Screening microorganisms for chitin hydrolysis and production of ethanol from amino sugars

Seventy-two strains of bacteria representing 39 genera and one yeast (Candida albicans) were screened for ability to hydrolyze chitin. Chitin hydrolysis was determined by a clear zone surrounding colonies growing on the surface of chitin agar. Species with the largest clear zone to colony size (CZ/CS) ratio were further compared for chitinolysis by assaying the level of reducing sugar produced in broth culture. Three yeasts and one bacterial strain known to produce ethanol from glucose were compared for their abilities to produce ethanol from amino sugars. Of the 72 strains screened, 23 produced CZ/CS ratios ranging from 0·38 to 2·5. The highest ratios were observed for strains in the genera: Bacillus and Serratia, followed by Micrococcus, Aeromonas, Vibrio, Clostridium and Plesiomonas. The other species examined produced ratios of less than 1 or were unable to hydrolyze chitin.Hansenula anomala, Pachysolen tannophilus, Saccharomyces cerevisiae, and Zymomonas mobilis were compared for their abilities to grow on and produce ethanol from glucose, glucosamine, and N-acetylglucosamine (NAG). Saccharomyces cerevisiae and H. anomala produced ethanol only from glucose. Pachysolen tannophilus and Z. mobilis produced ethanol from glucose, glucosamine and NAG. The highest concentration of ethanol produced from amino sugar was 598 μg ml⁻¹ from 10 mg ml⁻¹ glucosamine by Z. mobilis. This level was achieved only when yeast extract was included in the medium. Saccharomyces cerevisiae did not grow on glucosamine and Z. mobilis did not grow well on NAG.     

Ethanol production from paper sludge by simultaneous saccharification and co‐fermentation using recombinant xylose‐fermenting microorganisms

Simultaneous saccharification and co‐fermentation (SSCF) of waste paper sludge to ethanol was investigated using two recombinant xylose‐fermenting microbes: Zymomonas mobilis 8b and Saccharomyces cerevisiae RWB222. S. cerevisiae RWB222 produced over 40 g/L ethanol with a yield of 0.39 g ethanol/g carbohydrate on paper sludge at 37°C, while similar titers and yields were achieved by Z. mobilis 8b at 30°C. Both S. cerevisiae RWB222 and Z. mobilis 8b exhibited decreasing cell viability at 37°C when producing over 40 g/L ethanol. A high ethanol concentration can account for S. cerevisiae RWB222 viability loss, but ethanol concentration was not the only factor influencing Z. mobilis 8b viability loss at 37°C. Over 3 g/L residual glucose was observed at the end of paper sludge SSCF by Z. mobilis 8b, and a statistical analysis revealed that a high calcium concentration originating from paper sludge, a high ethanol concentration, and a high temperature were the key interactive factors resulting in glucose accumulation. The highest ethanol yields were achieved by SSCF of paper sludge with S. cerevisiae RWB222 at 37°C and Z. mobilis 8b at 30°C. With good sugar consumption at 37°C, S. cerevisiae RWB222 was able to gain an improvement in the polysaccharide to sugar yield compared to that at 30°C, whereas Z. mobilis 8b at 30°C had a lower polysaccharide to sugar yield, but a higher sugar to ethanol yield than S. cerevisiae. Both organisms under optimal conditions achieved a 19% higher overall conversion of paper sludge to ethanol than the non‐xylose utilizing S. cerevisiae D5A at its optimal process temperature of 37°C. Biotechnol. Bioeng. 2010;107: 235–244. © 2010 Wiley Periodicals, Inc.     

