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Jeenat Aslam,Umme Salma Siddiqui,Imtiyaz Ahmad Bhat,Kabir-ud-Din 한국공업화학회 2014 Journal of Industrial and Engineering Chemistry Vol.20 No.5
In the present study, mixtures of cationic gemini surfactants with a non-ionic sugar-based surfactant in aqueous solutions containing electrolyte (NaBr) have been studied. The experimental results were evaluated using the Regular Solution Theory. The strength of interaction of all the surfactants is attributed to the sterical and electrical factors on mixed monolayer and micelle formation and of surfactant–surfactant interactions. The results show stronger interaction at the air/water interface and greater preference for adsorbing at the air/water interface relative to mixed micelle formation in the solution phase. The alkyl chain length and spacer of gemini govern the aggregation behavior of the mixed micelles.
( Ju Yi Park ),( Soon Kwang Hong ),( Yong Keun Chang ) 한국미생물 · 생명공학회 2014 Journal of microbiology and biotechnology Vol.24 No.12
DagA, a β-agarase, was produced by cultivating a recombinant Streptomyces lividans in a glucose medium or a mixed-sugar medium simulating microalgae hydrolysate. The optimum composition of the glucose medium was identified as 25 g/l glucose, 10 g/l yeast extract, and 5 g/l MgCl2·6H2O. With this, a DagA activity of 7.26 U/ml could be obtained. When a mixedsugar medium containing 25 g/l of sugars was used, a DagA activity of 4.81 U/ml was obtained with very low substrate utilization efficiency owing to the catabolic repression of glucose against the other sugars. When glucose and galactose were removed from the medium, an unexpectedly high DagA activity of about 8.7 U/ml was obtained, even though a smaller amount of sugars was used. It is recommended for better substrate utilization and process economics that glucose and galactose be eliminated from the medium, by being consumed by some other useful applications, before the production of DagA.
Lebaka Veeranjaneya Reddy,박준혁,위영중 한국생물공학회 2015 Biotechnology and Bioprocess Engineering Vol.20 No.6
In the present study, lactic acid fermentation was carried out by batch culture of Enterococcus faecalis RKY1 using sucrose and mixed sugars as the major substrate. Maximum lactic acid productivity (5.2 g/L/h) was recorded when 50 and 100 g/L of sucrose were used as a carbon source. Sucrose concentration higher than 150 g/L resulted in the decrease of lactic acid productivity due to inhibition by high substrate concentration, but lactic acid productivity was remained > 3.0 g/L/h until the sucrose used for lactic acid fermentation increased up to 150 g/L. L-Lactic acid content of the total lactic acid produced from sucrose and mixed sugars was higher than 98%. When the fermentation media contained sucrose, the kinetic parameters showing specific rates such as μ, qS, and qP were relatively lower than those of fermentation using glucose as a sole carbon source, which might be due to additional time requirement to induce invertase enzyme for utilization of sucrose. There was no carbon catabolite repression observed when the sugar mixtures containing sucrose, glucose, and/ or fructose were used as a carbon source for lactic acid fermentation by E. faecalis RKY1.
Lim, W.S.,Lee, J.W. Elsevier Applied Science 2013 Bioresource technology Vol.140 No.-
In this study, the effects of different acid catalysts and pretreatment factors on the hydrolysis of mixed softwood were investigated over a range of thermochemical pretreatments. Maleic, oxalic, and sulfuric acids were each used, under different pretreatment conditions. The most influential factor for fermentable sugar production in the dicarboxylic acid pretreatment of softwood was the pH. Reaction temperature was the next significant factor. However, during sulfuric acid pretreatment, fermentable sugar production was more dependent on reaction temperature, than time or pH. Enzymatic hydrolysis yields differed, depending on acid catalyst and pretreatment factor, regardless of lignin content in pretreated biomass. The highest enzymatic hydrolysis yield was found following maleic acid pretreatment, which reached 61.23%. The trend in enzymatic hydrolysis yields that were detected concomitantly with pretreatment condition or type of acid catalyst was closely related to the fermentable sugar production in the hydrolysate.
Pichia stipitis에 의한 Glucose, Xylose 및 Cellobiose의 발효
이유석,권윤중,변유량 한국산업미생물학회 1992 한국미생물·생명공학회지 Vol.20 No.1
Xylose와 cellobiose를 모두 발효할 수 있는 효모를 선발한 결과 Pichia stipitis CBS 5775와 5776이 가장 우수하였다. P. stipitis CBS 5776은 glucose, xylose 및 cellobiose에서 각각 0.4, 0.36 및 0.23g/g substrate의 에탄올 수율을 나타내었다. 혼합당에서의 발효결과 glucose는 xylose와 cellobiose 이용에 대하여 catabolite regulation을 일으켜서 glucose가 다 소비된 후에 다른 기질이 소비되었다. 그러나 xylose와 cellobiose는 동시에 소비되었다. 혼합기질에서의 에탄올 수율은 단일기질에서의 각각의 수율의 합과 거의 유사하였다. The hydrolyzates of lignocellulosic biomass contain a mixture of glucose, xylose and cellobiose. The yeast which can produce ethanol efficiently from xylose and cellobiose was selected and its growth and ethanol formation behavior on each sugar and their mixture were investigated. Ethanol yields during batch culture of Pichia stipitis CBS 5776 were 0.4, 0.36 and 0.23 g/g substrate on glucose, xylose and cellobiose, respectively Mixed sugar fermentation data indicate that glucose causes catabolite regulation on xylose and cellobiose utilization. However, xylose and cellobiose were utilized simultaneously. Ethanol yields on mixtures of sugars were generally additive for each of the substrates.
( Yong Cheol Park ),( Hae Jin Lee ),( Chang Sup Kim ),( Jin Ho Seo ) 한국미생물 · 생명공학회 2013 Journal of microbiology and biotechnology Vol.23 No.4
D-Ribose is a value-added five-carbon sugar used for riboflavin production. To investigate the effects of oxygen supply and mixed sugar concentration on microbial production of D-ribose, a transketolase-deficient Bacillus subtilis SPK1 was cultured batch-wise using xylose and glucose. A change of agitation speed from 300 rpm to 600 rpm at 1 vvm of air supply increased both the xylose consumption rate and D-ribose production rate. Because the sum of the specific consumption rates for xylose and glucose was similar at all agitation speeds, metabolic preferences between xylose and glucose might depend on oxygen supply. Although B. subtilis SPK1 can take up xylose and glucose by the active transport mechanism, a high initial concentration of xylose and glucose was not beneficial for high D-ribose production.