Packing size effects on the liquid circulation property in an external‐loop packed bubble column
Packing size effects on the fluid dynamics in an external‐loop packed bubble column with Raschig rings of three different effective diameters (4.9, 14.1, and 40.7 mm) in the riser were investigated. The overall gas holdup, liquid circulating velocity and gas–liquid mass transfer coefficient were res...
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Published in | AIChE journal Vol. 68; no. 12 |
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Main Authors | , , |
Format | Journal Article |
Language | English |
Published |
Hoboken, USA
John Wiley & Sons, Inc
01.12.2022
American Institute of Chemical Engineers |
Subjects | |
Online Access | Get full text |
ISSN | 0001-1541 1547-5905 |
DOI | 10.1002/aic.17851 |
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Abstract | Packing size effects on the fluid dynamics in an external‐loop packed bubble column with Raschig rings of three different effective diameters (4.9, 14.1, and 40.7 mm) in the riser were investigated. The overall gas holdup, liquid circulating velocity and gas–liquid mass transfer coefficient were respectively measured by volume expansion, tracer‐response, and dynamic oxygen‐absorption techniques. CFD simulation with the Euler–Euler two‐fluid method was used to predict the liquid circulating velocity by treating the packing as a porous medium. Compared to the empty column, the gas holdup was found to increase in the presence of packing, however, the liquid circulating velocity and gas–liquid mass transfer coefficient are rather complicated. Specifically, the gas holdup increases with the decrease of packing size, while the liquid circulating velocity is on the contrary, and the maximal gas–liquid mass transfer coefficient is achieved under packing diameter of 14.1 mm. |
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AbstractList | Packing size effects on the fluid dynamics in an external‐loop packed bubble column with Raschig rings of three different effective diameters (4.9, 14.1, and 40.7 mm) in the riser were investigated. The overall gas holdup, liquid circulating velocity and gas–liquid mass transfer coefficient were respectively measured by volume expansion, tracer‐response, and dynamic oxygen‐absorption techniques. CFD simulation with the Euler–Euler two‐fluid method was used to predict the liquid circulating velocity by treating the packing as a porous medium. Compared to the empty column, the gas holdup was found to increase in the presence of packing, however, the liquid circulating velocity and gas–liquid mass transfer coefficient are rather complicated. Specifically, the gas holdup increases with the decrease of packing size, while the liquid circulating velocity is on the contrary, and the maximal gas–liquid mass transfer coefficient is achieved under packing diameter of 14.1 mm. |
Author | Cheng, Zhenmin Luo, Gang Tang, Yanling |
Author_xml | – sequence: 1 givenname: Yanling orcidid: 0000-0002-5256-919X surname: Tang fullname: Tang, Yanling organization: East China University of Science and Technology – sequence: 2 givenname: Gang surname: Luo fullname: Luo, Gang organization: East China University of Science and Technology – sequence: 3 givenname: Zhenmin orcidid: 0000-0001-8315-8580 surname: Cheng fullname: Cheng, Zhenmin email: zmcheng@ecust.edu.cn organization: East China University of Science and Technology |
