China University of PetroleumState Key Laboratory of Heavy Oil Processing Fuxue Road 18 102249 Beijing China
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32
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Comparison of solid phase closure models in Eulerian-Eulerian simulations of a circulating fluidized bed riser. Chem Eng Sci 2019. [DOI: 10.1016/j.ces.2018.11.031] [Citation(s) in RCA: 11] [Impact Index Per Article: 2.2] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 11/21/2022]
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33
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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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34
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Ahmad N, Tian Y, Lu B, Hong K, Wang H, Wang W. Extending the EMMS/bubbling model to fluidization of binary particle mixture: Formulation and steady-state validation. Chin J Chem Eng 2019. [DOI: 10.1016/j.cjche.2018.04.011] [Citation(s) in RCA: 7] [Impact Index Per Article: 1.4] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 10/17/2022]
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35
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36
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Lu Y, Zhou Y, Yang L, Hu X, Luo X, Chen H. Verification of optimal models for 2D-full loop simulation of circulating fluidized bed. ADV POWDER TECHNOL 2018. [DOI: 10.1016/j.apt.2018.07.024] [Citation(s) in RCA: 10] [Impact Index Per Article: 1.7] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 10/28/2022]
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37
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Ma Q, Lei F, Xiao Y. Numerical analysis of operating conditions for establishing high-density circulating fluidized bed by CPFD method. POWDER TECHNOL 2018. [DOI: 10.1016/j.powtec.2018.07.012] [Citation(s) in RCA: 16] [Impact Index Per Article: 2.7] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 11/25/2022]
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38
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Xu Y, Musser J, Li T, Gopalan B, Panday R, Tucker J, Breault G, Clarke MA, Rogers WA. Numerical Simulation and Experimental Study of the Gas–Solid Flow Behavior Inside a Full-Loop Circulating Fluidized Bed: Evaluation of Different Drag Models. Ind Eng Chem Res 2018. [DOI: 10.1021/acs.iecr.7b03817] [Citation(s) in RCA: 45] [Impact Index Per Article: 7.5] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 11/29/2022]
Affiliation(s)
- Yupeng Xu
- National Energy Technology Laboratory, Morgantown, West Virginia 26505, United States
| | - Jordan Musser
- National Energy Technology Laboratory, Morgantown, West Virginia 26505, United States
| | - Tingwen Li
- National Energy Technology Laboratory, Morgantown, West Virginia 26505, United States
- AECOM, Morgantown, West Virginia 26505, United States
| | - Balaji Gopalan
- National Energy Technology Laboratory, Morgantown, West Virginia 26505, United States
- West Virginia University Research Corporation, Morgantown, West Virginia 26506, United States
| | - Rupen Panday
- National Energy Technology Laboratory, Morgantown, West Virginia 26505, United States
- REM Engineering Services, Morgantown, West Virginia 26506, United States
| | - Jonathan Tucker
- National Energy Technology Laboratory, Morgantown, West Virginia 26505, United States
- West Virginia University, Morgantown, West Virginia 26506, United States
| | - Greggory Breault
- National Energy Technology Laboratory, Morgantown, West Virginia 26505, United States
- REM Engineering Services, Morgantown, West Virginia 26506, United States
| | - Mary Ann Clarke
- National Energy Technology Laboratory, Morgantown, West Virginia 26505, United States
- West Virginia University Research Corporation, Morgantown, West Virginia 26506, United States
| | - William A. Rogers
- National Energy Technology Laboratory, Morgantown, West Virginia 26505, United States
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39
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CPFD study of a full-loop three-dimensional pilot-scale circulating fluidized bed based on EMMS drag model. POWDER TECHNOL 2018. [DOI: 10.1016/j.powtec.2017.09.045] [Citation(s) in RCA: 46] [Impact Index Per Article: 7.7] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 11/21/2022]
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40
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Lu B, Zhang J, Luo H, Wang W, Li H, Ye M, Liu Z, Li J. Numerical simulation of scale-up effects of methanol-to-olefins fluidized bed reactors. Chem Eng Sci 2017. [DOI: 10.1016/j.ces.2017.05.007] [Citation(s) in RCA: 37] [Impact Index Per Article: 5.3] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 10/19/2022]
