Acetone stimulation of ethanol production from d-xylose by Pachysolen tannophilus

Summary Pachysolen tannophilus, a homothallic yeast, converts xylose to ethanol at a yield of 0.3 (g/g xylose). Concomitant with ethanol production, xylitol accumulates in the culture medium at similar yields (0.3 g/g xylose). The addition of the hydrogen-accepting compound, acetone, increases the amount of ethanol produced by this organism by 50–70%. The increase in ethanol is directly correlated with a decrease in xylitol secreted. The results indicate that conversion of acetone to 2-propanol by the cells provides the NAD⁺ used as a cofactor by xylitol dehydrogenase, the enzyme responsible for converting xylitol to xylulose.The mention of firm names or trade products does not imply that they are endorsed or recommended by the U. S. Department of Agriculture over other firms or similar products not mentioned.     

Sodium azide enhancement and inhibition of ethanol production from d-xylose Pachysolen tannophilus

The conversion of d-xylose to ethanol by the yeast Pachysolen tannophilus Y-2461 has been conducted in the presence of the respiratory inhibitor sodium azide. Conversion efficiencies improved for azide concentrations up to 0.2 mM. Concentrations above this value inhibited both ethanol production and cell growth. The work suggests that attempts to manipulate pentose conversion using extracellular factors, in this case azide, is of limited value in obtaining higher yield coefficients and better substrate conversion efficiencies.     

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.     

Factors in acid treated bagasse inhibiting ethanol production from d-xylose by Pachysolen tannophilus

The fermentation of d-xylose, the major sugar-cane bagasse hemicellulose component, to ethanol by Pachysolen tannophilus is inhibited by various factors produced or released during the acid hydrolysis of the bagasse or during the fermentation process. These include ethanol, iron, chromium, copper, nickel, acetic acid and furfural. Ethanol production by P. tannophilus is inhibited by ethanol fconcentrations >24 g l^?1. Furfural and acetic acid concentrations as low as 0.3 and 7 g l^?1, respectively, and iron, chromium, nickel and copper at concentrations of 0.07, 0.01, 0.01 and 0.004 g l^?1, respectively. Similar concentrations may be found in acid-hydrolysed bagasse. The removal of these factors by treatment with ion-exchange resin resulted in the fermentation of the sugars to ethanol. The d-glucose was used rapidly and completely whereas d-xylose utilization was slow and incomplete. An ethanol concentration of 4.1 g l^?1 was produced and an ethanol yield of 0.32 was obtained. Xylitol in significant amounts was produced.     

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.     

Comparative study of d-xylose conversion to ethanol by immobilized growing or non-growing cells of the yeast Pachysolen tannophilus

Summary The direct conversion of d-xylose to ethanol was investigated using immobilized growing and non-growing cells of the yeast Pachysolen tannophilus. Both preparations produced ethanol from d-xylose, however the d-xylose conversion to ethanol was much better with immobilized growing cells. Ethanol concentration up to 22.9 g/l and ethanol yield of 0.351 g/g of d-xylose were obtained in batch fermentation by immobilized growing cells whereas only 17.0 g/l and 0.308 g/g of d-xylose were obtained by immobilized non-growing cells. With continuous systems, immobilized growing cells were necessary for the long-term operation, since a steady state ethanol concentration of 17.7 g/l was maintained for only one week by immobilized non-growing cell reactor. With simultaneous control of aeration rate and concentrations of nitrogen sources in feed medium, immobilized growing cells of P. tannophilus showed excellent performance. At a residence time of 25 h, the immobilized cell reactor produced 26.9 g/l of ethanol from 65 g/l of d-xylose in feed medium.     

