Construction of lactose-consuming Saccharomyces cerevisiae for lactose fermentation into ethanol fuel

Two lactose-consuming diploid Saccharomyces cerevisiae strains, AY-51024A and AY-51024M, were constructed by expressing the LAC4 and LAC12 genes of Kluyveromyces marxianus in the host strain AY-5. In AY-51024A, both genes were targeted to the ATH1 and NTH1 gene-encoding regions to abolish the activity of acid/neutral trehalase. In AY-51024M, both genes were respectively integrated into the MIG1 and NTH1 gene-encoding regions to relieve glucose repression. Physiologic studies of the two transformants under anaerobic cultivations in glucose and galactose media indicated that the expression of both LAC genes did not physiologically burden the cells, except for AY-51024A in glucose medium. Galactose consumption was initiated at higher glucose concentrations in the MIG1 deletion strain AY-51024M than in the corresponding wild-type strain and AY-51024A, wherein galactose was consumed until glucose was completely depleted in the mixture. In lactose medium, the Sp. growth rates of AY-51024A and AY-51024M under anaerobic shake-flasks were 0.025 and 0.067 h^?1, respectively. The specific lactose uptake rate and ethanol production of AY-51024M were 2.50 g lactose g CDW^?1 h^?1 and 23.4 g l^?1, respectively, whereas those of AY-51024A were 0.98 g lactose g CDW^?1 h^?1 and 24.3 g lactose g CDW^?1 h^?1, respectively. In concentrated cheese whey powder solutions, AY-51024M produced 63.3 g l^?1 ethanol from approximately 150 g l^?1 initial lactose in 120 h, conversely, AY-51024A consumed 63.7 % of the initial lactose and produced 35.9 g l^?1 ethanol. Therefore, relieving glucose repression is an effective strategy for constructing lactose-consuming S. cerevisiae.     

Derepression of galactose metabolism in melibiase producing bakers' and distillers' yeast

Beet molasses is widely used as a growth substrate for bakers' and distillers' yeast in the production of biomass and ethanol. Most commercial yeasts do not fully utilise the carbohydrates in molasses since they are incapable of hydrolysing the disaccharide melibiose to glucose and galactose. Also, expression of genes encoding enzymes for the utilisation of carbon sources that are alternatives to glucose is tightly regulated, sometimes rates of yeast growth and/or ethanol production. The GAL genes are regulated by specific induction by galactose and repression during growth on glucose. In an industrial distillers' yeast, two genes interacting synergistically in glucose repression of galactose utilization, MIG1 and GAL80, have been disrupted with MEL1, encoding melibiase. The physiology of the wild-type strain and the recombinant strains was investigated on mixtures of glucose and galactose and on molasses. The recombinant strain started to ferment galactose when 9.7 g 1(-1) glucose was still present during a batch fermentation, whereas the wild-type strain did not consume any galactose in the presence of glucose. The ethanol yield in the recombinant strain was 0.50 g ethanol g sugar (-1) in an ethanol fermentation on molasses, compared with 0.48 g ethanol g sugar (-1) for the wild-type strain. The increased ethanol yield was due to utilization of melibiose in the molasses.     

Alcohol production by selected yeast strains in lactase-hydrolyzed acid whey

Ethanol production by Kluyveromyces fragilis and Saccharomyces cerevisiae was studied using cottage cheese whey in which 80 to 90% of the lactose present had been prehydrolyzed to glucose and galactose. Complete fermentation of the sugar by K. fragilis required 120 hr at 30°C in lactase-hydrolyzed whey compared to 72 hr in nonhydrolyzed whey. This effect was due to a diauxic fermentation pattern in lactase-hydrolyzed whey with glucose being fermented before galactose. Ethanol yields of about 2% were obtained in both types of whey when K. fragilis was the organism used for fermentation. Saccharomyces cerevisiae produced alcohol from glucose more rapidly than K. fragilis, but galactose was fermented only when S. cerevisiae was pregrown on galactose. Slightly lower alcohol yields were obtained with S. cerevisiae, owing to the presence of some lactose in the whey which was not fermented by this organism. Although prehydrolysis of lactose in whey and whey fractions is advantageous in that microbial species unable to ferment lactose may be utilized, diauxie and galactose utilization problems must be considered.     

Alcohol production from cheese whey permeate using genetically modified flocculent yeast cells.

Alcoholic fermentation of cheese whey permeate was investigated using a recombinant flocculating Saccharomyces cerevisiae, expressing the LAC4 (coding for beta-galactosidase) and LAC12 (coding for lactose permease) genes of Kluyveromyces marxianus enabling for lactose metabolization. Data on yeast fermentation and growth on cheese whey permeate from a Portuguese dairy industry is presented. For cheese whey permeate having a lactose concentration of 50 gL(-1), total lactose consumption was observed with a conversion yield of ethanol close to the expected theoretical value. Using a continuously operating 5.5-L bioreactor, ethanol productivity near 10 g L(-1) h(-1) (corresponding to 0.45 h(-1) dilution rate) was obtained, which raises new perspectives for the economic feasibility of whey alcoholic fermentation. The use of 2-times concentrated cheese whey permeate, corresponding to 100 gL(-1) of lactose concentration, was also considered allowing for obtaining a fermentation product with 5% (w/v) alcohol.     

Use ofClostridium acetobutylicum P262 for production of solvents from whey permeate

Summary The production of solvents from whey permeate in batch fermentation usingClostridium acetobutylicum P262 was examined. An overall reactor productivity of 0.24 g/l.h was observed, representing a marked improvement over reports using other strains of clostridia. Using a semi-synthetic medium galactose was shown to be as effective a substrate as glucose. When whey permeate was used in which the lactose was hydrolysed prior to fermentation, preferential uptake of glucose over galactose was observed, and such hydrolysis provided no advantage to the fermentation process.     