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Cites_doi | 10.1016/j.cej.2012.09.106 10.1002/jctb.3917 10.1016/S1385-8947(97)00043-0 10.1016/j.ces.2007.07.069 10.1016/j.ces.2007.08.036 10.1016/j.cej.2007.08.027 10.1016/j.ces.2005.08.024 10.1016/j.ces.2008.10.009 10.1016/j.memsci.2021.119592 10.1016/j.compchemeng.2010.06.006 10.1016/j.cej.2019.122292 10.1016/j.ces.2019.115294 10.1016/j.seppur.2020.116908 10.1016/S0009-2509(98)00209-7 10.1016/j.ces.2018.04.045 10.1073/pnas.2105058118 10.1002/aic.15543 10.1021/ie020436i 10.1016/j.jtice.2021.11.016 10.1016/j.bej.2005.08.014 10.1016/j.ces.2016.04.004 10.1007/s00231-012-1056-0 10.1002/aic.690250513 10.1021/ie970275w 10.1016/j.cej.2019.122993 10.1002/jctb.3783 10.1021/ie050402l 10.1021/acs.est.7b04905 10.1016/0009-2509(94)00290-8 10.1016/j.ces.2015.01.013 10.1021/acs.iecr.7b00123 10.1021/ie0494925 10.1017/S002211201000443X 10.1002/aic.16624 10.1111/j.1745-6592.1999.tb00211.x 10.1039/C4RA01852D 10.1021/ie0108301 10.1016/j.cej.2005.03.009 10.1252/jcej.9.29 10.1016/j.bej.2016.11.014 10.1021/i260049a016 10.1016/j.ces.2021.116988 10.1016/S1004-9541(14)60050-1 10.1016/j.ces.2010.04.019 10.1016/j.cep.2020.107800 10.1016/j.ces.2019.115231 10.1016/j.ces.2009.08.006 |
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References | 2018; 186 1995; 73 2022; 131 2017; 63 1974; 13 2013; 49 2009; 64 2013; 88 2015; 126 2020; 382 2021; 246 1997; 67 2020; 248 2020; 148 2011; 35 1994; 49 2016; 18 2005; 27 2017; 157 1976; 9 2005; 44 2014; 22 2017; 118 2017; 51 2011; 666 1998; 37 2010; 65 2014; 4 2006; 61 1979; 25 2002; 41 1999; 19 2019; 65 2021; 636 2017; 56 2021; 118 2020; 379 2005; 109 2008; 139 2020; 211 2007; 62 2012; 213 1998; 53 2003; 42 2019; 210 2012; 87 e_1_2_9_50_1 e_1_2_9_10_1 e_1_2_9_35_1 e_1_2_9_12_1 e_1_2_9_33_1 e_1_2_9_14_1 e_1_2_9_39_1 e_1_2_9_16_1 e_1_2_9_37_1 e_1_2_9_18_1 e_1_2_9_41_1 e_1_2_9_20_1 Bian Q (e_1_2_9_31_1) 2016; 18 e_1_2_9_22_1 e_1_2_9_45_1 e_1_2_9_24_1 e_1_2_9_43_1 e_1_2_9_8_1 e_1_2_9_6_1 e_1_2_9_4_1 e_1_2_9_2_1 e_1_2_9_26_1 e_1_2_9_49_1 e_1_2_9_28_1 e_1_2_9_47_1 e_1_2_9_30_1 e_1_2_9_11_1 e_1_2_9_34_1 Lamine AS (e_1_2_9_13_1) 1995; 73 e_1_2_9_32_1 e_1_2_9_15_1 e_1_2_9_38_1 e_1_2_9_17_1 e_1_2_9_36_1 e_1_2_9_19_1 e_1_2_9_42_1 e_1_2_9_40_1 e_1_2_9_21_1 e_1_2_9_46_1 e_1_2_9_23_1 e_1_2_9_44_1 e_1_2_9_7_1 e_1_2_9_5_1 e_1_2_9_3_1 e_1_2_9_9_1 e_1_2_9_25_1 e_1_2_9_27_1 e_1_2_9_48_1 e_1_2_9_29_1 |
References_xml | – volume: 35 start-page: 41 issue: 1 year: 2011 end-page: 49 article-title: Characteristics of liquid and tracer dispersion in trickle‐bed reactors: effect on CFD modeling and experimental analyses publication-title: Comput Chem Eng – volume: 210 year: 2019 article-title: Investigation of the liquid mixing characteristic of an external‐loop hybrid fluidized‐bed airlift reactor publication-title: Chem Eng Sci – volume: 382 year: 2020 article-title: Intensified steam methane reforming coupled with Ca‐Ni looping in a dual fluidized bed reactor system: a conceptual design publication-title: Chem Eng J – volume: 18 start-page: 83 issue: 3 year: 2016 end-page: 90 article-title: Hydrodynamic characteristics in an external loop airlift slurry reactor publication-title: China Pet Process Petrochemical Technol – volume: 4 start-page: 62347 issue: 107 year: 2014 end-page: 62355 article-title: Hydrodynamics and mass transfer study of oil‐water micro‐emulsion in a three phase external loop airlift reactor publication-title: RSC Adv – volume: 64 start-page: 4992 issue: 23 year: 2009 end-page: 5001 article-title: Dimensional similitude for scale‐up of hydrodynamics in a gas‐liquid‐(solid) EL‐ALR publication-title: Chem Eng Sci – volume: 63 start-page: 226 issue: 1 year: 2017 end-page: 237 article-title: Methanol synthesis in a three‐phase catalytic bed under nonwetted condition publication-title: AIChE J – volume: 67 start-page: 205 issue: 3 year: 1997 end-page: 214 article-title: Hydrodynamics and mass transfer studies in a novel external‐loop airlift reactor publication-title: Chem Eng J – volume: 157 start-page: 2 year: 2017 end-page: 14 article-title: Characterising gas behaviour during gas–liquid co‐current up‐flow in packed beds using magnetic resonance