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Experimental validation of multiphase particle-in-cell simulations of fluidization in a bubbling fluidized bed combustor. POWDER TECHNOL 2022. [DOI: 10.1016/j.powtec.2022.118204] [Citation(s) in RCA: 0] [Impact Index Per Article: 0] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 12/29/2022]
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2
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Detailed study of single bubble behavior and drag correlations in Newtonian and non-Newtonian liquids for the design of bubble columns. Chem Eng Res Des 2022. [DOI: 10.1016/j.cherd.2022.01.013] [Citation(s) in RCA: 0] [Impact Index Per Article: 0] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 11/03/2022]
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3
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Jang K, Feng Y, Li H. Investigation of Bubble Behavior in Gas‐Solid Fluidized Beds with Different Gas Distributors. Chem Eng Technol 2021. [DOI: 10.1002/ceat.202000156] [Citation(s) in RCA: 0] [Impact Index Per Article: 0] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 11/11/2022]
Affiliation(s)
- Kwangbyol Jang
- University of Science and Technology Beijing School of Civil & Resource Engineering Xueyuan Road 100083 Beijing China
| | - Yali Feng
- University of Science and Technology Beijing School of Civil & Resource Engineering Xueyuan Road 100083 Beijing China
| | - Haoran Li
- Chinese Academy of Sciences National Key Laboratory of Biochemical Engineering Institute of Process Engineering North Second Street 100080 Beijing China
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4
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Chai X, Lu J, Duan C, Zhou E, Zhao Y, Zhang Y, Gao Z. Investigation on flow pattern evolution and restraint of vibration energy to bubbles in vibrated dense medium fluidized bed. ADV POWDER TECHNOL 2021. [DOI: 10.1016/j.apt.2021.01.019] [Citation(s) in RCA: 1] [Impact Index Per Article: 0.3] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 10/22/2022]
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5
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Atashrouz S, Rahmani M, Nasernejad B, Soares JB. Prediction of Temperature and Concentration Profiles in an Industrial Polymerization Fluidized Bed Reactor under Condensed-Mode Operation. Ind Eng Chem Res 2021. [DOI: 10.1021/acs.iecr.0c04895] [Citation(s) in RCA: 1] [Impact Index Per Article: 0.3] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 11/28/2022]
Affiliation(s)
- Saeid Atashrouz
- Department of Chemical Engineering, Amirkabir University of Technology (Tehran Polytechnic), Mahshahr Campus, Mahshahr, P.O. Box 415, Iran
| | - Mohammad Rahmani
- Department of Chemical Engineering, Amirkabir University of Technology (Tehran Polytechnic), Mahshahr Campus, Mahshahr, P.O. Box 415, Iran
- Department of Chemical Engineering, Amirkabir University of Technology (Tehran Polytechnic), Hafez 424, P.O. Box 15875-4413 Tehran, Iran
| | - Bahram Nasernejad
- Department of Chemical Engineering, Amirkabir University of Technology (Tehran Polytechnic), Hafez 424, P.O. Box 15875-4413 Tehran, Iran
| | - João B.P. Soares
- Department of Chemical and Materials Engineering, University of Alberta, 9211 116 Street, Edmonton, Alberta T6G 1H9, Canada
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Design of a Bubble Reactor for Altitude Simulators Used to Humidify a Combustion Air Stream by Means of CFD Multi-Phase Models. APPLIED SCIENCES-BASEL 2020. [DOI: 10.3390/app11010295] [Citation(s) in RCA: 0] [Impact Index Per Article: 0] [Reference Citation Analysis] [Abstract] [Track Full Text] [Subscribe] [Scholar Register] [Indexed: 11/17/2022]
Abstract
In this paper, a procedure for the design of a bubble reactor which allows the control of the humidity of a gas stream used as combustion air is presented. This reactor is designed to be used as a component of an altitude simulator test facility for the optimization, homologation and calibration of new hybrid engines. The design has been carried out by means of Computational Fluid Dynamics (CFD) multi-phase models and validated against the experimental data obtained from the developed prototype. A discussion about the adequate mesh topology and cell size is presented, as well as a comparison between the two available models for the air–water interphase. Lastly, a validation of the CFD results using experimental data shows that the model that should be used is the multi-regime interaction model, from which the final design for the bubble reactor was obtained.
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Abstract
Drying in fluidized beds is an important step in the production of powdered materials. Especially in the food and pharmaceutical industry, fluidized bed dryers are often vibrated to improve the drying process. In the current work, a continuous fluidized bed drying model is implemented in the novel, open-source flowsheet simulation framework Dyssol. The new model accounts for the hydrodynamic characteristics of all Geldart groups as well as the impact of mechanical vibration on the drying process. Distributed particle properties are considered by the model. Comprehensive validation of the model was conducted for a wide range of process parameters, different materials, dryer geometries and dimensions as well as the impact of vibration. Particle properties are predicted accurately and represent the broad experimental data well. A sensitivity analysis of the model confirmed grid independence and the validity of underlying model assumptions.
