Fermentation of hardwood hemicellulose hydrolysate byPachysolen tannophilus,candida shehatae andPichia stipitis

Summary Hardwood hemicellulose hydrolysate has been utilized as a substrate for ethanol production. Among the three different yeasts tested, the best performances have been obtained, in decreasing order, usingPachysolen tannophilus, Candida shehatae andPichia stipitis. Several pretreatments of this raw material have been studied to improve ethanol yields; in one such pretreatment a strain ofP. tannophilus produced ethanol with a yield of 0.29 g_ethanol/g_sugars (g_P/g_S); which is only 15% less than the values observed with synthetic media. Neither aeration nor acetone addition improved the fermentation of this substrate; in fact, only a marked stimulation of biomass growth has been observed at the expense of both ethanol and xylitol production.     

The relation between redox potential and D-xylose fermentation by Candida shehatae and Pichia stipitis

Summary Fed-batch xylose fermentations with the yeastsCandida shehatae andPichia stipitis were conducted, using stirrer speed variation with the redox potential as control index to maintain oxygen-limited conditions. The best results were obtained withC. shehatae at 300 (±10) m V (relative to the standard hydrogen electrode), and these fermentation parameters compared favourably with those obtained previously with the dissolved oxygen tension as control variable. Redox control ofP. stipitis fermentations proved especially difficult. Cell growth during the fermentation was probably a major factor affecting redox potential.     

The effect of aeration on xylose fermentation by Candida shehatae and Pachysolen tannophilus

Summary The ability of a Candida shehatae and a Pachysolen tannophilus strain to ferment D-xylose to ethanol was evaluated in defined and complex media under different levels of aeration. Aeration enhanced the ethanol productivity of both yeasts considerably. C. shehatae maintained a higher fermentation rate and ethanol yield than P. tannophilus over a wide range of aeration levels. Ethanol production by C. shehatae commenced during the early stage of the fermentation, whereas with P. tannophilus there was a considerable lag between the initiation of growth and ethanol production. Both yeasts produced appreciable quantities of xylitol late in the fermentation. P. tannophilus failed to grow under anoxic conditions, producing a maximum of only 0.5 g · l^-1 ethanol. In comparison, C. shehatae exhibited limited growth in anoxic cultures, and produced ethanol much more rapidly. Under the condition of aeration where C. shehatae exhibited the highest ethanol productivity, the fermentation parameters were: maximum specific growth rate, 0.15 h^-1; maximum volumetric and specific rates of ethanol production, 0.7 g (l · h)^-1 and 0.34 g ethanol (g cells · h)^-1 respectively; ethanol yield, 0.36 g (g xylose)^-1. The best values obtained with P. tannophilus were: maximum specific growth rate, 0.14 h^-1; maximum volumetric and specific rates of ethanol production, 0.22 g (l · h)^-1 and 0.07 h^-1 respectively; ethanol yield coefficient, 0.28. Because of its higher ethanol productivity at various levels of aeration, C. shehatae has a greater potential for ethanol production from xylose than P. tannophilus.     

The D-xylose fermenting capacities of immobilizedPichia stipitis andPachysolen tannophilus

Summary The yeastsP. stipitis NRRL Y-7124 andP. tannophilus NRRL Y-2460 were entrapped in -carrageenan beads and used for repeated batch fermentation of D-xylose, in a series of four reactors. The operating conditions finally chosen gave an oxygen coefficient (K_La) of 0.83 min^–1, as measured by the sulphite method. Ethanol yields were 0.40 g/g forP. stipitis and 0.36 g/g forP. tannophilus (respectively 78.4% and 70.5% of the theoretical yields). In spite of its lower retention by the gel,P. stipitis exhibited greater fermenting capacities thanP. tannophilus.     

The fermentation of hexose and pentose sugars by Candida shehatae and Pichia stipitis