Deletion of the GRE3 Aldose Reductase Gene and Its Influence on Xylose Metabolism in Recombinant Strains of Saccharomyces cerevisiae Expressing the xylA and XKS1 Genes

Saccharomyces cerevisiae ferments hexoses efficiently but is unable to ferment xylose. When the bacterial enzyme xylose isomerase (XI) from Thermus thermophilus was produced in S. cerevisiae, xylose utilization and ethanol formation were demonstrated. In addition, xylitol and acetate were formed. An unspecific aldose reductase (AR) capable of reducing xylose to xylitol has been identified in S. cerevisiae. The GRE3 gene, encoding the AR enzyme, was deleted in S. cerevisiae CEN.PK2-1C, yielding YUSM1009a. XI from T. thermophilus was produced, and endogenous xylulokinase from S. cerevisiae was overproduced in S. cerevisiae CEN.PK2-1C and YUSM1009a. In recombinant strains from which the GRE3 gene was deleted, xylitol formation decreased twofold. Deletion of the GRE3 gene combined with expression of the xylA gene from T. thermophilus on a replicative plasmid generated recombinant xylose utilizing S. cerevisiae strain TMB3102, which produced ethanol from xylose with a yield of 0.28 mmol of C from ethanol/mmol of C from xylose. None of the recombinant strains grew on xylose.     

Enhancement of stress tolerance and ethanol production in Saccharomyces cerevisiae by heterologous expression of a trehalose biosynthetic gene from Streptomyces albus

The ability to grow and produce ethanol under stressful conditions is an important factor in industrial bioethanol production. Trehalose is found in many organisms including Saccharomyces cerevisiae, and has been known to play an important role in enhancing various types of stress tolerance. In this study, Streptomyces albus trehalose-6-phosphate synthase gene (salC) was expressed in Saccharomyces cerevisiae, and the recombinant strain with salC gene showed significantly improved stress resistances and ethanol production. The stress sensitivity and viability tests indicated that the recombinant had a greater resistance to ethanol than the control. At elevated temperatures, the results of flask cultures showed that the expression of salC played a positive role in protecting cells from heat stress. The recombinant strain was found to consume 100 g/L glucose and to produce 39 g/L ethanol at 40°C with an ethanol yield 6% higher than that of the control strain. In the fed-batch experiment in a bioreactor the recombinant strain produced 69 g/L ethanol with about 16% higher yield and about 13% higher productivity than the control strain. This demonstrated the enhancement of ethanol production capabilities of the recombinant strain under a high-ethanol stress condition.     

Engineering of <Emphasis Type="Italic">Saccharomyces cerevisiae</Emphasis> to utilize xylan as a sole carbohydrate source by co-expression of an endoxylanase,xylosidase and a bacterial xylose isomerase

Xylan represents a major component of lignocellulosic biomass, and its utilization by Saccharomyces cerevisiae is crucial for the cost effective production of ethanol from plant biomass. A recombinant xylan-degrading and xylose-assimilating Saccharomyces cerevisiae strain was engineered by co-expression of the xylanase (xyn2) of Trichoderma reesei, the xylosidase (xlnD) of Aspergillus niger, the Scheffersomyces stipitis xylulose kinase (xyl3) together with the codon-optimized xylose isomerase (xylA) from Bacteroides thetaiotaomicron. Under aerobic conditions, the recombinant strain displayed a complete respiratory mode, resulting in higher yeast biomass production and consequently higher enzyme production during growth on xylose as carbohydrate source. Under oxygen limitation, the strain produced ethanol from xylose at a maximum theoretical yield of ~90 %. This study is one of only a few that demonstrates the construction of a S. cerevisiae strain capable of growth on xylan as sole carbohydrate source by means of recombinant enzymes.     

Effect of C/N ratio and starch concentration on ethanol production from sago starch using recombinant yeast

Recombinant Saccharomyces cerevisiae YKU 131 (capable of expressing glucoamylase) was used to produce ethanol from sago starch. The optimum C/N ratio for ethanol production by the recombinant yeast was 7.9, where 4.7 and 10.1 g/l ethanol was produced from 20 and 40 g/l sago starch, respectively. At sago starch concentration higher than 40 g/l and C/N ratio higher than 10.4, glucoamylase production and rate of starch hydrolysis were reduced, which in turn, reduced ethanol production significantly. The theoretical yield of ethanol based on sago starch consumed in fermentation using 40 g/l was 72.6%. This yield was slightly lower than those obtained in fermentation using soluble starch such as potato and corn starch, which ranged from 80–90% as reported in the literature. However, S. cerevisiae YKU 131 could only utilize 62% of the total amount of starch added to a medium.     

