Induction of Xylose Reductase and Xylitol Dehydrogenase Activities in Pachysolen tannophilus and Pichia stipitis on Mixed Sugars

The induction of xylose reductase and xylitol dehydrogenase activities on mixed sugars was investigated in the yeasts Pachysolen tannophilus and Pichia stipitis. Enzyme activities induced on d-xylose served as the controls. In both yeasts, d-glucose, d-mannose, and 2-deoxyglucose inhibited enzyme induction by d-xylose to various degrees. Cellobiose, l-arabinose, and d-galactose were not inhibitory. In liquid batch culture, P. tannophilus utilized d-glucose and d-mannose rapidly and preferentially over d-xylose, while d-galactose consumption was poor and lagged behind that of the pentose sugar. In P. stipitis, all three hexoses were used preferentially over d-xylose. The results showed that the repressibility of xylose reductase and xylitol dehydrogenase may limit the potential of yeast fermentation of pentose sugars in hydrolysates of lignocellulosic substrates.     

Oxygen requirements for d-xylose fermentation to ethanol and polyols by Pachysolen tannophilus

The oxygen requirements for ethanol production from d-xylose (10 or 20 g l^?1) by Pachysolen tannophilus have been determined by controlling the availability of oxygen to shake flasks. Under anaerobic conditions no ethanol was produced whereas under aerobic conditions mainly biomass was formed. Semi-anaerobic conditions resulted in maximum ethanol production. By varying the stirring speed of a fermenter and supplying air to the liquid surface at various rates, the oxygen transfer rate (OTR) was controlled under semi-anaerobic conditions. By increasing the OTR from 0.05 to 16.04 mmol l^?1 h^?1, the ethanol yield coefficient decreased from 0.28 to 0.18 while the cell yield coefficient increased from 0.14 to 0.22. The accumulation of polyols decreased from 0.88 to 0.56 g l^?1 with increasing OTR. At OTRs between 0.09 and 1.18 mmol l^?1 h^?1, specific ethanol productivity attained a maximum value of 0.07 h^?1 and decreased with either increasing or decreasing OTR. The results indicate that the OTR must be carefully controlled for efficient ethanol production from d-xylose by P. tannophilus.     

Affinity Purifications of Aldose Reductase and Xylitol Dehydrogenase from the Xylose-Fermenting Yeast Pachysolen tannophilus

Although xylose is a major product of hydrolysis of lignocellulosic materials, few yeasts are able to convert it to ethanol. In Pachysolen tannophilus, one of the few xylose-fermenting yeasts found, aldose reductase and xylitol dehydrogenase were found to be key enzymes in the metabolic pathway for xylose fermentation. This paper presents a method for the rapid and simultaneous purification of both aldose reductase and xylitol dehydrogenase from P. tannophilus. Preliminary studies indicate that this method may be easily adapted to purify similar enzymes from other xylose-fermenting yeasts.     

Concurrent Production and Consumption of Ethanol by Cultures of Pachysolen tannophilus Growing on d-Xylose

Growing cultures of Pachysolen tannophilus concurrently consumed and produced ethanol in the presence of substantial concentrations of d-xylose. Ethanol was also assimilated in the presence of other sugars, the amount depending on the sugar. Less ethanol assimilation occurred with d-glucose than with d-xylose. The rate of ethanol consumption decreased as the concentration of glucose was increased, but some consumption still occurred when 2% glucose was present. The rate increased with the amount of oxygen available to the culture when d-xylose or ethanol was the carbon source. In most instances, estimates of consumption were based on the extent of incorporation of C from [1-C]ethanol into trichloroacetic acid-insoluble material. The results are pertinent to the use of P. tannophilus for the production of ethanol from d-xylose.     

Mutants of Pachysolen tannophilus with Improved Production of Ethanol from d-Xylose

The conversion of d-xylose to ethanol by the yeast Pachysolen tannophilus is relatively inefficient in batch culture. The inefficiency has been attributed in part to concurrent utilization of ethanol in the presence of appreciable concentrations of d-xylose and to the formation of xylitol and other by-products. To increase the concentration of ethanol accumulated in batch cultures, UV-induced mutants of P. tannophilus were selected on the basis of diminished growth on ethanol. Eleven independent mutant loci that conferred the ethanol-defective phenotype were identified. Three led to a greater yield and volumetric rate of production of ethanol than the wild type. One also produced less xylitol and was characterized by a deficiency in activity for malate dehydrogenase.     

