hydrodynamics;
aeration of bioreactor;
minimum fluidisation air velocity;
three-phase fluidised bed bioreactor;
low density biomass support;
D O I:
10.1016/S1369-703X(99)00016-9
中图分类号:
Q81 [生物工程学(生物技术)];
Q93 [微生物学];
学科分类号:
071005 ;
0836 ;
090102 ;
100705 ;
摘要:
The hydrodynamics of a gas-liquid-solid fluidised bed bioreactor with a low density biomass support (matrix density smaller than that of water) was investigated. In particular. a minimum fluidisation air velocity U-gf and an air holdup epsilon(g) were measured in a bioreactor with KMTR (Kaldnes Miljotechnologi AS) particles used as biomass support. It was found that values of U-gf depended on the ratio of bed (settled) volume to bioreactor volume (V-b/V-r) and the mass M-bp of cells grown on the particles. For a given mass M-bp the values of U-gf increased with an increase in the ratio of (V-b/V-r) The values of U-gf were strongly affected by the mass M-bp and decreased with an increase in Mbp There was a critical ratio (V-b/V-r)(er) above which movement of the whole bed was impossible: the particles either remained at the top of the bioreactor or settled at its bottom. The values of (V-b/V-r)(er) for which this was happening depended on the mass M-bp and decreased with an increase in M-bp. It was established that the air holdup epsilon(g) depended on the air velocity U-g, the ratio (V-b/V-r) and the mass M-bp. For a given ratio (V-b/V-r) and mass M-bp the values of epsilon(g) increased with an increase in the air velocity U-g. The optimal ratios (V-b/V-r)(o) for which the largest values of epsilon(g) were obtained depended on the mass M-bp. The values of (V-b/V-r)(o) decreased with an increase in M-bp. It was also established that the values of epsilon(g) obtained in a bioreactor with the KMTR particles were approximately 40% larger than those reported in the literature for bioreactors with other low density support media such as spheres and toroids. It was therefore concluded that the large values of the air holdup achieved with the KMTR particles merit their application as a biomass support for high-rate aerobic biological treatment of industrial and municipal wastewaters. (C) 1999 Elsevier Science S.A. All rights reserved.
机构:
China Univ Petr, State Key Lab Heavy Oil Proc, Beijing 102249, Peoples R China
China Univ Petr, China Natl Petr Corp, Key Lab Catalysis, Beijing 102249, Peoples R ChinaChina Univ Petr, State Key Lab Heavy Oil Proc, Beijing 102249, Peoples R China
Du, Wei
Zhang, Lifeng
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机构:
Univ Saskatchewan, Dept Chem & Biol Engn, Saskatoon, SK, CanadaChina Univ Petr, State Key Lab Heavy Oil Proc, Beijing 102249, Peoples R China
Zhang, Lifeng
Lv, Sha
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机构:
China Univ Petr, China Natl Petr Corp, Key Lab Catalysis, Beijing 102249, Peoples R ChinaChina Univ Petr, State Key Lab Heavy Oil Proc, Beijing 102249, Peoples R China
Lv, Sha
Lu, Panpan
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机构:
China Univ Petr, China Natl Petr Corp, Key Lab Catalysis, Beijing 102249, Peoples R ChinaChina Univ Petr, State Key Lab Heavy Oil Proc, Beijing 102249, Peoples R China
Lu, Panpan
Xu, Jian
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China Univ Petr, China Natl Petr Corp, Key Lab Catalysis, Beijing 102249, Peoples R ChinaChina Univ Petr, State Key Lab Heavy Oil Proc, Beijing 102249, Peoples R China
Xu, Jian
Wei, Weisheng
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China Univ Petr, China Natl Petr Corp, Key Lab Catalysis, Beijing 102249, Peoples R ChinaChina Univ Petr, State Key Lab Heavy Oil Proc, Beijing 102249, Peoples R China