Performance of Gas Induction in a Dual – Impeller Agitated Bioreactor

The rate of gas induction was measured in gas-inducing type mechanically agitated contactors provided with two impellers. A reactor of 0.5 m i.d. was used with a working capacity of 60 liters of liquid. Tap water was used as the liquid phase, and air was used as the gas phase. The bioreactor mixing...

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Autores principales: Alaa K. Mohammed, Hassanin Ali Hussen, Safa Abid Al-Rassul
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Lenguaje:EN
Publicado: Al-Khwarizmi College of Engineering – University of Baghdad 2008
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Acceso en línea:https://doaj.org/article/7a39dc41c3614b97b54027d218c608c4
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spelling oai:doaj.org-article:7a39dc41c3614b97b54027d218c608c42021-12-02T09:52:03ZPerformance of Gas Induction in a Dual – Impeller Agitated Bioreactor1818-11712312-0789https://doaj.org/article/7a39dc41c3614b97b54027d218c608c42008-12-01T00:00:00Zhttp://alkej.uobaghdad.edu.iq/index.php/alkej/article/view/604https://doaj.org/toc/1818-1171https://doaj.org/toc/2312-0789 The rate of gas induction was measured in gas-inducing type mechanically agitated contactors provided with two impellers. A reactor of 0.5 m i.d. was used with a working capacity of 60 liters of liquid. Tap water was used as the liquid phase, and air was used as the gas phase. The bioreactor mixing system consists of two equal diameter stirrers; the top impeller is shrouded-disk/curved-blade turbine with six evacuated bending blades, while the bottom impeller was disk turbine. The impeller speed was varied in the range of 50 to 800 rpm. The ratio of impeller diameter to tank diameter (D/T) and the submergence (S) of upper impeller from the top were varied. The effects of clearance of lower impeller from the tank bottom (C2) and the impeller spacing (C3, distance between the two impellers) were also varied over a wide range.  Rate of gas induction (Q) was measured for all these combinations. It was found that the rate of gas induction increases with both decreasing in submergence and increasing in the stirrer diameter. While it decreases with both increasing the impeller spacing and the clearance from the bottom. Alaa K. MohammedHassanin Ali HussenSafa Abid Al-RassulAl-Khwarizmi College of Engineering – University of BaghdadarticleChemical engineeringTP155-156Engineering (General). Civil engineering (General)TA1-2040ENAl-Khawarizmi Engineering Journal, Vol 4, Iss 4 (2008)
institution DOAJ
collection DOAJ
language EN
topic Chemical engineering
TP155-156
Engineering (General). Civil engineering (General)
TA1-2040
spellingShingle Chemical engineering
TP155-156
Engineering (General). Civil engineering (General)
TA1-2040
Alaa K. Mohammed
Hassanin Ali Hussen
Safa Abid Al-Rassul
Performance of Gas Induction in a Dual – Impeller Agitated Bioreactor
description The rate of gas induction was measured in gas-inducing type mechanically agitated contactors provided with two impellers. A reactor of 0.5 m i.d. was used with a working capacity of 60 liters of liquid. Tap water was used as the liquid phase, and air was used as the gas phase. The bioreactor mixing system consists of two equal diameter stirrers; the top impeller is shrouded-disk/curved-blade turbine with six evacuated bending blades, while the bottom impeller was disk turbine. The impeller speed was varied in the range of 50 to 800 rpm. The ratio of impeller diameter to tank diameter (D/T) and the submergence (S) of upper impeller from the top were varied. The effects of clearance of lower impeller from the tank bottom (C2) and the impeller spacing (C3, distance between the two impellers) were also varied over a wide range.  Rate of gas induction (Q) was measured for all these combinations. It was found that the rate of gas induction increases with both decreasing in submergence and increasing in the stirrer diameter. While it decreases with both increasing the impeller spacing and the clearance from the bottom.
format article
author Alaa K. Mohammed
Hassanin Ali Hussen
Safa Abid Al-Rassul
author_facet Alaa K. Mohammed
Hassanin Ali Hussen
Safa Abid Al-Rassul
author_sort Alaa K. Mohammed
title Performance of Gas Induction in a Dual – Impeller Agitated Bioreactor
title_short Performance of Gas Induction in a Dual – Impeller Agitated Bioreactor
title_full Performance of Gas Induction in a Dual – Impeller Agitated Bioreactor
title_fullStr Performance of Gas Induction in a Dual – Impeller Agitated Bioreactor
title_full_unstemmed Performance of Gas Induction in a Dual – Impeller Agitated Bioreactor
title_sort performance of gas induction in a dual – impeller agitated bioreactor
publisher Al-Khwarizmi College of Engineering – University of Baghdad
publishDate 2008
url https://doaj.org/article/7a39dc41c3614b97b54027d218c608c4
work_keys_str_mv AT alaakmohammed performanceofgasinductioninadualimpelleragitatedbioreactor
AT hassaninalihussen performanceofgasinductioninadualimpelleragitatedbioreactor
AT safaabidalrassul performanceofgasinductioninadualimpelleragitatedbioreactor
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