Whey disposal by deproteinization and fermentation

The non-pollutant plant support material of the dwarf duckweed Wolffia arrhiza (Fam. Lemnaceae) was used for the entrapment of living yeast cells (Kluyveromyces fragilis) which hydrolyse lactose with the subsequent fermentation of glucose and galactose at high cell densities (up to 7.0 × 10⁸/ml support). The stabile yeast-plant cell immobilizates are able to produce ethanol from lactose-containing media (e.g. whey) by batch fermentation (on a rotary shaker) or continuous fermentation (in a turbulence reactor) for several days (at a pH below 4.2 and a temperature of 30°C). The removal of whey proteins by a preceding heat denaturation of whey, high dilution rates, C_So values of 50 to 60 g lactose per litre whey and the preferential use of the K. fragilis strain DSM 7238 were determined as the prerequisites for an optimum continuous fermentation. Economically interesting productivities (P_max ? 15 g ethanol/1 · h, D = 0.72 h^?1) with an actual lactose turnover of 90% were obtained by using these parameters.     

Improved ethanol production from whey with Saccharomyces cerevisiae using permeabilized cells of Kluyveromyces marxianus

Permeabilized cells of Kluyveromyces marxianus CCY eSY2 were tested as the source of lactase in the ethanol fermentation of concentrated deproteinized whey (65–70 g/l lactose) by Saccharomyces cerevisiae CCY 10–13–14. Rapid lactose hydrolysis by small amounts of permeabilized cells following the fermentation of released glucose and galactose by S. cerevisiae resulted in a twofold enhancement of the overall volumetric productivity (1.03 g/l × h), compared to the fermentation in which the lactose was directly fermented by K. marxianus.     

Acetic acid production from whey lactose by the co-culture ofStreptococcus lactis andClostridium formicoaceticum

Summary Acetic acid was produced from anaerobic fermentation of lactose by the co-culture ofStreptococcus lactis andClostridium formicoaceticum at 35° C and pHs between 7.0 and 7.6. Lactose was converted to lactic acid, and then to acetic acid in this mixed culture fermentation. The overall acetic acid yield from lactose was about 95% at pH 7.6 and 90% at pH 7.0. The fermentation rate was also higher at pH 7.6 than at pH 7.0. In batch fermentation of whey permeate containing about 5% lactose at pH 7.6, the concentration of acetic acid reached 20 g/l within 20 h. The production rate then became very slow due to end-product inhibition and high Na⁺ concentration. About 30 g/l acetate and 20 g/l lactate were obtained at a fermentation time of 80 h. However, when diluted whey permeate containing 2.5% lactose was used, all the whey lactose was converted to acetic acid within 30 h by this mixed culture.     

Butanol from whey ultrafiltrate: batch experiments with Clostridium beyerinckii LMD 27.6

Summary For batch fermentations by Clostridium beyerinckii LMD 27.7 (formerly known as Clostridium butylicum) whey ultrafiltrate, glucose, lactose, and galactose were used as substrates. The aims of the experiments were to find the conditions for butanol production from whey ultrafiltrate and to compare the results with those of other substrates. The conditions necessary for butanol production were established. The mean solvent productivity found on whey ultrafiltrate fermentation was two to three times lower than that found on glucose; the overall solvent yields were comparable. Butanol production from galactose and mixtures of glucose and galactose was also possible.     

Fermentation of lactose by yeast cells secreting recombinant fungal lactase.

Strains of Saccharomyces cerevisiae transformed with a yeast multicopy expression vector carrying the cDNA for Aspergillus niger secretory beta-galactosidase under the control of ADH1 promoter and terminator were studied for their fermentation properties on lactose (V. Kumar, S. Ramakrishnan, T. T. Teeri, J. K. C. Knowles, and B. S. Hartley, Biotechnology 10:82-85, 1992). Lactose was hydrolyzed extracellularly into glucose and galactose, and both sugars were utilized simultaneously. Diauxic growth patterns were not observed. However, a typical biphasic growth was observed on a mixture of glucose and galactose under aerobic and anaerobic conditions with transformants of a haploid S. cerevisiae strain, GRF167. Polyploid distiller's yeast (Mauri) transformants were selected simply on the basis of the cloned gene expression on X-Gal (5-bromo-4-chloro-3-indolyl-beta-D-galactopyranoside) plates. Rapid and complete lactose hydrolysis and higher ethanol (0.31 g/g of sugar) and biomass (0.24 g/g of sugar) production were observed with distiller's yeast grown under aerobic conditions. A constant proportion (10%) of the population retained the plasmid throughout the fermentation period (48 h). Nearly theoretical yields of ethanol were obtained under anaerobic conditions on lactose, glucose, galactose, and whey permeate media. However, the rate and the amount of lactose hydrolysis were lower under anaerobic than aerobic conditions. All lactose-grown cells expressed partial galactokinase activity.     

Selection and Study of Potent Lactose-Fermenting Yeasts

Whey-fermenting Kluyveromyces cultures were revealed among 105 yeast strains assimilating lactose. Eighteen strains from milk products, showing maximum potency, fermented galactose, sucrose, and raffinose, in addition to lactose. Many yeast strains fermented inulin. Most strains were resistant to cycloheximide and grew in medium containing glucose, NaCl, and ethanol at concentrations of up to 50, 11–12, and 10–12%, respectively (4°C). Three strains had mycocinogenic activity. After fermentation of whey with selected yeast strains at 30°C for 2–3 days, the ethanol concentration was 4–5%.