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Received February 15, 2021
Accepted April 23, 2021
- This is an Open-Access article distributed under the terms of the Creative Commons Attribution Non-Commercial License (http://creativecommons.org/licenses/bync/3.0) which permits unrestricted non-commercial use, distribution, and reproduction in any medium, provided the original work is properly cited.
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Prediction of gas holdup in various types of airlift reactors
Department of Chemical and Biological Engineering, Hanbat National University, 125, Dongseodaero, Yoseong-gu, Daejeon 305719, Korea
khchoi@hanbat.ac.kr
Korean Journal of Chemical Engineering, September 2021, 38(9), 1781-1790(10), 10.1007/s11814-021-0822-4
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Abstract
Useful correlations were derived for the prediction of available gas holdup data in air water systems, using the operational and geometric parameters of airlift reactors only. To successfully consider the geometric difference between various types of airlift reactors, the characteristic distance (Dch) and the gas separation area (As) were defined as geometric parameters, respectively. The riser gas holdup (εr) in various types of airlift reactors was satisfactorily correlated with the operational and geometric parameters, such as the riser superficial gas velocity (UGr), a parameter containing the ratio of the top clearance to downcomer length (1+Ct/Ld), the characteristic distance to downcomer length ratio (Dch/Ld), the downcomer to riser cross-sectional area ratio (Ad/Ar), the ratio of the gas separation area to riser cross-sectional area (As/Ar), and the bottom to downcomer cross-sectional area ratio (Ab/Ad). The downcomer gas holdup in various types of airlift reactors was well correlated by a nonlinear equation involving εr, Dch/Ld, Ad/Ar, Ab/Ad, (1+Ct/Ld), and As/Ar.
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Blazej M, Glover GMC, Generalis SC, Markos J, Chem. Eng. Process., 43(2), 137 (2004)
Douek RS, Livingston AG, Hewitt GF, AIChE J., 41(11), 2508 (1995)
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Bello RA, Robinson CW, Moo-Young M, Can. J. Chem. Eng., 62, 573 (1984)
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Philip J, Proctor JM, Niranjan K, Davidson JF, Chem. Eng. Sci., 45, 651 (1990)
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Kojic PS, Tokic MS, Sijacki IM, Lukic NL, Petrovic DL, Jovicevic DZ, Popovic SS, Chem. Eng. Technol., 38(4), 701 (2015)
Luo LJ, Liu FN, Xu YY, Yuan JQ, Chem. Eng. J., 175, 494 (2011)
Sijacki IM, Tokic MS, Kojic PS, Petrovic DL, Tekic MN, Djuric MS, Milovancev SS, Ind. Eng. Chem. Res., 50, 6 (2011)
Fakhari ML, Moraveji MK, Davarnejad R, Chinese J. Chem. Eng., 22, 267 (2014)
Siegel MH, Merchuk JC, Schugerl K, AIChE J., 32, 1585 (1986)
Kojic PS, Popovic SS, Tokic MS, Sijacki IM, Lukic NL, Jovicevic DZ, Petrovic DL, Braz. J. Chem. Eng., 34, 493 (2017)
Choi KH, Korean Chem. Eng. Res., 58(4), 665 (2020)
Bello R, Robinson CW, Moo-Young M, Biotechnol. Bioeng., 27, 369 (1985)
Bentifraouine C, Xuereb C, Riba JP, J. Chem. Tech. Biotechnol., 69, 345 (1997)
Couvert A, Roustan M, Chatellier P, Chem. Eng. Sci., 54(21), 5245 (1999)
Al-Masry WA, Chem. Eng. Res. Des., 84(A6), 483 (2006)
Jones AG, Chem. Eng. Sci., 40, 449 (1985)
Wachi S, Jones AG, Elson TP, Chem. Eng. Sci., 46, 657 (1991)
Petrovic DL, Posarac D, Dudukovic A, Skala D, J. Serb. Chem. Soc., 56, 227 (1991)
Lu WJ, Hwang SJ, Chang CM, Chem. Eng. Sci., 50(8), 1301 (1995)
Blazej A, Kisa A, Markos J, Chem. Eng. Process., 43(12), 1519 (2004)
Popovic M, Robinson CW, Chem. Eng. Sci., 42, 2811 (1987)
AlMasry WA, Dukkan AR, Chem. Eng. J., 65(3), 263 (1997)
Bentifraouine C, Xuereb C, Riba JP, Chem. Eng. J., 66, 91 (1997)
Chisti MY, Halard B, Moo-Young M, Chem. Eng. Sci., 43, 451 (1988)
Chisti Y, Moo-Yong M, Chem. Eng. Process., 9, 38 (1993)
Chisti Y, Airlift bioreactors, Elsevier Applied Science, London (1989).
Choi KH, Chisti Y, Moo-Young M, Chem. Eng. J., 62, 223 (1996)