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Yu Y, Yang P, Meng H, Liu H, Zhang J, Yu H. Bubble Morphology Analysis and Pressure Drop of Gas–Liquid Two-Phase Flow inside a Quarto Static Mixer. Ind Eng Chem Res 2022. [DOI: 10.1021/acs.iecr.2c03917] [Citation(s) in RCA: 0] [Impact Index Per Article: 0] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 12/14/2022]
Affiliation(s)
- Yanfang Yu
- Liaoning Key Laboratory of Chemical Technology for Efficient Mixing, Shenyang University of Chemical Technology, Shenyang 110142, China
| | - Peng Yang
- Liaoning Key Laboratory of Chemical Technology for Efficient Mixing, Shenyang University of Chemical Technology, Shenyang 110142, China
| | - Huibo Meng
- College of New Energy, China University of Petroleum (East China), Qingdao 266580, China
| | - Huanchen Liu
- Liaoning Key Laboratory of Chemical Technology for Efficient Mixing, Shenyang University of Chemical Technology, Shenyang 110142, China
| | - Jiawei Zhang
- Liaoning Key Laboratory of Chemical Technology for Efficient Mixing, Shenyang University of Chemical Technology, Shenyang 110142, China
| | - Henglei Yu
- Liaoning Key Laboratory of Chemical Technology for Efficient Mixing, Shenyang University of Chemical Technology, Shenyang 110142, China
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2
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Bae K, Young Kim J, Seok Go K, Sun Nho N, Kim D, Wook Bae J, Hyun Lee D. Heat transfer with single- and dual-gas distribution in a pressurised bubble column. Chem Eng Sci 2022. [DOI: 10.1016/j.ces.2022.118264] [Citation(s) in RCA: 0] [Impact Index Per Article: 0] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 11/06/2022]
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3
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Puiman L, Elisiário MP, Crasborn LM, Wagenaar LE, Straathof AJ, Haringa C. Gas mass transfer in syngas fermentation broths is enhanced by ethanol. Biochem Eng J 2022. [DOI: 10.1016/j.bej.2022.108505] [Citation(s) in RCA: 0] [Impact Index Per Article: 0] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 11/02/2022]
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4
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Nedeltchev S, Katerla J, Basiak E. Novel Hybrid Methods for Identifying the Main Transition Velocities in Various Bubble Columns. JOURNAL OF CHEMICAL ENGINEERING OF JAPAN 2022. [DOI: 10.1252/jcej.21we082] [Citation(s) in RCA: 0] [Impact Index Per Article: 0] [Reference Citation Analysis] [Track Full Text] [Subscribe] [Scholar Register] [Indexed: 11/11/2022]
Affiliation(s)
| | - Jakub Katerla
- Institute of Chemical Engineering, Polish Academy of Sciences
| | - Ewelina Basiak
- Institute of Chemical Engineering, Polish Academy of Sciences
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5
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Puiman L, Abrahamson B, Lans RGVD, Haringa C, Noorman HJ, Picioreanu C. Alleviating mass transfer limitations in industrial external-loop syngas-to-ethanol fermentation. Chem Eng Sci 2022. [DOI: 10.1016/j.ces.2022.117770] [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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6
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Bae K, Kim JY, Go KS, Nho NS, Kim D, Bae JW, Lee DH. Bubble/micro-bubble regime transition in a pressurized bubble column of a low surface tension liquid system. Chem Eng Sci 2022. [DOI: 10.1016/j.ces.2021.117191] [Citation(s) in RCA: 2] [Impact Index Per Article: 1.0] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 11/30/2022]
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7
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Abstract
Micro-fluidized bed has aroused much attention due to its low-cost, intensified-process and fast-screening properties. In this paper, a micro-fluidized bed (15 × 15 mm in cross-section) was designed and fabricated with the use of the stereolithography printing technique, for the investigation of bubbles’ hydrodynamics and comparison of the solids (3D-printed particles VS fungal pellets) fluidization characteristics. In a liquid–gas system, bubble flow regime started from mono-dispersed homogeneous regime, followed by poly-dispersed homogeneous regime, transition bubble regime and heterogeneous bubble regime with increasing gas flowrates from 3.7 mL/min to 32.7 mL/min. The impacts from operating parameters such as gas flowrate, superficial liquid velocity and gas sparger size on bubble size, velocity and volume fraction have been summarized. In liquid–solid fluidization, different solid fluidization regimes for both particles bed and pellets bed were identified. From the bed expansion results, much higher Umf of 7.8 mm/s from pellets fluidization was observed compared that of 2.3 mm/s in particles fluidization, because the hyphal structures of fungal pellets increased surface friction but also tended to agglomerate. The similar R–Z exponent n (5.7 and 5.5 for pellets and particles, respectively) between pellets and particles was explained by the same solid diameter, but much higher Ut of 436 µm/s in particles bed than that of 196 µm/s in pellets bed is a consequence of the higher density of solid particles. This paper gives insights on the development of MFB and its potential in solid processing.