Reversible inactivation of d-xylose utilization by d-glucose in the pentose-fermenting yeast Pachysolen tannophilus

Abstract A major problem in fermenting pentoses using lignocellulosic substrates is the presence of d -glucose which inhibits d -xylose utilization. We previously showed that d -glucose represses the induction of xylose reductase and xylitol dehydrogenase activities, thereby inhibiting d -xylose utilization in Pachysolen tannophilus . The question arose whether d -glucose can also inactivate d -xylose fermentation. P. tannophilus cells were grown on a defined d -xylose-containing liquid medium. At about 40 h, d -glucose was added to a final concentration of 3% (w/v). This led to a rapid cessation of d -xylose utilization, which resumed after 10–12 h before d -glucose was completely consumed. This suggests that d -glucose inactivated existing d -xylose catabolic enzymes and that inactivation was reversed at low d -glucose concentrations. This reversible inactivation was distinct from d -glucose repression. Addition of cycloheximide did not block the resumption of d -xylose consumption, suggesting that reactivation was independent of protein synthesis.     

Conversion of D-xylose to ethanol by the yeast Pachysolen tannophilus

The yeast Pachysolen tannophilus was found to be capable of converting D-xylose to ethanol. Batch cultures initially containing 50 g/L D-xylose yielded 0.34 g of ethanol per gram of pentose consumed. Aerobic conditions were required for cell growth but not for ethanol production. Both alcohol formation and growth were optimum when incubation temperature was 32 degrees C, when pH was near 2.5, and when D-xylose and ethanol concentrations did not exceed 50 and 20 g/L, respectively.     

Conversion of D-xylose into ethanol by the yeast Pachysolen tannophilus

Summary The yeast Pachysolen tannophilus has been identified as being able to convert an aldopentose, D-xylose, into ethanol. A feature of the conversion is that it can take place under aerobic conditions.Issued as N.R.C.C. Publication No. 19095.     

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.     

Ethanol production from d-galactose and glycerol by Pachysolen tannophilus

Pachysolen tannophilus has recently been shown to be able to convert d-xylose, a pentose, to ethanol. Previously, d-xylose had been considered to be nonfermentable by yeasts. The present study shows that the organism can be used to obtain ethanol from other carbohydrates previously considered as nonfermentable, either by P. tannophilus in particular, d-galactose, or by yeasts in general, glycerol. Such identification for d-galactose allows P. tannophilus to be considered for fermentation of four of the five major plant monosaccharides: d-glucose, d-mannose, d-galactose and d-xylose. The ability to ferment glycerol is of potential use, in part, for the conversion of glycerol derived from algae into ethanol.     

Hybrid formation and copulation activity in the yeast Pachysolen tannophilus

The copulation activity and hybrid formation efficiency have been studied in the xylose-assimilating yeast Pachysolen tannophilus. It was shown that the presence of 2% D-glucose, 0.5% yeast extract, and 2% agarose in the growth medium provided for the highest frequencies of hybrid formation. Atypical hybrid cultures similar in morphophysiological characteristics to native haploid strains of P. tannophilus were revealed in the course of hybridization. The genesis mechanism of such cultures and the reasons for the restricted applicability of hybridological analysis to genetic studies of P. tannophilus are discussed.     

Potential utilization of sorghum field waste for fuel ethanol production employing Pachysolen tannophilus and Saccharomyces cerevisiae

In this study, we demonstrate that the sorghum field waste, sorghum stover could be used to produce fuel grade ethanol. The alkaline treatment of 2% NaOH for 8h removed 64% of lignin from sorghum stover. Maximum of 68 and 56 g/L of ethanol yield were obtained by Saccharomyces cerevisiae (MTCC 173) and Pachysolen tannophilus (MTCC 1077) from sorghum stover under optimized condition, respectively. pH and temperature were optimized for the better growth of S. cerevisiae and P. tannophilus. A total of 51% and 48% more ethanol yield was obtained at initial sugar concentration of 200 g/L than 150 g/L by P. tannophilus and S. cerevisiae, respectively. Respiratory deficiency and ethanol tolerance of the organisms were studied. This investigation showed that sorghum field waste could be effectively used for the production of fuel ethanol to avoid conflicts between human food use and industrial use of crops.     