Raw starch conversion by <Emphasis Type="Italic">Saccharomyces cerevisiae</Emphasis> expressing <Emphasis Type="Italic">Aspergillus tubingensis</Emphasis> amylases

Background

Starch is one of the most abundant organic polysaccharides available for the production of bio-ethanol as an alternative transport fuel. Cost-effective utilisation of starch requires consolidated bioprocessing (CBP) where a single microorganism can produce the enzymes required for hydrolysis of starch, and also convert the glucose monomers to ethanol.

Results

The Aspergillus tubingensis T8.4 α-amylase (amyA) and glucoamylase (glaA) genes were cloned and expressed in the laboratory strain Saccharomyces cerevisiae Y294 and the semi-industrial strain, S. cerevisiae Mnuα1. The recombinant AmyA and GlaA displayed protein sizes of 110–150 kDa and 90 kDa, respectively, suggesting significant glycosylation in S. cerevisiae. The Mnuα1[AmyA-GlaA] and Y294[AmyA-GlaA] strains were able to utilise 20 g l^-1 raw corn starch as sole carbohydrate source, with ethanol titers of 9.03 and 6.67 g l^-1 (0.038 and 0.028 g l^-1 h^-1), respectively, after 10 days. With a substrate load of 200 g l^-1 raw corn starch, Mnuα1[AmyA-GlaA] yielded 70.07 g l^-1 ethanol (0.58 g l^-1 h^-1) after 120 h of fermentation, whereas Y294[AmyA-GlaA] was less efficient at 43.33 g l^-1 ethanol (0.36 g l^-1 h^-1).

Conclusions

In a semi-industrial amylolytic S. cerevisiae strain expressing the A. tubingensis α-amylase and glucoamylase genes, 200 g l^-1 raw starch was completely hydrolysed (saccharified) in 120 hours with 74% converted to released sugars plus fermentation products and the remainder presumably to biomass. The single-step conversion of raw starch represents significant progress towards the realisation of CBP without the need for any heat pretreatment. Furthermore, the amylases were produced and secreted by the host strain, thus circumventing the need for exogenous amylases.

     

Expression of bacterial xylose isomerase in Saccharomyces cerevisiae under galactose supplemented condition

We constructed recombinant Saccharomyces cerevisiae harboring the xylose isomerase (XI) gene isolated from Clostridium phytofermentans to metabolize xylose and use it as a carbon and energy source. In this study, the effect of supplementation using co-substrate such as glucose or galactose on xylose utilization was studied in recombinant S. cerevisiae. Glucose, which is transported with high affinity by the same transport system as is xylose, was not affected by the heterologous expression of XI, thus xylose utilization was not observed in recombinant S. cerevisiae. However, supplemental galactose added to the recombinant S. cerevisiae stimulated xylose utilization as well as the expression of XI protein. Recombinant S. cerevisiae consumed up to 23.48 g/L of xylose when grown in media containing 40 g/L of xylose and supplemented with 20 g/L of galactose. These cells also produced 15.89 g/L of ethanol. Therefore, expression of the bacterial XI in recombinant S. cerevisiae was highly induced by the addition of supplemental galactose as a co-substrate with xylose, and supplemented galactose enabled the yeast strain to grow on xylose and ferment xylose to ethanol.     