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8
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Validation studies to assist in the development of scale and system independent CFD models for industrial bubble columns. Chem Eng Res Des 2021. [DOI: 10.1016/j.cherd.2021.04.023] [Citation(s) in RCA: 6] [Impact Index Per Article: 2.0] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 11/19/2022]
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9
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Roche P, Glennon B, Jones RC, Donnellan P. Low-temperature evaporation of continuous pharmaceutical process streams in a bubble column. Chem Eng Res Des 2021. [DOI: 10.1016/j.cherd.2020.09.008] [Citation(s) in RCA: 3] [Impact Index Per Article: 1.0] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 11/25/2022]
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10
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Affiliation(s)
- Xiaoping Guan
- State Key Laboratory of Multi‐phase Complex System, Institute of Process Engineering Chinese Academy of Sciences Beijing China
- Innovation Academy for Green Manufacture Chinese Academy of Sciences Beijing China
| | - Ning Yang
- State Key Laboratory of Multi‐phase Complex System, Institute of Process Engineering Chinese Academy of Sciences Beijing China
- School of Chemical Engineering University of Chinese Academy of Sciences Beijing China
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11
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Effects of the Microbubble Generation Mode on Hydrodynamic Parameters in Gas–Liquid Bubble Columns. Processes (Basel) 2020. [DOI: 10.3390/pr8060663] [Citation(s) in RCA: 3] [Impact Index Per Article: 0.8] [Reference Citation Analysis] [Abstract] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 11/17/2022] Open
Abstract
The hydrodynamics parameters of microbubbles in a bubble column were studied in an air–water system with a range of superficial gas velocity from 0.013 to 0.100 m/s using a differential pressure transmitter, double probe optical fiber probe, and electrical resistance tomography (ERT) technique. Two kinds of microbubble generators (foam gun, sintered plate) were used to generate microbubbles in the bubble column with a diameter of 90 mm, and to compare the effects of different foaming methods on the hydrodynamics parameters in the bubble column. The hydrodynamic behavior of the homogeneous regime and the transition regime was also studied. The results show that, by changing the microbubble-generating device, the hydrodynamic parameters in the column are changed, and both microbubble-generating devices can obtain a higher gas holdup and a narrower chord length distribution. When the foam gun is used as the gas distributor, a higher gas holdup and a narrower average bubble chord length can be obtained than when the sintered plate is used as the gas distributor. In addition, under different operating conditions, the relative frequency distribution of the chord length at different radial positions is mainly concentrated in the interval of 0–5 mm, and it is the highest in the center of the column.