Bioconversion of wheat straw cellulose/hemicellulose to ethanol by Saccharomyces uvarum and Pachysolen tannophilus

The information presented in this publication represents current research findings on the production of glucose and xylose from straw and subsequent direct fermentation of both sugars to ethanol. Agricultural straw was subjected to thermal or alkali pulping prior to enzymatic saccharification. When wheat straw (WS) was treated at 170 degrees C for 30-60 min at a water-to-solids ratio of 7:1, the yield of cellulosic pulp was 70-82%. A sodium hydroxide extration yielded a 60% cellulosic pulp and a hemicellulosic fraction available for fermentation to ethanol. The cellulosic pulps were subjected to cellulase hydrolysis at 55 degrees C for production of sugars to support a 6-C fermentation. Hemicellulose was recovered from the liquor filtrates by acid/alcohol precipitation followed by acid hydrolysis to xylose for fermentation. Subsequent experiments have involved the fermentation of cellulosic and hemicelluosic hydrolysates to ethanol. Apparently these fermentations were inhibited by substances introduced by thermal and alkali treatment of the straws, because ethanol efficiencies of only 40-60% were achieved. Xylose from hydrolysis of wheat straw pentosans supported an ethanol fermentation by Pachysolen tannophilus strain NRRL 2460. This unusual yeast is capable of producing ethanol from both glucose and xylose. Ethanol yields were not maximal due to deleterious substances in the WS hydrolysates.     

Conditions favoring differentiation and stabilization of the life cycle of the yeast Pachysolen tannophilus

Conditions favoring differentiation and stabilization of the life cycle of the yeast Pachysolen tannophilus have been studied. When concentrations of the carbon source in the medium were lower than 100 g/l, it was found to be favorable to the mating of vegetative cells, both haploid and diploid. The addition of nitrogen and sulfur sources to the medium influenced the life phases of haploid cells and partially stabilized the vegetative growth of diploid cells. Enrichment of the nutrient medium with potassium, vitamins, and microelements was shown to be necessary for the formation and maturation of conjugated ascospores. Microelements, vitamins, and phosphorus in excessive amounts activated conjugation but did not provide for the distinct phases of formation of unconjugated asci and spores in the diploid cells. Possible reasons for the unstable diplophase in the yeast P. tannophilus are discussed.     

Valorization of olive stones for xylitol and ethanol production from dilute acid pretreatment via enzymatic hydrolysis and fermentation by Pachysolen tannophilus

Olive stones are an agro-industrial by-product abundant in the Mediterranean area that is regarded as a potential lignocellulosic feedstock for sugar production. Statistical modeling of dilute-sulphuric acid hydrolysis of olive stones has been performed using a response surface methodology, with treatment temperature and process time as factors, to optimize the hydrolysis conditions aiming to attain maximum d-xylose extraction from hemicelluloses. Thus, solid yield and composition of solid and liquid phases were assessed by empirical modeling. The highest yield of d-xylose was found at a temperature of 195 °C for 5 min. Under these conditions, 89.7% of the total d-xylose was recovered from raw material. The resulting solids from optimal conditions were assayed as substrate for enzymatic hydrolysis, while fermentability of hemicellulosic hydrolysates was tested using the d-xylose-fermenting yeast Pachysolen tannophilus. Both bioprocesses were considerably influenced by enzyme loading and inoculum size. In the enzymatic hydrolysis step, about 56% of cellulose was converted into d-glucose by using an enzyme/solid ratio of 40 FPU g⁻¹, while in the fermentation carried out with a cell concentration of 2 g L⁻¹ a yield of 0.44 g xylitol/g d-xylose and a global volumetric productivity of 0.11 g L⁻¹ h⁻¹ were achieved.     

Assignment of cloned genes to electrophoretically separated chromosomes of the yeast Pachysolen tannophilus

An electrophoretic karyotype of Pachysolen tannophilus has been obtained using Pulsed Field Gel Electrophoresis. Seven chromosomal bands were separated with one of the bands migrating probably as a doublet. The sizes of the chromosomes were estimated to be between 1 and 3.1 megabase pairs. Eleven loci have been assigned to chromosomal bands, including four involved in the metabolism of D-xylose.