1
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Yao Y, Liu Z, Zheng G, Tao C, Wang Y, Xi B. Intensification of Solid–Liquid Suspension Performance in an Elliptical Uncovered Unbaffled Stirred Tank. Ind Eng Chem Res 2023. [DOI: 10.1021/acs.iecr.2c03923] [Citation(s) in RCA: 0] [Impact Index Per Article: 0] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 03/18/2023]
Affiliation(s)
- Yuan Yao
- School of Chemistry and Chemical Engineering, Chongqing University, Chongqing 401331, China
| | - Zuohua Liu
- School of Chemistry and Chemical Engineering, Chongqing University, Chongqing 401331, China
| | - Guocan Zheng
- School of Chemistry and Chemical Engineering, Chongqing University, Chongqing 401331, China
| | - Changyuan Tao
- School of Chemistry and Chemical Engineering, Chongqing University, Chongqing 401331, China
| | - Yundong Wang
- Department of Chemical Engineering, Tsinghua University, Beijing 100084, China
| | - Benjun Xi
- Hubei Three Gorges Laboratory, Yichang 443007, China
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2
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Posadas-Navarro DI, Gonza´lez-Rivera C, Ram´ırez-Arga´ez MA, Ascanio G. Power Characteristics and Mass Transfer of Rotor Injectors in a Water Physical Model of an Aluminum Degassing Ladle. Chem Eng Res Des 2023. [DOI: 10.1016/j.cherd.2023.01.040] [Citation(s) in RCA: 0] [Impact Index Per Article: 0] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 01/22/2023]
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3
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Computational Fluid Dynamics Study of a Pharmaceutical Full-Scale Hydrogenation Reactor. Processes (Basel) 2022. [DOI: 10.3390/pr10061163] [Citation(s) in RCA: 0] [Impact Index Per Article: 0] [Reference Citation Analysis] [Abstract] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 11/16/2022] Open
Abstract
The pharmaceutical industry has been quite successful in developing new hydrogenation processes, and the chemistry of hydrogenation is currently well understood. However, it is a complex process to scale and optimize due to its high exothermicity, use of expensive catalysts and solvents, and its mass transfer requirements. Therefore, the aim of this work is to develop a CFD model to be able to describe the mass transfer, hydrodynamics, and mixing with respect to changes in rotational speed for a full-scale pharmaceutical hydrogenation reactor. In the first stage, a simple CFD model is used to predict the development of the surface vortex, and it is validated against literature data. In the second stage, the CFD model is tested on a full-scale configuration equipped with a Rushton turbine and a bottom kicker to study the formation of the surface vortex. Simulation results show the ability to predict the development of the surface vortex. These results are used to estimate the liquid height and mixing time as a function of several rotational speeds, allowing us to propose novel process correlations for this particular configuration. Although modelling the complete hydrogenation process would be challenging, this work is seen as a first step towards developing models that demonstrate the use of CFD at such large reactor scales.
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4
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Wang P, Cao H, Wang F, Zheng Y, Liu R, Dong H, Zhang X, Wang X. Suspended particles behavior in aqueous [Bmim]BF4 solution by novel on-line electrical sensing zone method. Chem Eng Sci 2022. [DOI: 10.1016/j.ces.2021.117280] [Citation(s) in RCA: 0] [Impact Index Per Article: 0] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 11/30/2022]
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5
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Młynarczykowska A, Ferrari S, Demurtas L, Jaszczur M. Impact of baffle geometry on the fluid motion in the stirred vessel. EPJ WEB OF CONFERENCES 2022. [DOI: 10.1051/epjconf/202226901039] [Citation(s) in RCA: 0] [Impact Index Per Article: 0] [Reference Citation Analysis] [Abstract] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 11/07/2022] Open
Abstract
The fluids mixing is a crucial operation in a large number of engineering systems. It has major significance in chemical engineering, food, cosmetics and pharmaceutics production, biotechnology, wastewater treatment engineering, and countless other applications. Among many available systems online mixing with static mixers and stirred tanks plays a primary role and has been developed to meet several processing objectives. The effectiveness of the mixing process depends on a number of parameters, i.e. impeller shape, mixing phases properties, process conditions as well as stirred vessel design - in particular, number and baffles’ design. The optimal baffles geometry is still an open issue and is usually design with trial and error methods. In this study, the focus is on the experimental investigations of the baffle geometry on the fluid flow and mixing phenomenon as well as on the required by the mixer power. In order to evaluate velocity field and mixing parameters, particle image velocimetry measurement is used whereas to obtain the power consumption by the stirred vessel precise torque meters were used. Measurements are carried out for different Reynolds numbers, to determine the most efficient process parameters. It has been shown that for the analyzed range of Reynolds numbers, the baffles design significantly influences fluid flow motion, mixing phenomena and the pumping number power number, but not affect the power number.
