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Title: Chemical hydrodynamics of a downward microbubble flow for intensification of gas‐fed bioreactors

Abstract

Bioreactors are of interest for value‐upgrading of stranded or waste industrial gases. Reactor intensification requires development of low cost bioreactors with fast gas–liquid mass transfer rate. Here we assess published reactor technology in comparison with a novel downward bubble flow created by a micro‐jet array. Compared to known technology, the advanced design achieves higher volumetric gas transfer efficiency (k L a per power density) and can operate at higher k L a. We measure the effect of four reactor heights (height‐to‐diameter ratios of 12, 9, 6, and 3) on the gas transfer coefficient k L , total interfacial area a, liquid residence time distribution, energy consumption, and turbulent hydrodynamics. Leading models for predicting k L and a are appraised with experimental data. The results show k L is governed by “entrance effects” due to Higbie penetration dominate at short distances below the micro‐jet array, while turbulence dominates at intermediate distances, and finally terminal rise velocity dominates at large distances. © 2017 American Institute of Chemical Engineers AIChE J , 64: 1399–1411, 2018

Authors:
 [1]; ORCiD logo [1];  [1];  [1];  [1];  [1]; ORCiD logo [2]
  1. Dept. of Chemical Engineering, The City College of New York CUNY Energy Institute New York NY 10031
  2. Homi Bhabha National Institute, Anushaktinagar Mumbai 400094 India, Dept. of Chemical Engineering Institute of Chemical Technology Mumbai 400019 India
Publication Date:
Sponsoring Org.:
USDOE
OSTI Identifier:
1405215
Resource Type:
Publisher's Accepted Manuscript
Journal Name:
AIChE Journal
Additional Journal Information:
Journal Name: AIChE Journal Journal Volume: 64 Journal Issue: 4; Journal ID: ISSN 0001-1541
Publisher:
Wiley Blackwell (John Wiley & Sons)
Country of Publication:
United States
Language:
English

Citation Formats

Ansari, Manizheh, Turney, Damon E., Yakobov, Roman, Kalaga, Dinesh V., Kleinbart, Simon, Banerjee, Sanjoy, and Joshi, Jyeshtharaj B. Chemical hydrodynamics of a downward microbubble flow for intensification of gas‐fed bioreactors. United States: N. p., 2017. Web. doi:10.1002/aic.16002.
Ansari, Manizheh, Turney, Damon E., Yakobov, Roman, Kalaga, Dinesh V., Kleinbart, Simon, Banerjee, Sanjoy, & Joshi, Jyeshtharaj B. Chemical hydrodynamics of a downward microbubble flow for intensification of gas‐fed bioreactors. United States. https://doi.org/10.1002/aic.16002
Ansari, Manizheh, Turney, Damon E., Yakobov, Roman, Kalaga, Dinesh V., Kleinbart, Simon, Banerjee, Sanjoy, and Joshi, Jyeshtharaj B. Fri . "Chemical hydrodynamics of a downward microbubble flow for intensification of gas‐fed bioreactors". United States. https://doi.org/10.1002/aic.16002.
@article{osti_1405215,
title = {Chemical hydrodynamics of a downward microbubble flow for intensification of gas‐fed bioreactors},
author = {Ansari, Manizheh and Turney, Damon E. and Yakobov, Roman and Kalaga, Dinesh V. and Kleinbart, Simon and Banerjee, Sanjoy and Joshi, Jyeshtharaj B.},
abstractNote = {Bioreactors are of interest for value‐upgrading of stranded or waste industrial gases. Reactor intensification requires development of low cost bioreactors with fast gas–liquid mass transfer rate. Here we assess published reactor technology in comparison with a novel downward bubble flow created by a micro‐jet array. Compared to known technology, the advanced design achieves higher volumetric gas transfer efficiency (k L a per power density) and can operate at higher k L a. We measure the effect of four reactor heights (height‐to‐diameter ratios of 12, 9, 6, and 3) on the gas transfer coefficient k L , total interfacial area a, liquid residence time distribution, energy consumption, and turbulent hydrodynamics. Leading models for predicting k L and a are appraised with experimental data. The results show k L is governed by “entrance effects” due to Higbie penetration dominate at short distances below the micro‐jet array, while turbulence dominates at intermediate distances, and finally terminal rise velocity dominates at large distances. © 2017 American Institute of Chemical Engineers AIChE J , 64: 1399–1411, 2018},
doi = {10.1002/aic.16002},
journal = {AIChE Journal},
number = 4,
volume = 64,
place = {United States},
year = {Fri Oct 27 00:00:00 EDT 2017},
month = {Fri Oct 27 00:00:00 EDT 2017}
}

Journal Article:
Free Publicly Available Full Text
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https://doi.org/10.1002/aic.16002

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Cited by: 15 works
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