Abstract:Twelve lactose-assimilating strains of the yeast species Kluyveromyces marxianus and its varieties marxianus, lactis and bulgaricus were studied with respect to transport mechanisms for lactose, glucose and galactose, fermentation of these sugars and the occurrence of extracellular lactose hydrolysis. The strains fell into three groups. Group I (two strains): Fermentation of lactose, glucose and galactose, extracellular lactose hydrolysis, apparent facilitated diffusion of glucose and galactose; Group II (two … Show more
“…16 In other Kluyveromyces species lactose uptake has also been described to proceed via a proton symport mechanism. [19][20][21] Lac12p shows sequence similarity to the E. coli xylose and arabinose proton symporters 15 and a significant sequence and structure homology with the S. cerevisiae maltose proton symporter Mal61p, 22 but no significant sequence similarity with the lactose permease (lacY gene) of E. coli. 15 The β-galactosidase (lactase) is encoded by the LAC4 gene 23 and is described to be intracellular.…”
Lactose is an interesting carbon source for the production of several bio-products by fermentation, primarily because it is the major component of cheese whey, the main by-product of dairy activities. However, the microorganism more widely used in industrial fermentation processes, the yeast Saccharomyces cerevisiae, does not have a lactose metabolization system. Therefore, several metabolic engineering approaches have been used to construct lactose-consuming S. cerevisiae strains, particularly involving the expression of the lactose genes of the phylogenetically related yeast Kluyveromyces lactis, but also the lactose genes from Escherichia coli and Aspergillus niger, as reviewed here. Due to the existing large amounts of whey, the production of bio-ethanol from lactose by engineered S. cerevisiae has been considered as a possible route for whey surplus. Emphasis is given in the present review on strain improvement for lactose-to-ethanol bioprocesses, namely flocculent yeast strains for continuous high-cell-density systems with enhanced ethanol productivity.
“…16 In other Kluyveromyces species lactose uptake has also been described to proceed via a proton symport mechanism. [19][20][21] Lac12p shows sequence similarity to the E. coli xylose and arabinose proton symporters 15 and a significant sequence and structure homology with the S. cerevisiae maltose proton symporter Mal61p, 22 but no significant sequence similarity with the lactose permease (lacY gene) of E. coli. 15 The β-galactosidase (lactase) is encoded by the LAC4 gene 23 and is described to be intracellular.…”
Lactose is an interesting carbon source for the production of several bio-products by fermentation, primarily because it is the major component of cheese whey, the main by-product of dairy activities. However, the microorganism more widely used in industrial fermentation processes, the yeast Saccharomyces cerevisiae, does not have a lactose metabolization system. Therefore, several metabolic engineering approaches have been used to construct lactose-consuming S. cerevisiae strains, particularly involving the expression of the lactose genes of the phylogenetically related yeast Kluyveromyces lactis, but also the lactose genes from Escherichia coli and Aspergillus niger, as reviewed here. Due to the existing large amounts of whey, the production of bio-ethanol from lactose by engineered S. cerevisiae has been considered as a possible route for whey surplus. Emphasis is given in the present review on strain improvement for lactose-to-ethanol bioprocesses, namely flocculent yeast strains for continuous high-cell-density systems with enhanced ethanol productivity.
“…Strains of Kluyveromyces or their synonyms, K. fragilis and Saccharomyces fragilis, have been considered the most suitable for bio-conversion of lactose in whey [2,4,20]. However, incomplete or slow fermentations have been observed for many Kluyveromyces strains, when concentrated whey or lactose-enriched substrates have been employed [12,32].…”
A strain of Kluyveromyces marxianus was grown in batch culture in lactose-based media at varying initial lactose concentrations (10-60 g L(-1)) at 30 degrees C, pH 5.0, dissolved oxygen concentrations greater than 20%. Increasing the concentration of mineral salts three-fold at 40 g L(-1) and 60 g L(-1) initial lactose concentration showed only a small increase in the yield of biomass, from 0.38 g g(-1) to 0.41 g g(-1), indicating that the initial batch cultures were not significantly nutrient- (mineral salts)-limited. A relatively high biomass concentration (105 g L(-1)) was obtained in fed-batch culture following extended lactose feeding. An average specific growth rate (0.27 h(-1)), biomass yield (0.38 g g(-1)) and overall productivity (2.9 g L(-1) h(-1)) were obtained for these fed-batch conditions. This fed-batch protocol provides a strategy for achieving relatively high concentrations and productivities of K. marxianus on other lactose-based substrate streams (e.g., whey) from the dairy industry.
“…Lactose utilisation in fungi takes place by two ways. Lactose is either hydrolysed extracellularly before or in connection with uptake and the product glucose and galactose are taken up (MORTBERG and NEUJAHR 1986, CARVALHO-SILVA andSPENCER-MARTINS 1990), or lactose is transported into the cell and hydrolysed intracellularly (CAR- VALHO-SILVA and SPENCER-MARTINS 1990, BOZE et al 1987, DICKSON and BARR 1983.Previously we have purified and characterised an intracellular enzyme with β-galactosidase activity (NAGY et al 2001) which implies that in our strain lactose is probably utilised by the consecutive action of lactose permease and β-galactosidase.Here we present our recent results on the production of β-galactosidase and the influence of different carbon sources on the biosynthesis of the enzyme.…”
Growth and β‐galactosidase activity of the penicillin producer industrial Penicillium chrysogenum NCAIM 00237 strain were examined using different carbon sources. Good growth was observed using glucose, sucrose, glycerol and galactose, while growth on lactose was substantially slower. β‐Galactosidase activity was high on lactose and very low on all the other carbon sources tested. In glucose grown cultures after exhaustion of glucose as repressing carbon source a derepressed low level of the enzyme was observed. cAMP concentration in lactose grown cultures was relatively high, in glucose grown cultures was low. Caffeine substantially decreased glucose consumption and growth but did not increase β‐galactosidase activity and did not prevent glucose repression which rules out the involvement of cAMP in the regulation of β‐galactosidase biosynthesis in Penicillium chrysogenum.
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