Enhanced expression of the codon-optimized exo-inulinase gene from the yeast Meyerozyma guilliermondii in Saccharomyces sp. W0 and bioethanol production from inulin

In the present study, after the exo-inulinase gene INU1 from Meyerozyma guilliermondii was optimized according to the codon usage bias of Saccharomyces cerevisiae, both the optimized gene INU1Y and the native gene INU1 were ligated into the homologous integration expression vector pMIRSC11 and expressed in Saccharomyces sp. W0. It was determined that the inulinase activity of the recombinant yeast Y13 with the optimized gene INU1Y was 43.84 U/mL, which was obviously higher than that (31.39 U/mL) produced by the recombinant yeast EX3 with the native gene INU1. Moreover, it was indicated that the recombinant yeast Y13 could produce 126.30 mg/mL ethanol from 300.0 g/L inulin while the recombinant yeast EX3 and Saccharomyces sp. W0 produced 122.75 mg/mL and 114.15 mg/mL ethanol, respectively, under the same conditions. In addition, the ethanol productivity of the recombinant yeast Y13 was 2.25 mg/mL/h within 48 h of the fermentation, which was obviously higher than that of the recombinant yeast EX3 (1.97 mg/mL/h) and Saccharomyces sp. W0 (1.77 mg/mL/h) within the same period. The results demonstrated that the recombinant yeast Y13 had higher ethanol production and productivity than the recombinant yeast EX3 and Saccharomyces sp. W0. Therefore, it was concluded that the codon optimization of the exo-inulinase gene from M. guilliermondii effectively enhanced inulinase activity and improved ethanol production from inulin by Saccharomyces sp. W0 carrying the optimized inulinase gene.     

Production of Ethanol from Starch by Respiration-Deficient Recombinant Saccharomyces cerevisiae

A 100%-respiration-deficient nuclear petite amylolytic Saccharomyces cerevisiae NPB-G strain was generated, and its employment for direct fermentation of starch into ethanol was investigated. In a comparison of ethanol fermentation performances with the parental respiration-sufficient WTPB-G strain, the NPB-G strain showed an increase of ca. 48% in both ethanol yield and ethanol productivity.     

Expression of exoinulinase genes in Saccharomyces cerevisiae to improve ethanol production from inulin sources

To improve inulin utilization and ethanol fermentation, exoinulinase genes from the yeast Kluyveromyces marxianus and the recently identified yeast, Candida kutaonensis, were expressed in Saccharomyces cerevisiae. S. cerevisiae harboring the exoinulinase gene from C. kutaonensis gave higher ethanol yield and productivity from both inulin (0.38 vs. 0.34 g/g and 1.35 vs. 1.22 g l^?1 h^?1) and Jerusalem artichoke tuber flour (0.47 vs. 0.46 g/g and 1.62 vs. 1.54 g l^?1 h^?1) compared with the strain expressing the exoinulinase gene from K. marxianus. Thus, the exoinulinase gene from C. kutaonensis is advantageous for engineering S. cerevisiae to improve ethanol fermentation from inulin sources.     

Direct Production of Ethanol from Raw Corn Starch via Fermentation by Use of a Novel Surface-Engineered Yeast Strain Codisplaying Glucoamylase and α-Amylase

Direct and efficient production of ethanol by fermentation from raw corn starch was achieved by using the yeast Saccharomyces cerevisiae codisplaying Rhizopus oryzae glucoamylase and Streptococcus bovis α-amylase by using the C-terminal-half region of α-agglutinin and the flocculation functional domain of Flo1p as the respective anchor proteins. In 72-h fermentation, this strain produced 61.8 g of ethanol/liter, with 86.5% of theoretical yield from raw corn starch.     

Efficient production of ethanol from raw starch by a mated diploid Saccharomyces cerevisiae with integrated α-amylase and glucoamylase genes

The goal of this research was to construct a stable and efficient process for the production of ethanol from raw starch, using a recombinant Saccharomyces cerevisiae, which is productive even under conditions such as non-selection or long-term operation. Three recombinant yeast strains were used, two haploid strains (MT8-1SS and NBRC1440SS) and one diploid strain (MN8140SS). The recombinant strains were constructed by integrating the glucoamylase gene from Rhizopus oryzae fused with the 3′-half of the α-agglutinin gene as the anchor protein, and the α-amylase gene from Streptococcus bovis, respectively, into their chromosomal DNA by homologous recombination. The diploid strain MN8140SS was constructed by mating these opposite types of integrant haploid strains in order to enhance the expression of integrated amylase genes. The diploid strain had the highest ethanol productivity and reusability during fermentation from raw starch. Moreover, the ethanol production rate of the integrant diploid strain was maintained when batch fermentation was repeated three times (0.67, 0.60, and 0.67 g/l/h in each batch). These results clearly show that a diploid strain developed by mating two integrant haploid strains is useful for the establishment of an efficient ethanol production process.     

