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Performance of trickle-bed bioreactors for converting synthesis gas to methane.

作者信息

Kimmel D E, Klasson K T, Clausen E C, Gaddy J L

机构信息

University of Arkansas, Department of Chemical Engineering, Fayetteville 72701.

出版信息

Appl Biochem Biotechnol. 1991 Spring;28-29:457-69. doi: 10.1007/BF02922625.

DOI:10.1007/BF02922625
PMID:1929378
Abstract

Carbon monoxide, H2, and CO2 in synthesis gas can be converted to CH4 by employing a triculture of Rhodospirillum rubrum, Methanosarcina barkeri, and Methanobacterium formicicum. Trickle-bed reactors have been found to be effective for this conversion because of their high mass-transfer coefficients. This paper compares results obtained for the conversion of synthesis gas to CH4 in 5-cm- and 16.5-cm-diameter trickle-bed reactors. Mass-transfer and scale-up parameters are defined, and light requirements for R. rubrum are considered in bioreactor design.

摘要

相似文献

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本文引用的文献

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气体发酵:细胞工程的可能性及放大
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Single-carbon catabolism in acetogens: analysis of carbon flow in Acetobacterium woodii and Butyribacterium methylotrophicum by fermentation and 13C nuclear magnetic resonance measurement.产乙酸菌中的一碳分解代谢:通过发酵和¹³C核磁共振测量分析木醋杆菌和甲基营养丁酸杆菌中的碳流
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Methanogens and the diversity of archaebacteria.产甲烷菌与古细菌的多样性
Microbiol Rev. 1987 Mar;51(1):135-77. doi: 10.1128/mr.51.1.135-177.1987.