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41
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Syamlal M, Celik IB, Benyahia S. Quantifying the uncertainty introduced by discretization and time-averaging in two-fluid model predictions. AIChE J 2017. [DOI: 10.1002/aic.15868] [Citation(s) in RCA: 7] [Impact Index Per Article: 1.0] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 11/05/2022]
Affiliation(s)
- Madhava Syamlal
- Science & Technology Strategic Plans & Programs, National Energy Technology Laboratory; Morgantown WV 26507
| | - Ismail B. Celik
- Research & Innovation Center, National Energy Technology Laboratory; Morgantown WV 26507
- Mechanical and Aerospace Engineering, West Virginia University; Morgantown WV 26506
| | - Sofiane Benyahia
- Research & Innovation Center, National Energy Technology Laboratory; Morgantown WV 26507
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42
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43
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Cahyadi A, Anantharaman A, Yang S, Karri SR, Findlay JG, Cocco RA, Chew JW. Review of cluster characteristics in circulating fluidized bed (CFB) risers. Chem Eng Sci 2017. [DOI: 10.1016/j.ces.2016.10.002] [Citation(s) in RCA: 74] [Impact Index Per Article: 10.6] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 11/26/2022]
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44
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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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45
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Luo K, Wang S, Yang S, Hu C, Fan J. Computational Fluid Dynamics–Discrete Element Method Investigation of Pressure Signals and Solid Back-Mixing in a Full-Loop Circulating Fluidized Bed. Ind Eng Chem Res 2017. [DOI: 10.1021/acs.iecr.6b04047] [Citation(s) in RCA: 26] [Impact Index Per Article: 3.7] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 11/30/2022]
Affiliation(s)
- Kun Luo
- State Key Laboratory of Clean
Energy Utilization, Zhejiang University, Hangzhou 310027, PR China
| | - Shuai Wang
- State Key Laboratory of Clean
Energy Utilization, Zhejiang University, Hangzhou 310027, PR China
| | - Shiliang Yang
- State Key Laboratory of Clean
Energy Utilization, Zhejiang University, Hangzhou 310027, PR China
| | - Chenshu Hu
- State Key Laboratory of Clean
Energy Utilization, Zhejiang University, Hangzhou 310027, PR China
| | - Jianren Fan
- State Key Laboratory of Clean
Energy Utilization, Zhejiang University, Hangzhou 310027, PR China
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46
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Yao X, Zhang Y, Lu C, Wen D. CFD investigation of gas-solids flow in a new fluidized catalyst cooler. POWDER TECHNOL 2016. [DOI: 10.1016/j.powtec.2016.08.022] [Citation(s) in RCA: 2] [Impact Index Per Article: 0.3] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 11/17/2022]
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47
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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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48
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Lu B, Luo H, Li H, Wang W, Ye M, Liu Z, Li J. Speeding up CFD simulation of fluidized bed reactor for MTO by coupling CRE model. Chem Eng Sci 2016. [DOI: 10.1016/j.ces.2016.01.010] [Citation(s) in RCA: 30] [Impact Index Per Article: 3.8] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 10/22/2022]
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49
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Liu C, Zhao M, Wang W, Li J. 3D CFD simulation of a circulating fluidized bed with on-line adjustment of mechanical valve. Chem Eng Sci 2015. [DOI: 10.1016/j.ces.2015.07.006] [Citation(s) in RCA: 13] [Impact Index Per Article: 1.4] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 11/30/2022]
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50
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Zhong H, Lan X, Gao J, Zheng Y, Zhang Z. The difference between specularity coefficient of 1 and no-slip solid phase wall boundary conditions in CFD simulation of gas–solid fluidized beds. POWDER TECHNOL 2015. [DOI: 10.1016/j.powtec.2015.08.055] [Citation(s) in RCA: 15] [Impact Index Per Article: 1.7] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 10/23/2022]
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