Effect of galactose feeding on the improved production of hirudin in fed-batch cultures of recombinant Saccharomyces cerevisiae

Different feeding strategies of galactose were employed to improve the production of anticoagulant, hirudin, by fed-batch mode of cultivation from recombinant Saccharomyces cerevisiae. The structural gene coding for hirudin was harboured with GAL10 promoter for controlled expression of hirudin and the MFα 1 signal sequence for secretion into the growth medium. A step-wise feeding of galactose was found as more suitable feeding strategy of galactose which resulted in the final hirudin volumetric productivity of 6,840?μg/l?·?h, than intermittent, continuous and ethanol controlled feeding of galactose. The final volumetric productivity of hirudin obtained by step-wise feeding of galactose was 3.88 fold higher compared with simple batch fermentation.     

Metabolic Engineering of a Phosphoketolase Pathway for Pentose Catabolism in Saccharomyces cerevisiae

Low ethanol yields on xylose hamper economically viable ethanol production from hemicellulose-rich plant material with Saccharomyces cerevisiae. A major obstacle is the limited capacity of yeast for anaerobic reoxidation of NADH. Net reoxidation of NADH could potentially be achieved by channeling carbon fluxes through a recombinant phosphoketolase pathway. By heterologous expression of phosphotransacetylase and acetaldehyde dehydrogenase in combination with the native phosphoketolase, we installed a functional phosphoketolase pathway in the xylose-fermenting Saccharomyces cerevisiae strain TMB3001c. Consequently the ethanol yield was increased by 25% because less of the by-product xylitol was formed. The flux through the recombinant phosphoketolase pathway was about 30% of the optimum flux that would be required to completely eliminate xylitol and glycerol accumulation. Further overexpression of phosphoketolase, however, increased acetate accumulation and reduced the fermentation rate. By combining the phosphoketolase pathway with the ald6 mutation, which reduced acetate formation, a strain with an ethanol yield 20% higher and a xylose fermentation rate 40% higher than those of its parent was engineered.     

Xylulokinase Overexpression in Two Strains of Saccharomyces cerevisiae Also Expressing Xylose Reductase and Xylitol Dehydrogenase and Its Effect on Fermentation of Xylose and Lignocellulosic Hydrolysate

Fermentation of the pentose sugar xylose to ethanol in lignocellulosic biomass would make bioethanol production economically more competitive. Saccharomyces cerevisiae, an efficient ethanol producer, can utilize xylose only when expressing the heterologous genes XYL1 (xylose reductase) and XYL2 (xylitol dehydrogenase). Xylose reductase and xylitol dehydrogenase convert xylose to its isomer xylulose. The gene XKS1 encodes the xylulose-phosphorylating enzyme xylulokinase. In this study, we determined the effect of XKS1 overexpression on two different S. cerevisiae host strains, H158 and CEN.PK, also expressing XYL1 and XYL2. H158 has been previously used as a host strain for the construction of recombinant xylose-utilizing S. cerevisiae strains. CEN.PK is a new strain specifically developed to serve as a host strain for the development of metabolic engineering strategies. Fermentation was carried out in defined and complex media containing a hexose and pentose sugar mixture or a birch wood lignocellulosic hydrolysate. XKS1 overexpression increased the ethanol yield by a factor of 2 and reduced the xylitol yield by 70 to 100% and the final acetate concentrations by 50 to 100%. However, XKS1 overexpression reduced the total xylose consumption by half for CEN.PK and to as little as one-fifth for H158. Yeast extract and peptone partly restored sugar consumption in hydrolysate medium. CEN.PK consumed more xylose but produced more xylitol than H158 and thus gave lower ethanol yields on consumed xylose. The results demonstrate that strain background and modulation of XKS1 expression are important for generating an efficient xylose-fermenting recombinant strain of S. cerevisiae.     