imaging publication-title: Chem Eng Sci – volume: 211 year: 2020 article-title: Hydrodynamics and mass transfer in a slurry external airlift loop reactor integrating mixing and separation publication-title: Chem Eng Sci – volume: 41 start-page: 2124 year: 2002 end-page: 2128 article-title: Hydrodynamic characteristics in an external loop airlift bioreactor containing a spinning Sparger and a packed bed publication-title: Ind Eng Chem Res – volume: 666 start-page: 189 year: 2011 end-page: 203 article-title: Bubbles emerging from a submerged granular bed publication-title: J Fluid Mech – volume: 53 start-page: 4085 issue: 24 year: 1998 end-page: 4094 article-title: On the scale‐up of external loop airlift reactors: Newtonian systems publication-title: Chem Eng Sci – volume: 131 year: 2022 article-title: Effects of blade structures on the dissolution and gas‐liquid mass transfer performance of cup‐shaped blade mixers publication-title: J Taiwan Inst Chem Eng – volume: 246 year: 2021 article-title: An analysis on catalyst wettability design in strong exothermic reactions publication-title: Chem Eng Sci – volume: 118 start-page: 53 year: 2017 end-page: 63 article-title: Enhanced mass transfer in a novel external‐loop airlift reactor with self‐agitated impellers publication-title: Biochem Eng J – volume: 213 start-page: 50 year: 2012 end-page: 61 article-title: Investigation of mixing characteristics in a packed‐bed external loop airlift bioreactor using tomography images publication-title: Chem Eng J – volume: 56 start-page: 13490 issue: 45 year: 2017 end-page: 13496 article-title: Packingsize effect on the mean bubble diameter in a fixed bed under gas‐liquid concurrent upflow publication-title: Ind Eng Chem Res – volume: 139 start-page: 523 issue: 3 year: 2008 end-page: 531 article-title: Experimental study and modeling on liquid dispersion in external‐loop airlift slurry reactors publication-title: Chem Eng J – volume: 248 year: 2020 article-title: Enhanced enzyme‐based CO capture in countercurrent packed‐bed column reactors publication-title: Sep Purif Technol – volume: 22 start-page: 267 issue: 3 year: 2014 end-page: 273 article-title: Hydrodynamics and mass transfer of oily micro‐emulsions in an external loop airlift reactor publication-title: Chin J Chem Eng – volume: 62 start-page: 7026 issue: 24 year: 2007 end-page: 7032 article-title: Hydrodynamics of trickle bed reactors at high pressure: two‐phase flow model for pressure drop and liquid holdup, formulation and experimental validation publication-title: Chem Eng Sci – volume: 44 start-page: 9299 issue: 24 year: 2005 end-page: 9306 article-title: Volatile organic chemical mass transfer in an external loop airlift bioreactor with a packed bed publication-title: Ind Eng Chem Res. – volume: 636 year: 2021 article-title: Enhancement of gas‐liquid mass transfer in curved membrane contactors with the generation of dean vortices publication-title: J Membr Sci – volume: 19 start-page: 105 issue: 2 year: 1999 end-page: 113 article-title: Fundamental changes in situ air sparging how patterns publication-title: Ground Water – volume: 118 issue: 30 year: 2021 article-title: Flowering in bursting bubbles with viscoelastic interfaces publication-title: Proc Natl Acad Sci U S A – volume: 379 year: 2020 article-title: Gas‐liquid hydrogenation in continuous flow—the effect of mass transfer and residence time in powder packed‐bed and catalyst‐coated reactors publication-title: Chem Eng J – volume: 109 start-page: 49 issue: 1 year: 2005 end-page: 55 article-title: Liquid circulation rates in two‐ and three‐phase external airlift reactors publication-title: Chem Eng J – volume: 51 start-page: 14233 year: 2017 end-page: 14243 article-title: Surrogate‐based correlation models in view of real‐time control of ozonation of