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Predicate | Object |
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rdf:type | |
lifeskim:mentions | |
pubmed:issue |
1-2
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pubmed:dateCreated |
1991-10-28
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pubmed:abstractText |
Factors influencing the operation of a vertical bioreactor segmented with perforated plates supporting immobilized yeast cells were studied. It was found that the most important factors are the length-diameter (L/D) ratio of the reactor and the dilution rate. It was supposed that the optimal L/D ratio is about 1. The operation of the reactor was more favourable at a low liquid phase-solid phase ratio. The spatial distribution of the biocatalyst had only a slight, if any effect. The periodically changed direction of feed flow has no improving effect on the fermentation process.
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pubmed:language |
eng
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pubmed:journal | |
pubmed:citationSubset |
IM
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pubmed:chemical | |
pubmed:status |
MEDLINE
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pubmed:issn |
0237-6261
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pubmed:author | |
pubmed:issnType |
Print
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pubmed:volume |
25
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pubmed:owner |
NLM
|
pubmed:authorsComplete |
Y
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pubmed:pagination |
9-16
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pubmed:dateRevised |
2006-11-15
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pubmed:meshHeading |
pubmed-meshheading:2130575-Cell Division,
pubmed-meshheading:2130575-Chromatography, Gas,
pubmed-meshheading:2130575-Culture Media,
pubmed-meshheading:2130575-Ethanol,
pubmed-meshheading:2130575-Fermentation,
pubmed-meshheading:2130575-Industrial Microbiology,
pubmed-meshheading:2130575-Saccharomyces cerevisiae
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pubmed:year |
1990
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pubmed:articleTitle |
Factors influencing the operation of a vertical bioreactor segmented with perforated plates.
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pubmed:affiliation |
Department of Biochemistry, József Attila University, Szeged, Hungary.
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pubmed:publicationType |
Journal Article,
Research Support, Non-U.S. Gov't
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