High solids fermentation of hydrolysates of wheat starch B in a continuous dynamic immobilized biocatalyst bioreactor

Summary A simple and efficient method of conversion of wheat starch B to ethanol was investigated. Employing a two-stage enzymatic saccharification process, 95% of the wheat starch was converted to fermentable sugars in 40 h. From 140 g/l total sugars in the feed solution, 63.6 g/l ethanol was produced continuously with a residence time of 3.3 h in a continuous dynamic immobilized biocatalyst bioreactor by immobilized cells ofSaccharomyces cerevisiae. The advantages and the application of this bioreactor to continuous alcoholic fermentation of industrial substrates are presented.     

Cloning and expression of amyE gene from Bacillus subtilis in Zymomonas mobilis and direct production of ethanol from soluble starch

Two proven secretion signal zmo130 and zmo331 native to Zymomonas mobilis were fused to the N terminal of ??-amylase from Bacillus subtilis and transformed into 5 different strains of Z. mobilis separately. It was found that the signal zmo130 could direct the extracellular secretion of the expressed ??-amylase with high activity, but zmo331 could not. Fermentation experiments demonstrated that the recombinant Z. mobilis CICC 10225(p130A) exhibited the highest level of ethanol production, which is nearly 50% of the theoretical yield of ethanol from soluble starch, but another recombinant Z. mobilis ATCC 31821(p130A) took the shortest fermentation time of approximately 3 days, with the second high level of ethanol yield. The recombined strains in our study could be an important target for the following genetic engineering of next amylase in order to hydrolyze starch completely.     

Yeast strains for concentrated substrates

Summary The screening of twenty yeast strains for ethanol productivity at high osmotic pressure at temperatures ranging from 32°C to 45°C is described. Shake flask fermentations of 30°, 40°, and 50° Bx cane molasses were performed. The effect of temperature on productivity at a non-inhibitory ethanol level is weakly pronounced. Most strains fermented poorly at 50° Bx molasses but two Schizosaccharomyces pombe and one commercial baker's yeast, Saccharomyces cerevisiae performed well at all concentrations of molasses. In an extended study with Schizosaccharomyces pombe (CBS 352) and Saccharomyces cerevisiae (SJAB, fresh yeast), simulating a continuous run it was shown that Schizosaccharomyces pombe was less sensitive to high DS than Saccharomyces cerevisiae. At 25% DS the productivity of Schizosaccharomyces pombe is almost twice that of Saccharomyces cerevisiae.     

Killer activity of Saccharomyces cerevisiae strains: partial characterization and strategies to improve the biocontrol efficacy in winemaking

Killer yeasts are considered potential biocontrol agents to avoid or reduce wine spoilage by undesirable species. In this study two Saccharomyces cerevisiae strains (Cf8 and M12) producing killer toxin were partially characterized and new strategies to improve their activity in winemaking were evaluated. Killer toxins were characterized by biochemical tests and growth inhibition of sensitive yeasts. Also genes encoding killer toxin were detected in the chromosomes of both strains by PCR. Both toxins showed optimal activity and production at conditions used during the wine-making process (pH 3.5 and temperatures of 15–25 °C). In addition, production of both toxins was higher when a nitrogen source was added. To improve killer activity different strategies of inoculation were studied, with the sequential inoculation of killer strains the best combination to control the growth of undesired yeasts. Sequential inoculation of Cf8–M12 showed a 45 % increase of killer activity on sensitive S. cerevisiae and spoilage yeasts. In the presence of ethanol (5–12 %) and SO₂ (50 mg/L) the killer activity of both toxins was increased, especially for toxin Cf8. Characteristics of both killer strains support their future application as starter cultures and biocontrol agents to produce wines of controlled quality.