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12
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Abufalgha AA, Clarke KG, Pott RW. Characterisation of bubble diameter and gas hold-up in simulated hydrocarbon-based bioprocesses in a bubble column reactor. Biochem Eng J 2020. [DOI: 10.1016/j.bej.2020.107577] [Citation(s) in RCA: 8] [Impact Index Per Article: 2.0] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 11/26/2022]
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13
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Kumar N, Gupta R, Bansal A. Effect of Surface Tension on Hydrodynamics and Mass Transfer Coefficient in Airlift Reactors. Chem Eng Technol 2020. [DOI: 10.1002/ceat.201900271] [Citation(s) in RCA: 3] [Impact Index Per Article: 0.8] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 11/09/2022]
Affiliation(s)
- Nikesh Kumar
- Dr. B. R. Ambedkar National Institute of TechnologyDepartment of Chemical Engineering Jalandhar Punjab 144011 India
| | - Renu Gupta
- Dr. B. R. Ambedkar National Institute of TechnologyDepartment of Chemical Engineering Jalandhar Punjab 144011 India
| | - Ajay Bansal
- Dr. B. R. Ambedkar National Institute of TechnologyDepartment of Chemical Engineering Jalandhar Punjab 144011 India
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14
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Yan P, Jin H, He G, Guo X, Ma L, Yang S, Zhang R. Numerical simulation of bubble characteristics in bubble columns with different liquid viscosities and surface tensions using a CFD-PBM coupled model. Chem Eng Res Des 2020. [DOI: 10.1016/j.cherd.2019.11.030] [Citation(s) in RCA: 20] [Impact Index Per Article: 5.0] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 11/29/2022]
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15
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Lu X, Ding Y, Yu J, Long B, Zheng X. Experimental study of hydrodynamics and bubble size distribution of an external loop airlift reactor. CAN J CHEM ENG 2019. [DOI: 10.1002/cjce.23456] [Citation(s) in RCA: 6] [Impact Index Per Article: 1.2] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 11/07/2022]
Affiliation(s)
- Xia Lu
- School of Chemical and Engineering and PharmacyWuhan Institute of TechnologyWuhan CityHubei ProvinceP. R. China
- The College of Post and Telecommunication of Wuhan Institute of TechnologyWuhan CityHubei ProvinceP. R. China
| | - Yigang Ding
- School of Chemical and Engineering and PharmacyWuhan Institute of TechnologyWuhan CityHubei ProvinceP. R. China
| | - Jiuyang Yu
- School of Mechanical and Electronic EngineeringWuhan Institute of TechnologyWuhan CityHubei ProvinceP. R. China
| | - Bingwen Long
- School of Chemical and Engineering and PharmacyWuhan Institute of TechnologyWuhan CityHubei ProvinceP. R. China
| | - Xiaotao Zheng
- School of Mechanical and Electronic EngineeringWuhan Institute of TechnologyWuhan CityHubei ProvinceP. R. China
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Salierno G, Maestri M, Piovano S, Cassanello M, Cardona MA, Hojman D, Somacal H. Features of the motion of gel particles in a three-phase bubble column under foaming and non-foaming conditions. Chin J Chem Eng 2018. [DOI: 10.1016/j.cjche.2018.03.026] [Citation(s) in RCA: 4] [Impact Index Per Article: 0.7] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 01/10/2023]
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17
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18
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Guan X, Yang N. Bubble properties measurement in bubble columns: From homogeneous to heterogeneous regime. Chem Eng Res Des 2017. [DOI: 10.1016/j.cherd.2017.09.017] [Citation(s) in RCA: 43] [Impact Index Per Article: 6.1] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 11/25/2022]
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19
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Besagni G, Inzoli F. The effect of liquid phase properties on bubble column fluid dynamics: Gas holdup, flow regime transition, bubble size distributions and shapes, interfacial areas and foaming phenomena. Chem Eng Sci 2017. [DOI: 10.1016/j.ces.2017.03.043] [Citation(s) in RCA: 69] [Impact Index Per Article: 9.9] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 11/29/2022]
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20
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De Guido G, Pellegrini LA. Prediction of the gas hold-up in a large-diameter bubble column with liquid mixtures and electrolytes. Chem Eng Res Des 2017. [DOI: 10.1016/j.cherd.2017.06.022] [Citation(s) in RCA: 3] [Impact Index Per Article: 0.4] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 10/19/2022]
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21
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Besagni G, Inzoli F, Ziegenhein T, Lucas D. Computational Fluid-Dynamic modeling of the pseudo-homogeneous flow regime in large-scale bubble columns. Chem Eng Sci 2017. [DOI: 10.1016/j.ces.2016.11.031] [Citation(s) in RCA: 46] [Impact Index Per Article: 6.6] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 11/16/2022]
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22
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The effect of electrolyte concentration on counter-current gas–liquid bubble column fluid dynamics: Gas holdup, flow regime transition and bubble size distributions. Chem Eng Res Des 2017. [DOI: 10.1016/j.cherd.2016.12.012] [Citation(s) in RCA: 32] [Impact Index Per Article: 4.6] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 11/23/2022]
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23
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Besagni G, Inzoli F, De Guido G, Pellegrini LA. The dual effect of viscosity on bubble column hydrodynamics. Chem Eng Sci 2017. [DOI: 10.1016/j.ces.2016.11.003] [Citation(s) in RCA: 69] [Impact Index Per Article: 9.9] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 10/20/2022]
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