Summary The fermentation by Candida shehatae and Pichia stipitis of xylitol and the various sugars which are liberated upon hydrolysis of lignocellulosic biomass was investigated. Both yeasts produced ethanol from d-glucose, d-mannose, d-galactose and d-xylose. Only P. stipitis fermented d-cellobiose, producing 6.5 g·l^-1 ethanol from 20 g·l^-1 cellobiose within 48 h. No ethanol was produced from l-arabinose, l-rhamnose or xylitol. Diauxie was evident during the fermentation of a sugar mixture. Following the depletion of glucose, P. stipitis fermented galactose, mannose, xylose and cellobiose simultaneously with no noticeable preceding lag period. A similar fermentation pattern was observed with C. shehatae, except that it failed to utilize cellobiose even though it grew on cellobiose when supplied as the sole sugar. P. stipitis produced considerably more ethanol from the sugar mixture than C. shehatae, primarily due to its ability to ferment cellobiose. In general P. stipitis exhibited a higher volumetric rate and yield of ethanol production. This yeast fermented glucose 30–50% more rapidly than xylose, whereas the rates of ethanol production from these two sugars by C. shehatae were similar. P. stipitis had no absolute vitamin requirement for xylose fermentation, but biotin and thiamine enhanced the rate and yield of ethanol production significantly.Nomenclature _max Maximum specific growth rate, h^-1 - Q _p Maximum volumetric rate of ethanol production, calculated from the slope of the ethanol vs. time curve, g·(l·h)^-1 - q _p Maximum specific rate of ethanol production, g·(g cells·h) - Y _p/s Ethanol yield coefficient, g ethanol·(g substrate utilized)^-1 - Y _x/s Cell yield coefficient, g biomass·(g substrate utilized)^-1 - E Efficiency of substrate utilization, g substrate consumed·(g initial substrate)^-1·100     

Fluorescence measurements under aerobic and anaerobic conditions on Pichia stipitis,Pachysolen tannophilus and Candida utilis grown on D-xylose

Batch growth of the yeasts Candida utilis, Pachysolen tannophilus and Pichia stipitis on 1% D-xylose was monitored using a commercial fluorosensor with an excitation wavelength of 340 nm and a detection wavelength of 460 nm. Step changes in oxygen concentration were made and in the presence of 0.3 g/l of xylose, step changes from aerobic to anaerobic conditions resulted in an increase of the fluorescence level by about 40% for the non-fermentative yeast C. utilis. However, the increases of the fluorescence levels for P. tannophilus and P. stipitis stayed below 10%. These measurements indicate better control of (or better redox balance for) intracellular NADH concentration in P. tannophilus and P. stipitis than in C. utilis.List of Symbols F NFU fluorescence - F ₀ NFU initial fluorescence - F NFU final fluorescence difference - t s time - s time constant     

Comparative study of the fermentation of D-glucose/D-xylose mixtures with Pachysolen tannophilus and Candida shehatae

We have performed a comparative analysis of the fermentation of the solutions of the mixtures of D-glucose and D-xylose with the yeasts Pachysolen tannophilus (ATCC 32691) and Candida shehatae (ATCC 34887), with the aim of producing bioethanol. All the experiments were performed in a batch bioreactor, with a constant aeration level, temperature of 30v°C, and a culture medium with an initial pH of 4.5. For both yeasts, the comparison was established on the basis of the following parameters: maximum specific growth rate, biomass productivity, specific rate of substrate consumption (q_s) and of ethanol production (q_E), and overall ethanol and xylitol yields. For the calculation of the specific rates of substrate consumption and ethanol production, differential and integral methods were applied to the kinetic data. From the experimental results, it is deduced that both Candida and Pachysolen sequentially consume the two substrates, first D-glucose and then D-xylose. In both yeasts, the specific substrate-consumption rate diminished over each culture. The values q_s and q_E proved higher in Candida, although the higher ethanol yield was of the same order for both yeasts, close to 0.4 kg kg^у.     

D-xylose fermentation by Candida shehatae and pichia stipitis at low dissolved oxygen levels in fed-batch cultures

Summary The fermentation of D-xylose byCandida shehatae andPichia stipitis was studied in fed-batch fermentations using dissolved oxygen tension (DOT) control in the range of 0.2 to 1.4% air saturation. The response of these two yeasts to DOT was significantly different. Whereas the ethanol yield withC. shehatae was 0.35 to 0.38 g.g^–1 at all DOT levels, that ofP. stipitis decreased from 0.44 at a zero DOT reading to 0.19 g.g^–1 at 1.4% DOT.     

Xylose fermentation by Candida shehatae and Pichia stipitis: effects of pH,temperature and substrate concentration

The effects of temperature, pH and xylose concentration on the fermentation parameters of Candida shehatae and Pichia stipitis were evaluated. The optimum pH was in the region of pH 4–5.5, with an optimum fermentation temperature of 30°C. Maximum fermentation rates were reached at 50 g l⁻¹ xylose. A maximum volumetric ethanol productivity of about 0.9 g (l h)⁻¹ was obtained with both yeast strains. The ethanol yield of C. shehatae decreased considerably when cultivated above 30°C or when the xylose concentration was increased. Xylitol accumulated concomitantly. Xylitol production by P. stipitis was observed only during cultivation at 36°C. Whereas the ethanol yield of C. shehatae was usually about 75% of the theoretical maximum, it was 85–90% with P. stipitis.     