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6
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Manzano Martínez AN, Assirelli M, van der Schaaf J. Droplet size and liquid-liquid mass transfer with reaction in a rotor-stator Spinning Disk Reactor. Chem Eng Sci 2021. [DOI: 10.1016/j.ces.2021.116706] [Citation(s) in RCA: 10] [Impact Index Per Article: 3.3] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 02/07/2023]
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7
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Numerical analysis of hydrodynamics characteristics in a top-covered unbaffled stirred tank. CHEMICAL PAPERS 2021. [DOI: 10.1007/s11696-021-01767-9] [Citation(s) in RCA: 2] [Impact Index Per Article: 0.7] [Reference Citation Analysis] [Track Full Text] [Subscribe] [Scholar Register] [Indexed: 11/26/2022]
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8
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Płusa T, Talaga J, Duda A, Duda P. Modeling mixing dynamics in uncovered baffled and unbaffled stirred tanks. AIChE J 2021. [DOI: 10.1002/aic.17322] [Citation(s) in RCA: 3] [Impact Index Per Article: 1.0] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 11/07/2022]
Affiliation(s)
- Tomasz Płusa
- Faculty of Mechanical Engineering, Institute of Thermal and Process Engineering Cracow University of Technology Kraków Poland
| | - Jan Talaga
- Faculty of Mechanical Engineering, Institute of Thermal and Process Engineering Cracow University of Technology Kraków Poland
| | - Andrzej Duda
- Faculty of Mechanical Engineering, Institute of Thermal and Process Engineering Cracow University of Technology Kraków Poland
| | - Piotr Duda
- Faculty of Mechanical Engineering, Institute of Thermal and Process Engineering Cracow University of Technology Kraków Poland
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9
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Abstract
This study investigated the efficacy of a novel correlation of power input, energy dissipation rate and mixing time as a potential route to identify the orbitally shaken bioreactor (OSB) system. The Buckingham’s π-theorem was used to designate and transform dimensionless Newton numbers with five relevant power input variables. These variables were empirically varied to evaluate the correlation among the dimensionless numbers. The Newton number decreases with the increased shaking frequency and filling volume. Previous work has focused on optimizing the mixing process by evaluating different shaking and agitation mixing methods. We establish a new mixing process and assessable measurement of the mixing time in the OSB. An innovative explanation of mixing time for the thermal method is proposed. The optimal mixing time is independent of the temperature of filled liquid. The dimensionless mixing number remained constant in the turbulent regime and increasing with the increased liquid viscosity and filling volume. Our findings revealed that the observed correlation is a practical tool to figure the power consumption and mixing efficiency as cell cultivation in all OSB scales and is fully validated when scaling–up system.
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10
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Kazemzadeh A, Elias C, Tamer M, Lohi A, Ein-Mozaffari F. Mass transfer in a single-use angled-shaft aerated stirred bioreactor applicable for animal cell culture. Chem Eng Sci 2020. [DOI: 10.1016/j.ces.2020.115606] [Citation(s) in RCA: 8] [Impact Index Per Article: 2.0] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 10/24/2022]
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11
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Scargiali F, Brucato A, Micale G, Tamburini A. On the Reduction of Power Consumption in Vortexing Unbaffled Bioslurry Reactors. Ind Eng Chem Res 2020. [DOI: 10.1021/acs.iecr.0c00726] [Citation(s) in RCA: 0] [Impact Index Per Article: 0] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 10/24/2022]
Affiliation(s)
- Francesca Scargiali
- Dipartimento di Ingegneria, Università di Palermo, Viale delle Scienze, Ed.6, 90128 Palermo, Italy
| | - Alberto Brucato
- Dipartimento di Ingegneria, Università di Palermo, Viale delle Scienze, Ed.6, 90128 Palermo, Italy
| | - Giorgio Micale
- Dipartimento di Ingegneria, Università di Palermo, Viale delle Scienze, Ed.6, 90128 Palermo, Italy
| | - Alessandro Tamburini
- Dipartimento di Ingegneria, Università di Palermo, Viale delle Scienze, Ed.6, 90128 Palermo, Italy
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12
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Effect of Impeller Design on Power Characteristics and Newtonian Fluids Mixing Efficiency in a Mechanically Agitated Vessel at Low Reynolds Numbers. ENERGIES 2020. [DOI: 10.3390/en13030640] [Citation(s) in RCA: 20] [Impact Index Per Article: 5.0] [Reference Citation Analysis] [Abstract] [Track Full Text] [Subscribe] [Scholar Register] [Indexed: 11/16/2022]
Abstract
The mixing process is a widespread phenomenon, which plays an essential role among a large number of industrial processes. The effectiveness of mixing depends on the state of mixed phases, temperature, viscosity and density of liquids, mutual solubility of mixed fluids, type of stirrer, and, what is the most critical property, the shape of the impeller. In the present research, the objective was to investigate the Newtonian fluids flow motion as well as all essential parameters for the mechanically agitated vessel with a new impeller type. The velocity field, the power number, and the pumping capacity values were determined using computer simulation and experimental measurements. The basis for the assessment of the intensity degree and the efficiency of mixing had to do with the analysis of the distribution of velocity vectors and the power number. An experimental and numerical study was carried out for various stirred process parameters and for fluids whose viscosity ranged from low to very high in order to determine optimal conditions for the mixing process.