Mutants of Pachysolen tannophilus showing enhanced rates of growth and ethanol formation from d-xylose

Mutants of Pachysolen tannophilus NRRL Y-2460 have been sought that show enhanced rates of d-xylose fermentation. Mutagenesis followed by enrichment in urea-xylitol broth generally resulted in a lower frequency of good ethanol producers than enrichment in nitrate-xylitol broth. Under aerobic conditions, the best xylose-fermenting strains (which were obtained from nitrate-xylitol broth) produced ethanol from xylose twice as fast and in 32% better yield than the parent strain. Under anaerobic conditions, these strains produced ethanol from xylose 50% faster than (but in the same yield as) the parent strain. These findings show that enrichment in nitrate-xylitol broth is a promising method for obtaining mutants of Pachysolen having enhanced fermentation rates.     

Some properties of polysaccharides of microorganisms from degraded straw

Extracellular polysachcarides from bacteria and yeasts isolated from decomposed straw contained various proportions of d-galactose, d-glucose, d-mannose, uronic acid, d-xylose, l-fucose and l-rhamnose. Molecular weights of the polymers determined by viscometry and gel filtration were in the range 40 000–1800 000. All the polysaccharides stabilized aggregates of volcanic ash and most were more effective than the polysaccharide from Lipomyces starkeyi. Effectiveness seemed to be more related to molecular weight than to chemical composition.     

A kinetic analysis of d-xylose transport in rhodotorula glutinis

The kinetics of D-xylose transport were studied in Rhodotorula glutinis. Analysis of the saturation isotherm revealed the presence of at least two carriers for d-xylose in the Rhodotorula plasma membrane. These two carriers exhibited Km values differing by more than an order of magnitude. The low K_m carrier was repressed in rapidly growing cells and depressed by starvation of the cells.Several hexoses were observed to inhibit d-xylose transport. In the studies reported here, the inhibitions produced by d-galactose and 2-deoxy-d-glucose were examined in some detail in order to define the interactions of these sugars with the d-xylose carriers. 2-Deoxy-d-glucose competitively inhibited both of the d-xylose carriers. In contrast, only the low-K_m carrier was competitively inhibited by d-galactose.     

Pachysolen tannophilus: Properties and process considerations for ethanol production from d-xylose

d-Xylose comprises nearly one-third of the reducing sugars obtained from lignocellulose hydrolysis. Despite its relative abundance in crop and forest residues, xylose has been found unfermentable by most yeasts. A process for efficient xylose fermentation is expected to have significant impact on the future economics of converting lignocellulose to ethanol and may also provide additional profit for existing wood processing industries releasing xylose-rich waste streams, i.e. paper mills producing sulphite liquor. Pachysolen tannophilus was the first yeast discovered capable of significant ethanol production from xylose and has served as a model for studies of other yeasts mediating this conversion. Current knowledge about biochemical pathways involved in xylose utilization by this yeast is reviewed. Factors involved in regulating carbon flow to products are discussed in conjunction with process considerations for optimizing ethanol accumulation. Finally, the prospect of more efficient ethanol production through genetic strain improvement is considered.     

Production of Ethanol from d-Xylose by Using d-Xylose Isomerase and Yeasts

d-Xylulose, an intermediate of d-xylose catabolism, was observed to be fermentable to ethanol and carbon dioxide in a yield of greater than 80% by yeasts (including industrial bakers' yeast) under fermentative conditions. This conversion appears to be carried out by many yeasts known for d-glucose fermentation. In some yeasts, xylitol, in addition to ethanol, was produced from d-xylulose. Fermenting yeasts are also able to produce ethanol from d-xylose when d-xylose isomerizing enzyme is present. The results indicate that ethanol could be produced from d-xylose in a yield of greater than 80% by a two-step process. First, d-xylose is converted to d-xylulose by xylose isomerase. d-Xylulose is then fermented to ethanol by yeasts.     