secondary treated municipal wastewater‐model development and dynamic validation publication-title: Environ Sci Technol – volume: 65 issue: 8 year: 2019 article-title: Gas hold‐up and bubble behavior in an upflow packed bed column in the limit of low flow rate publication-title: AIChE J – volume: 61 start-page: 1300 issue: 4 year: 2006 end-page: 1311 article-title: Solid effects on hydrodynamics and heat transfer in an external loop airlift reactor publication-title: Chem Eng Sci – volume: 49 start-page: 11 issue: 1 year: 2013 end-page: 19 article-title: Hydrodynamics and oxygen mass transfer in a packed bed split‐cylinder airlift reactor containing dilute alcoholic solutions publication-title: Heat Mass Transf – volume: 49 start-page: 5747 year: 1994 end-page: 5762 article-title: Gas‐liquid flow in bubble columns and loop reactors: Part II. Comparison of detailed experiments and flow simulations publication-title: Chem Eng Sci – volume: 148 year: 2020 article-title: HETP measurement using industrial‐scale batch distillation publication-title: Chem Eng Process – volume: 27 start-page: 138 issue: 2 year: 2005 end-page: 145 article-title: Hydrodynamic and oxygen mass transfer in an external loop airlift bioreactor with a packed bed publication-title: Biochem Eng J – volume: 42 start-page: 929 issue: 4 year: 2003 end-page: 936 article-title: Influence of gas and liquid flow rates and the size and shape of particles on the regime flow maps obtained in concurrent gas‐liquid downflow and upflow through packed beds publication-title: Ind Eng Chem Res – volume: 88 start-page: 887 issue: 5 year: 2013 end-page: 896 article-title: Dynamic and local gas holdup studies in external loop recirculating airlift reactor with two rolls of fiberglass packing using electrical resistance tomography publication-title: J Chem Technol Biotechnol – volume: 62 start-page: 7033 issue: 24 year: 2007 end-page: 7044 article-title: Investigation of liquid maldistribution in trickle‐bed reactors using porous media concept in CFD publication-title: Chem Eng Sci – volume: 65 start-page: 4231 issue: 14 year: 2010 end-page: 4238 article-title: Effect of coalescence and breakup on bubble size distributions in a two‐dimensional packed bed publication-title: Chem Eng Sci – volume: 87 start-page: 1529 year: 2012 end-page: 1540 article-title: Liquid velocity in a high‐solids‐loading three‐phase external‐loop airlift reactor publication-title: J Chem Technol Biotechnol – volume: 73 start-page: 280 issue: 3 year: 1995 end-page: 285 article-title: Influence of viscosity and foaming properties on heat‐transfer in packed‐bed with cocurrent upflow of gas and liquid publication-title: Chem Eng Res Des – volume: 44 start-page: 1067 issue: 4 year: 2005 end-page: 1072 article-title: Enhanced oxygen mass transfer in an external loop airlift bioreactor using a packed bed publication-title: Ind Eng Chem Res – volume: 25 start-page: 843 issue: 5 year: 1979 end-page: 855 article-title: Drag coefficient and relative velocity in bubbly, droplet or particulate flows publication-title: AIChE J – volume: 9 start-page: 29 issue: 1 year: 1976 end-page: 34 article-title: Liquid‐phase mass transfer coefficient and gas holdup in a packed‐bed concurrent up‐flow column publication-title: J Chem Eng Japan – volume: 37 start-page: 759 issue: 3 year: 1998 end-page: 769 article-title: Liquid phase hydrogenation of maleic anhydride to 1,4‐butanediol in a packed bubble column reactor publication-title: Ind Eng Chem Res – volume: 64 start-page: 207 issue: 2 year: 2009 end-page: 218 article-title: CFD modeling of radial spreading of flow in trickle‐bed reactors due to mechanical and capillary dispersion publication-title: Chem Eng Sci – volume: 186 start-page: 199 year: 2018 end-page: 208 article-title: Effect of packing size on packed