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8
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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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9
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Torres Brauer N, Serrano Rosales B, de Lasa H. Single-Bubble Dynamics in a Dense Phase Fluidized Sand Bed Biomass Gasification Environment. Ind Eng Chem Res 2020. [DOI: 10.1021/acs.iecr.9b05674] [Citation(s) in RCA: 4] [Impact Index Per Article: 1.0] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 11/28/2022]
Affiliation(s)
- Nicolas Torres Brauer
- Chemical Reactor Engineering Centre (CREC), Faculty of Engineering Science, Department of Chemical and Biochemical Engineering, Western University, London, Ontario N6A 5B9, Canada
| | - Benito Serrano Rosales
- Unidad Académica de Ciencias Químicas, Programa de Ingeniería Química, Universidad Autónoma de Zacatecas, Campus UAZ Siglo XXI, Zacatecas, Zacatecas 98160, Mexico
| | - Hugo de Lasa
- Chemical Reactor Engineering Centre (CREC), Faculty of Engineering Science, Department of Chemical and Biochemical Engineering, Western University, London, Ontario N6A 5B9, Canada
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Huang K, Meng S, Guo Q, Yang W, Zhang T, Ye M, Liu Z. Effect of Electrode Length of an Electrical Capacitance Tomography Sensor on Gas−Solid Fluidized Bed Measurements. Ind Eng Chem Res 2019. [DOI: 10.1021/acs.iecr.9b03988] [Citation(s) in RCA: 3] [Impact Index Per Article: 0.6] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 11/28/2022]
Affiliation(s)
- Kai Huang
- Dalian National Laboratory for Clean Energy and National Engineering Laboratory for MTO, Dalian Institute of Chemical Physics, Chinese Academy of Sciences, Dalian 116023, Liaoning, China
- University of Chinese Academy of Sciences, Beijing 100049, Beijing, China
| | - Shuanghe Meng
- Dalian National Laboratory for Clean Energy and National Engineering Laboratory for MTO, Dalian Institute of Chemical Physics, Chinese Academy of Sciences, Dalian 116023, Liaoning, China
| | - Qiang Guo
- Dalian National Laboratory for Clean Energy and National Engineering Laboratory for MTO, Dalian Institute of Chemical Physics, Chinese Academy of Sciences, Dalian 116023, Liaoning, China
- University of Chinese Academy of Sciences, Beijing 100049, Beijing, China
| | - Wuqiang Yang
- School of Electrical and Electronic Engineering, The University of Manchester, Manchester M13 9PL, Lancashire, U.K
| | - Tao Zhang
- Dalian National Laboratory for Clean Energy and National Engineering Laboratory for MTO, Dalian Institute of Chemical Physics, Chinese Academy of Sciences, Dalian 116023, Liaoning, China
| | - Mao Ye
- Dalian National Laboratory for Clean Energy and National Engineering Laboratory for MTO, Dalian Institute of Chemical Physics, Chinese Academy of Sciences, Dalian 116023, Liaoning, China
| | - Zhongmin Liu
- Dalian National Laboratory for Clean Energy and National Engineering Laboratory for MTO, Dalian Institute of Chemical Physics, Chinese Academy of Sciences, Dalian 116023, Liaoning, China
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Agu CE, Ugwu A, Pfeifer C, Eikeland M, Tokheim LA, Moldestad BME. Investigation of Bubbling Behavior in Deep Fluidized Beds at Different Gas Velocities using Electrical Capacitance Tomography. Ind Eng Chem Res 2019. [DOI: 10.1021/acs.iecr.8b05013] [Citation(s) in RCA: 9] [Impact Index Per Article: 1.8] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 11/29/2022]
Affiliation(s)
- Cornelius E. Agu
- Department of Process, Energy and Environmental Technology, University College of Southeast Norway, 3918 Porsgrunn, Norway
| | - Ambrose Ugwu
- Department of Energy and Process Engineering, Norwegian University of Science and Technology, 7491 Trondheim, Norway
| | - Christoph Pfeifer
- Department of Material Sciences and Process Engineering, University of Natural Resources and Life Sciences, 1190 Vienna, Austria
| | - Marianne Eikeland
- Department of Process, Energy and Environmental Technology, University College of Southeast Norway, 3918 Porsgrunn, Norway
| | - Lars-Andre Tokheim
- Department of Process, Energy and Environmental Technology, University College of Southeast Norway, 3918 Porsgrunn, Norway
| | - Britt M. E. Moldestad
- Department of Process, Energy and Environmental Technology, University College of Southeast Norway, 3918 Porsgrunn, Norway
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