Alcoholic Fermentation of d-Xylose by Yeasts

Type strains of 200 species of yeasts able to ferment glucose and grow on xylose were screened for fermentation of d-xylose. In most of the strains tested, ethanol production was negligible. Nineteen were found to produce between 0.1 and 1.0 g of ethanol per liter. Strains of the following species produce more than 1 g of ethanol per liter in the fermentation test with 2% xylose: Brettanomyces naardenensis, Candida shehatae, Candida tenuis, Pachysolen tannophilus, Pichia segobiensis, and Pichia stipitis. Subsequent screening of these yeasts for their capacity to ferment d-cellobiose revealed that only Candida tenuis CBS 4435 was a good fermenter of both xylose and cellobiose under the test conditions used.     

Structural features of an acidic polysaccharide from the mucin of Drosera binata

The polysaccharide from the mucin secreted by the leaves of Drosera binata is composed of l-arabinose, d-xylose, d-galactose, d-man     

Isolation and Screening of Yeasts That Ferment d-Xylose Directly to Ethanol

Natural habitats of yeasts were examined for the presence of strains able to produce ethanol from d-xylose. Black knots, insect frass, and tree exudates were screened by enrichment in liquid d-xylose-yeast extract medium. These and each d-xylose-assimilating yeast in a collection from cactus fruits and Drosophila spp. were tested for alcohol production from this sugar. Among the 412 isolates examined, 36 produced more than 1 g of ethanol liter from 20 g of d-xylose liter, all under aerated conditions. Closer examination of the strains indicated that their time courses of d-xylose fermentation followed different patterns. Some strains produced more biomass than ethanol, and among these, ethanol may or may not be assimilated rapidly after depletion of d-xylose. Others produced more ethanol than biomass, but all catabolized ethanol after carbohydrate exhaustion. Ethanol production appeared best at low pH values and under mild aeration. Possible correlations between the nutritional profiles of the yeasts and their ability to produce ethanol from d-xylose were explored by multivariate analysis. d-Xylose appeared slightly better utilized by yeasts which rate poorly in terms of fermentation. The fermentation of d-glucose had no bearing on d-xylose fermentation. No specific nutritional trait could discriminate well between better d-xylose fermentors and other yeasts.     

Polysaccharide components of the seed-coat mucilage from hyptis suaveolens

The mucilage isolated from the seed coat of Hyptis suaveolens contains l-fucose, d-xylose, d-mannose, d-galactose, d-glucose and 4-O-methyl-d-glucuronic acid in the mol ratios 1.0:2.5:1.5:7.0:12.5:1.1. Fractionation of the mucilage with Fehling's solution gave a neutral and an acidic polysaccharide. The neutral polysaccharide appears to be homogeneous and is composed of d-mannose, d-galactose and d-glucose in the mol ratios 1.0:4.5:7.5. The acidic polysaccharide is composed of l-fucose, d-xylose and 4-O-methyl-d-glucuronic acid in the mol ratios 1.0:2.5:1.1. It is homogeneous on gel filtration, DEAE-cellulose chromatography, sedimentation analysis and electrophoresis.     

Purification and characterization of the d-xylose isomerase gene from Escherichia coli

A DNA fragment containing both the Escherichia coli d-xylose isomerase (d-xylose ketol-isomerase, EC 5.3.1.5) gene and the d-xylulokinase (ATP: d-xylulose 5-phosphotransferase, EC 2.7.1.17) gene has been cloned on an E. coli plasmid. The d-xylose isomerase gene was separated from the d-xylulokinase gene by the construction of a new deletion plasmid, pLX7. The d-xylose isomerase gene cloned on pLX7 was found still to be an intact gene. The precise location of the d-xylose isomerase gene on the plasmid pLX7 was further determined by the construction of two more plasmids, pLX8 and pLX9. This is believed to be the first d-xylose isomerase gene that has been isolated and extensively purified from any organism. d-Xylose isomerase, the enzyme product of the d-xylose isomerase gene, is responsible for the conversion of d-xylose to d-xylulose, as well as d-glucose to d-fructose. It is widely believed that yeast cannot ferment d-xylose to ethanol primarily because of the lack of d-xylose isomerase in yeast. d-Xylose isomerase (also known as d-glucose isomerase) is also used for the commercial production of high-fructose syrups. The purification of the d-xylose isomerase gene may lead to the following industrial applications: (1) cloning and expression of the gene in yeast to make the latter organism capable of directly fermenting d-xylose to ethanol, and (2) cloning of the gene on a high-copy-number plasmid in a proper host to overproduce the enzyme, which should have a profound impact on the high-fructose syrup technology.     