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13
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Effects of geometrical and physical factors on light particles dispersion by agitation characteristic curve. Chin J Chem Eng 2019. [DOI: 10.1016/j.cjche.2019.02.012] [Citation(s) in RCA: 4] [Impact Index Per Article: 0.8] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 11/23/2022]
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14
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Experimental study of power consumption, local characteristics distributions and homogenization energy in gas–liquid stirred tank reactors. Chin J Chem Eng 2019. [DOI: 10.1016/j.cjche.2018.10.011] [Citation(s) in RCA: 7] [Impact Index Per Article: 1.4] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 11/24/2022]
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15
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Gas-liquid mass transfer rates in unbaffled tanks stirred by PBT: scale-up effects and pumping direction. Chem Eng Res Des 2018. [DOI: 10.1016/j.cherd.2018.07.006] [Citation(s) in RCA: 4] [Impact Index Per Article: 0.7] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 11/22/2022]
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16
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Liu Z, Li M, Xu W, Ouyang D, Li M, Li Z, Xie D, Sun J. On the Agitation Characteristic Curve of Medium Light Particles in a Stirred Tank Based on CFD Simulation. JOURNAL OF CHEMICAL ENGINEERING OF JAPAN 2018. [DOI: 10.1252/jcej.17we140] [Citation(s) in RCA: 3] [Impact Index Per Article: 0.5] [Reference Citation Analysis] [Track Full Text] [Subscribe] [Scholar Register] [Indexed: 11/11/2022]
Affiliation(s)
- Zeng Liu
- Department of Naval Architecture and Ocean Engineering, Huazhong University of Science and Technology
- Hubei Key Laboratory of Naval Architecture and Ocean Engineering, Hydrodynamics, Huazhong University of Science and Technology
- Collaborative Innovation Center for Advanced Ship and Deep-Sea Exploration
| | - Meng Li
- Department of Naval Architecture and Ocean Engineering, Huazhong University of Science and Technology
| | - Wentao Xu
- Department of Naval Architecture and Ocean Engineering, Huazhong University of Science and Technology
| | - Degang Ouyang
- Research and Development Centre of Wuhan Iron and Steel Co., Ltd
| | - Minghui Li
- Research and Development Centre of Wuhan Iron and Steel Co., Ltd
| | - Zhishan Li
- Department of Naval Architecture and Ocean Engineering, Huazhong University of Science and Technology
| | - De Xie
- Department of Naval Architecture and Ocean Engineering, Huazhong University of Science and Technology
- Hubei Key Laboratory of Naval Architecture and Ocean Engineering, Hydrodynamics, Huazhong University of Science and Technology
- Collaborative Innovation Center for Advanced Ship and Deep-Sea Exploration
| | - Jianglong Sun
- Department of Naval Architecture and Ocean Engineering, Huazhong University of Science and Technology
- Hubei Key Laboratory of Naval Architecture and Ocean Engineering, Hydrodynamics, Huazhong University of Science and Technology
- Collaborative Innovation Center for Advanced Ship and Deep-Sea Exploration
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17
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Labík L, Petricříček R, Moucha T, Brucato A, Caputo G, Grisafi F, Scargiali F. Scale-up and viscosity effects on gas–liquid mass transfer rates in unbaffled stirred tanks. Chem Eng Res Des 2018. [DOI: 10.1016/j.cherd.2018.01.051] [Citation(s) in RCA: 7] [Impact Index Per Article: 1.2] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 10/18/2022]
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18
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Li L, Wang J, Feng L, Gu X. Computational fluid dynamics simulation of hydrodynamics in an uncovered unbaffled tank agitated by pitched blade turbines. KOREAN J CHEM ENG 2017. [DOI: 10.1007/s11814-017-0208-9] [Citation(s) in RCA: 8] [Impact Index Per Article: 1.1] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 10/18/2022]
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19