bubble column hydrodynamics publication-title: Chem Eng Sci – volume: 13 start-page: 84 year: 1974 end-page: 91 article-title: Bubble size, interfacial area, and liquid‐phase mass transfer coefficient in bubble columns publication-title: Ind Eng Chem Process Des Dev – volume: 126 start-page: 698 year: 2015 end-page: 710 article-title: Liquid spreading in trickle‐bed reactors: experiments and numerical simulations using Eulerian‐Eulerian two‐fluid approach publication-title: Chem Eng Sci – ident: e_1_2_9_33_1 doi: 10.1016/j.cej.2012.09.106 – ident: e_1_2_9_34_1 doi: 10.1002/jctb.3917 – ident: e_1_2_9_26_1 doi: 10.1016/S1385-8947(97)00043-0 – ident: e_1_2_9_39_1 doi: 10.1016/j.ces.2007.07.069 – ident: e_1_2_9_43_1 doi: 10.1016/j.ces.2007.08.036 – ident: e_1_2_9_29_1 doi: 10.1016/j.cej.2007.08.027 – ident: e_1_2_9_46_1 doi: 10.1016/j.ces.2005.08.024 – volume: 18 start-page: 83 issue: 3 year: 2016 ident: e_1_2_9_31_1 article-title: Hydrodynamic characteristics in an external loop airlift slurry reactor publication-title: China Pet Process Petrochemical Technol – ident: e_1_2_9_40_1 doi: 10.1016/j.ces.2008.10.009 – ident: e_1_2_9_20_1 doi: 10.1016/j.memsci.2021.119592 – ident: e_1_2_9_41_1 doi: 10.1016/j.compchemeng.2010.06.006 – ident: e_1_2_9_2_1 doi: 10.1016/j.cej.2019.122292 – ident: e_1_2_9_32_1 doi: 10.1016/j.ces.2019.115294 – ident: e_1_2_9_4_1 doi: 10.1016/j.seppur.2020.116908 – ident: e_1_2_9_48_1 doi: 10.1016/S0009-2509(98)00209-7 – ident: e_1_2_9_12_1 doi: 10.1016/j.ces.2018.04.045 – ident: e_1_2_9_21_1 doi: 10.1073/pnas.2105058118 – ident: e_1_2_9_24_1 doi: 10.1002/aic.15543 – ident: e_1_2_9_14_1 doi: 10.1021/ie020436i – ident: e_1_2_9_18_1 doi: 10.1016/j.jtice.2021.11.016 – ident: e_1_2_9_37_1 doi: 10.1016/j.bej.2005.08.014 – ident: e_1_2_9_6_1 doi: 10.1016/j.ces.2016.04.004 – ident: e_1_2_9_17_1 doi: 10.1007/s00231-012-1056-0 – ident: e_1_2_9_45_1 doi: 10.1002/aic.690250513 – ident: e_1_2_9_7_1 doi: 10.1021/ie970275w – volume: 73 start-page: 280 issue: 3 year: 1995 ident: e_1_2_9_13_1 article-title: Influence of viscosity and foaming properties on heat‐transfer in packed‐bed with cocurrent upflow of gas and liquid publication-title: Chem Eng Res Des – ident: e_1_2_9_27_1 doi: 10.1016/j.cej.2019.122993 – ident: e_1_2_9_30_1 doi: 10.1002/jctb.3783 – ident: e_1_2_9_36_1 doi: 10.1021/ie050402l – ident: e_1_2_9_3_1 doi: 10.1021/acs.est.7b04905 – ident: e_1_2_9_50_1 doi: 10.1016/0009-2509(94)00290-8 – ident: e_1_2_9_42_1 doi: 10.1016/j.ces.2015.01.013 – ident: e_1_2_9_9_1 doi: 10.1021/acs.iecr.7b00123 – ident: e_1_2_9_38_1 doi: 10.1021/ie0494925 – ident: e_1_2_9_16_1 doi: 10.1017/S002211201000443X – ident: e_1_2_9_10_1 doi: 10.1002/aic.16624 – ident: e_1_2_9_15_1 doi: 10.1111/j.1745-6592.1999.tb00211.x – ident: e_1_2_9_23_1 doi: 10.1039/C4RA01852D – ident: e_1_2_9_35_1 doi: 10.1021/ie0108301 – ident: e_1_2_9_49_1 doi: 10.1016/j.cej.2005.03.009 – ident: e_1_2_9_8_1 doi: 10.1252/jcej.9.29 – ident: e_1_2_9_19_1 doi: 10.1016/j.bej.2016.11.014 – ident: 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Snippet | Packing size effects on the fluid dynamics in an external‐loop packed bubble column with Raschig rings of three different effective diameters (4.9, 14.1, and... |
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SubjectTerms | Bubble columns Column packings Diameters external‐loop packed bubble column Fluid dynamics gas holdup gas–liquid mass transfer Hydrodynamics liquid circulation Mass transfer Packing Porous media porous medium Size effects Thermal expansion Velocity |
Title | Packing size effects on the liquid circulation property in an external‐loop packed bubble column |
URI | https://onlinelibrary.wiley.com/doi/abs/10.1002%2Faic.17851 https://www.proquest.com/docview/2735474291 |
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