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dc.contributor.authorBirgen, Cansu
dc.contributor.authorMarkussen, Sidsel
dc.contributor.authorWentzel, Alexander
dc.contributor.authorPreisig, Heinz A.
dc.date.accessioned2023-05-31T13:31:14Z
dc.date.available2023-05-31T13:31:14Z
dc.date.created2018-07-05T20:17:34Z
dc.date.issued2018
dc.identifier.citationChemical Engineering Transactions. 2018, 65, 61-66.en_US
dc.identifier.issn1974-9791
dc.identifier.urihttps://hdl.handle.net/11250/3069520
dc.description.abstractWe applied response surface methodology to understand the effect and extend of carbon catabolite repression (CCR) on growth of Clostridium beijerinckii NCIMB 8052 using xylose and glucose as representative lignocellulosic sugars. We performed batch growth experiments based on the central composite design with different concentrations of glucose and xylose, and estimated the respective growth rates as the response. Fitting the quadratic model with interaction coefficient to experimental data gave a good quality of fit (R-squared=0.939). We found that glucose is the most significant factor affecting the growth rate. Interaction between glucose and xylose is another highly significant factor. Response surface illustrated that increasing or decreasing both sugar concentrations at the same time results in a decreasing growth rate, and increasing either sugar concentration while decreasing the other sugar increases the growth rate. It is an important finding as it suggests that CCR can be not only from glucose on xylose but also from xylose on glucose. A transcriptional study will be necessary to understand the repression mechanism and to improve the utilization of sugars in mixed form, thus lignocellulosic fermentation processes.en_US
dc.language.isoengen_US
dc.publisherAIDICen_US
dc.titleResponse Surface Methodology for Understanding Glucose and Xylose Utilization by Clostridium beijerinckii NCIMB 8052en_US
dc.typePeer revieweden_US
dc.typeJournal articleen_US
dc.description.versionpublishedVersionen_US
dc.source.pagenumber61-66en_US
dc.source.volume65en_US
dc.source.journalChemical Engineering Transactionsen_US
dc.identifier.doi10.3303/CET1865011
dc.identifier.cristin1596013
dc.relation.projectNorges forskningsråd: 257622en_US
dc.relation.projectNorges forskningsråd: 521732en_US
cristin.ispublishedtrue
cristin.fulltextoriginal
cristin.qualitycode1


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