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Sirasitthichoke C, Armenante PM. Power Dissipation and Power Number Correlations for a Retreat-Blade Impeller under Different Baffling Conditions. Ind Eng Chem Res 2017. [DOI: 10.1021/acs.iecr.7b02634] [Citation(s) in RCA: 8] [Impact Index Per Article: 1.1] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 11/29/2022]
Affiliation(s)
- Chadakarn Sirasitthichoke
- Otto H. York Department of
Chemical, Biological and Pharmaceutical Engineering, New Jersey Institute of Technology, 323 M. L. King Boulevard, Newark, New Jersey 07102-1982, United States
| | - Piero M. Armenante
- Otto H. York Department of
Chemical, Biological and Pharmaceutical Engineering, New Jersey Institute of Technology, 323 M. L. King Boulevard, Newark, New Jersey 07102-1982, United States
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20
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Deshpande S, Kar K, Walker J, Pressler J, Su W. An experimental and computational investigation of vortex formation in an unbaffled stirred tank. Chem Eng Sci 2017. [DOI: 10.1016/j.ces.2017.04.002] [Citation(s) in RCA: 22] [Impact Index Per Article: 3.1] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 11/26/2022]
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21
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Scargiali F, Tamburini A, Caputo G, Micale G. On the assessment of power consumption and critical impeller speed in vortexing unbaffled stirred tanks. Chem Eng Res Des 2017. [DOI: 10.1016/j.cherd.2017.04.035] [Citation(s) in RCA: 21] [Impact Index Per Article: 3.0] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 11/26/2022]
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22
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Numerical simulation of hydrodynamics in an uncovered unbaffled stirred tank. CHEMICAL PAPERS 2017. [DOI: 10.1007/s11696-017-0180-1] [Citation(s) in RCA: 7] [Impact Index Per Article: 1.0] [Reference Citation Analysis] [Track Full Text] [Subscribe] [Scholar Register] [Indexed: 10/19/2022]
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23
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Steiros K, Bruce PJK, Buxton ORH, Vassilicos JC. Power consumption and form drag of regular and fractal-shaped turbines in a stirred tank. AIChE J 2016. [DOI: 10.1002/aic.15414] [Citation(s) in RCA: 20] [Impact Index Per Article: 2.5] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 11/09/2022]
Affiliation(s)
- K. Steiros
- Dept. of Aeronautics; Imperial College London; London SW7 2AZ U.K
| | - P. J. K. Bruce
- Dept. of Aeronautics; Imperial College London; London SW7 2AZ U.K
| | - O. R. H. Buxton
- Dept. of Aeronautics; Imperial College London; London SW7 2AZ U.K
| | - J. C. Vassilicos
- Dept. of Aeronautics; Imperial College London; London SW7 2AZ U.K
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24
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Tamburini A, Cipollina A, Micale G, Scargiali F, Brucato A. Particle Suspension in Vortexing Unbaffled Stirred Tanks. Ind Eng Chem Res 2016. [DOI: 10.1021/acs.iecr.6b00824] [Citation(s) in RCA: 16] [Impact Index Per Article: 2.0] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 11/29/2022]
Affiliation(s)
- Alessandro Tamburini
- Dipartimento di Ingegneria
Chimica, Gestionale, Informatica, Meccanica, Università di Palermo, Viale delle Scienze Edificio 6, 90128 Palermo, Italy
| | - Andrea Cipollina
- Dipartimento di Ingegneria
Chimica, Gestionale, Informatica, Meccanica, Università di Palermo, Viale delle Scienze Edificio 6, 90128 Palermo, Italy
| | - Giorgio Micale
- Dipartimento di Ingegneria
Chimica, Gestionale, Informatica, Meccanica, Università di Palermo, Viale delle Scienze Edificio 6, 90128 Palermo, Italy
| | - Francesca Scargiali
- Dipartimento di Ingegneria
Chimica, Gestionale, Informatica, Meccanica, Università di Palermo, Viale delle Scienze Edificio 6, 90128 Palermo, Italy
| | - Alberto Brucato
- Dipartimento di Ingegneria
Chimica, Gestionale, Informatica, Meccanica, Università di Palermo, Viale delle Scienze Edificio 6, 90128 Palermo, Italy
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25
