Residential College | false |
Status | 已發表Published |
A trickling fibrous-bed bioreactor for biofiltration of benzene in air | |
Zhou Q.1; Huang Y.L.1; Tseng D.-H.1; Shim H.1; Yang S.-T.1 | |
1998-12-01 | |
Source Publication | Journal of Chemical Technology and Biotechnology |
ISSN | 02682575 |
Volume | 73Issue:4Pages:359-368 |
Abstract | A novel trickling fibrous-bed bioreactor was developed for biofiltration to remove pollutants present in contaminated air. Air containing benzene as the sole carbon source was effectively treated with a coculture of Pseudomonas putida and Pseudomonas fIuorescens immobilized in the trickling biofilter, which was wetted with a liquid medium containing only inorganic mineral salts. When the inlet benzene concentration (C(gl)) was 0.37 g m, the benzene removal efficiency in the biofilter was greater than 90% at an empty bed retention time (EBRT) of 8 min or a superficial air flow rate of 1.8 m m h. In general, the removal efficiency decreased but the elimination capacity of the biofilter increased with increasing the inlet benzene concentration and the air (feed) flow rate. It was also found that the removal efficiency decreased but the elimination capacity increased with an increase in the loading capacity, which is equal to the inlet concentration divided by EBRT. The maximum elimination capacity achieved in this study was ~11.5 g m h when the inlet benzene concentration was 1.7 g m and the superficial air flow rate was 3.62 m m h. A simple mathematical model based on the first-order reaction kinetics was developed to simulate the biofiltration performance. The apparent first order parameter K in this model was found to be linearly related to the inlet benzene concentration (K = 4.64 - 1.38 C(gl)). The model can be used to predict the benzene removal efficiency and elimination capacity of the biofilter for benzene loading capacity up to ~30 g m h. Using this model, the maximum elimination capacity for the biofilter was estimated to be 12.3 g m h, and the critical loading capacity was found to be 14 g m h. The biofilter had a fast response to process condition changes and was stable for long-term operation; no degeneration or clogging of the biofilter was encountered during the 3-month period studied. The biofilter also had a relatively low pressure drop of 750 Pa m at a high superficial air flow rate of 7.21 m m h, indicating a good potential for further scale up for industrial applications. |
Keyword | Benzene Biofiltration Trickling Fibrous-bed Bioreactor |
DOI | 10.1002/(SICI)1097-4660(199812)73:4<359::AID-JCTB970>3.0.CO;2-V |
URL | View the original |
Language | 英語English |
WOS ID | WOS:000077605900006 |
Scopus ID | 2-s2.0-0032403621 |
Fulltext Access | |
Citation statistics | |
Document Type | Journal article |
Collection | University of Macau |
Affiliation | 1.Ohio State University 2.Tongji University 3.National Central University Taiwan |
Recommended Citation GB/T 7714 | Zhou Q.,Huang Y.L.,Tseng D.-H.,et al. A trickling fibrous-bed bioreactor for biofiltration of benzene in air[J]. Journal of Chemical Technology and Biotechnology, 1998, 73(4), 359-368. |
APA | Zhou Q.., Huang Y.L.., Tseng D.-H.., Shim H.., & Yang S.-T. (1998). A trickling fibrous-bed bioreactor for biofiltration of benzene in air. Journal of Chemical Technology and Biotechnology, 73(4), 359-368. |
MLA | Zhou Q.,et al."A trickling fibrous-bed bioreactor for biofiltration of benzene in air".Journal of Chemical Technology and Biotechnology 73.4(1998):359-368. |
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