Ethanol production from pentoses by immobilized microorganisms

The capabilities of immobilized Fusarium oxysporum f. sp. lini, Mucor sp., and Saccharomyces cerevisiae in fermenting pentose to ethanol have been compared. S. cerevisiae was found to have the best fermentation rate on d-xylulose of 0.3 g l^?1 h^?1. By using a separate isomerase column for converting d-xylose to d-xylulose and a yeast column for converting d-xylulose to ethanol, an ethanol concentration of 32 g l^?1 was obtained from 10% d-xylose. The ethanol yield was calculated to be 64% of the theoretical yield.     

A kinetic analysis of d-xylose transport in rhodotorula glutinis

The kinetics of D-xylose transport were studied in Rhodotorula glutinis. Analysis of the saturation isotherm revealed the presence of at least two carriers for d-xylose in the Rhodotorula plasma membrane. These two carriers exhibited Km values differing by more than an order of magnitude. The low K_m carrier was repressed in rapidly growing cells and depressed by starvation of the cells.Several hexoses were observed to inhibit d-xylose transport. In the studies reported here, the inhibitions produced by d-galactose and 2-deoxy-d-glucose were examined in some detail in order to define the interactions of these sugars with the d-xylose carriers. 2-Deoxy-d-glucose competitively inhibited both of the d-xylose carriers. In contrast, only the low-K_m carrier was competitively inhibited by d-galactose.     

Genetic and Biochemical Characterization of Mutations Affecting the Ability of the Yeast Pachysolen tannophilus To Metabolize d-Xylose

Induced mutants, selected for their defective growth on d-xylose while retaining the ability to grow normally on d-glucose, were studied in Pachysolen tannophilus, a yeast capable of converting d-xylose to ethanol. Fourteen of the mutations were found to occur at nine distinct loci, and data indicated that many more loci remain to be detected. Most of the mutations were pleiotropic in character, and the expression of some of them was much affected by nutritional conditions and by genetic background. Mutations at several loci resulted in poor growth on at least one compound that was either an intermediate of the tricarboxylic acid cycle, succinate or alpha-ketoglutarate, or on compounds metabolizable via this cycle, ethanol or glycerol. An initial biochemical characterization of the mutants was undertaken. Analysis for xylose reductase, xylitol dehydrogenase, and xylulose kinase activity showed that one or more of these activities was affected in 12 of 13 mutants. However, drastic reduction in activity of a single enzyme was confined to that of xylitol dehydrogenase by mutations at three different loci and to that of d-xylose reductase by mutation at another locus. Growth of these latter four mutants was normal on all carbon sources tested that were not five-carbon sugars.     

Changes in microflora and biochemical composition during the Baceman stage of traditional indonesian Kecap (soy sauce) production

Indonesian soy sauce (kecap) is made from black soybeans in a traditional way which involves two microbiological stages: a solid-state fermentation and a brine fermentation. This study is concerned with the brine fermentation, called baceman. Samples from different kecap producers were analyzed for (bio)chemical content and micro-organisms. It was found that the final composition of the baceman differed from manufacturer to manufacturer, and even within companies large differences were found in microflora and the amounts of fermentation products, formol nitrogen and salt concentration. The main fermentation products were lactate, acetate, glycerol and ethanol. Pediococcus halophilus, staphylococci, a coryneform bacterium and yeasts belonging to Candida, Debaromyces and Sterigmatomyces were isolated from the brines. Compared to Japanese soy sauce production, fermentation by yeasts does not play an important role in Indonesian kecap production. This is due to the fact that kecap is made from whole soybeans only, which are poor in sugars. After fermentation by P. halophilus no substrates are left for growth and ethanol production by yeasts. The presence of film forming yeasts can even lead to spoilage of the product.