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Wang S, Jiang M, Ibrahim S, Wu J, Feng X, Duan X, Yang Z, Yang C, Ohmura N. Optimized Stirred Reactor for Enhanced Particle Dispersion. Chem Eng Technol 2016. [DOI: 10.1002/ceat.201500458] [Citation(s) in RCA: 10] [Impact Index Per Article: 1.3] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 11/12/2022]
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26
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Scargiali F, Busciglio A, Grisafi F, Brucato A. Free surface oxygen transfer in large aspect ratio unbaffled bio-reactors, with or without draft-tube. Biochem Eng J 2015. [DOI: 10.1016/j.bej.2015.04.006] [Citation(s) in RCA: 10] [Impact Index Per Article: 1.1] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 10/23/2022]
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27
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Senda S, Yamagami N, Komoda Y, Hirata Y, Suzuki H, Hidema R. Power Characteristics of a Rotationally Reciprocating Impeller. JOURNAL OF CHEMICAL ENGINEERING OF JAPAN 2015. [DOI: 10.1252/jcej.14we392] [Citation(s) in RCA: 8] [Impact Index Per Article: 0.9] [Reference Citation Analysis] [Track Full Text] [Subscribe] [Scholar Register] [Indexed: 11/11/2022]
Affiliation(s)
- Saki Senda
- Department of Chemical Science and Engineering, Kobe University
| | | | | | | | - Hiroshi Suzuki
- Department of Chemical Science and Engineering, Kobe University
| | - Ruri Hidema
- Organization of Advanced Science and Technology, Kobe University
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28
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Devi TT, Kumar B. Scale up criteria for dual stirred gas-liquid unbaffled tank with concave blade impeller. KOREAN J CHEM ENG 2014. [DOI: 10.1007/s11814-014-0090-7] [Citation(s) in RCA: 6] [Impact Index Per Article: 0.6] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 10/25/2022]
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29
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Tamburini A, Brucato A, Busciglio A, Cipollina A, Grisafi F, Micale G, Scargiali F, Vella G. Solid–Liquid Suspensions in Top-Covered Unbaffled Vessels: Influence of Particle Size, Liquid Viscosity, Impeller Size, and Clearance. Ind Eng Chem Res 2014. [DOI: 10.1021/ie500203r] [Citation(s) in RCA: 38] [Impact Index Per Article: 3.8] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 11/29/2022]
Affiliation(s)
- A. Tamburini
- Dipartimento di Ingegneria
Chimica, Gestionale, Informatica, Meccanica, Università di Palermo, Viale delle Scienze Ed. 6, 90128 Palermo, Italy
| | - A. Brucato
- Dipartimento di Ingegneria
Chimica, Gestionale, Informatica, Meccanica, Università di Palermo, Viale delle Scienze Ed. 6, 90128 Palermo, Italy
| | - A. Busciglio
- Dipartimento di Ingegneria
Chimica, Gestionale, Informatica, Meccanica, Università di Palermo, Viale delle Scienze Ed. 6, 90128 Palermo, Italy
| | - A. Cipollina
- Dipartimento di Ingegneria
Chimica, Gestionale, Informatica, Meccanica, Università di Palermo, Viale delle Scienze Ed. 6, 90128 Palermo, Italy
| | - F. Grisafi
- Dipartimento di Ingegneria
Chimica, Gestionale, Informatica, Meccanica, Università di Palermo, Viale delle Scienze Ed. 6, 90128 Palermo, Italy
| | - G. Micale
- Dipartimento di Ingegneria
Chimica, Gestionale, Informatica, Meccanica, Università di Palermo, Viale delle Scienze Ed. 6, 90128 Palermo, Italy
| | - F. Scargiali
- Dipartimento di Ingegneria
Chimica, Gestionale, Informatica, Meccanica, Università di Palermo, Viale delle Scienze Ed. 6, 90128 Palermo, Italy
| | - G. Vella
- Dipartimento di Ingegneria
Chimica, Gestionale, Informatica, Meccanica, Università di Palermo, Viale delle Scienze Ed. 6, 90128 Palermo, Italy
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30
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Scargiali F, Busciglio A, Grisafi F, Brucato A. Mass transfer and hydrodynamic characteristics of unbaffled stirred bio-reactors: Influence of impeller design. Biochem Eng J 2014. [DOI: 10.1016/j.bej.2013.11.009] [Citation(s) in RCA: 46] [Impact Index Per Article: 4.6] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 11/28/2022]
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