Simultaneous fermentation of D-xylose and glucose byCandida shehatae

Summary Mixtures of xylose and glucose were anaerobically fermented with the yeastCandida shehatae. Cells previously grown aerobically on glucose fermented glucose and xylose sequentially. Cells grown aerobically on xylose fermented glucose and xylose simultaneously, with no lag in xylose consumption. The best results were obtained with cells grown aerobically on xylose and inoculated into a 7525 mixture. 25 g/L of ethanol and 25 g/L of xylitol were obtained from 120 g/L of carbohydrates within 50 hours.     

Performance evaluation of Pichia kluyveri, Kluyveromyces marxianus and Saccharomyces cerevisiae in industrial tequila fermentation

Traditionally, industrial tequila production has used spontaneous fermentation or Saccharomyces cerevisiae yeast strains. Despite the potential of non-Saccharomyces strains for alcoholic fermentation, few studies have been performed at industrial level with these yeasts. Therefore, in this work, Agave tequilana juice was fermented at an industrial level using two non-Saccharomyces yeasts (Pichia kluyveri and Kluyveromyces marxianus) with fermentation efficiency higher than 85 %. Pichia kluyveri (GRO3) was more efficient for alcohol and ethyl lactate production than S. cerevisiae (AR5), while Kluyveromyces marxianus (GRO6) produced more isobutanol and ethyl-acetate than S. cerevisiae (AR5). The level of volatile compounds at the end of fermentation was compared with the tequila standard regulation. All volatile compounds were within the allowed range except for methanol, which was higher for S. cerevisiae (AR5) and K. marxianus (GRO6). The variations in methanol may have been caused by the Agave tequilana used for the tests, since this compound is not synthesized by these yeasts.     

Alcoholic fermentation of D-xylose by immobilizedPichia stipitis yeast

Summary Pichia stipitis NRRL Y-7124 yeast cells were for the first time immobilized both in agar gel beads and on fine nylon net for ethanol fermentation on D-xylose, in order to investigate the possibility of using the biocatalyst for improved utilization of the biomass pentose fraction. With free cells the initial xylose level affected little ethanol production, with a maximum of 22 g/l ethanol obtained in 5 days on 5% and of 40 g/l in 8 days on 10% xylose, and an average volumetric productivity of about 0.22 g/lh. The maximum ethanol concentration of 19.5% on 5% xylose with the nylon net attached cells in a continuous packed-bed column reactor was obtained with 35 h residence time. The volumetric productivities of 0.56 g/lh at 19.5 g/l ethanol and 1.0 g/lh at 15.0 g/l ethanol were markedly higher than those obtained with free cells. The stability of the immobilized biocatalyst was excellent. The same reactor could be used for at least 80 days without significant activity loss.     

The induction of D-xylose catabolizing enzymes inPachysolen tannophilus and the relationship to anaerobic D-xylose fermentation

Summary Aerobic cultures harvested from the lag and early exponential growth phases fermented D-xylose poorly under anaerobic conditions whereas fermentation by late exponential and stationary phase cultures was rapid. These differences could be related to the ratios of NADH- to NADPH-linked xylose reductase (XR) and the levels of NADH-linked XR and NAD-linked xylitol dehydrogenase (XD) present. Under aerobic conditions, induction of NADPH-linked XR preceded NADH-linked XR which suggested the presence of two separate XR't's. Induction of XR and XD was more rapid under aerobic than anaerobic conditions.     

Effect of aerobiosis on fermentation and key enzyme levels during growth of Pichia stipitis,Candida shehatae and Candida tenuis on d-xylose

The relationship between the degree of aerobiosis, xylitol production and the initial two key enzymes of d-xylose metabolism were investigated in the yeasts Pichia stipitis, Candida shehatae and C. tenuis. Anoxic conditions severely curtailed growth and retarded ethanol productivity. This, together with the inverse relationship between xylitol accumulation and aeration level, suggested a degree of redox imbalance. The ratios of NADH- to NADPH-linked xylose reductase were similar in all three yeasts and essentially independent of the degree of aerobiosis, and thus did not correlate with their differing capacities for ethanol production, xylitol accumulation or growth under the different conditions of aerobiosis. Under anoxic conditions the enzyme activity of Pichia stipitis decreased significantly, which possibly contributed to its weaker anoxic fermentation of xylose compared to C. shehatae.     

Segregation of altered parental properties in fusions between Saccharomyces cerevisiae and the D-xylose fermenting yeasts Candida shehatae and Pichia stipitis.

A prototrophic strain of Saccharomyces cerevisiae CSIR Y190 MATa xyl-, resistant to high levels of ethanol, was hybridized with xylose-fermenting, auxotrophic mutants of Candida shehatae and Pichia stipitis through polyethylene glycol-induced protoplast fusion in an attempt to produce ethanol-tolerant, xylose-fermenting hybrids. Mononucleate fusants were obtained, but these dissociated into a mixture of parental-type segregants. Purified Candida- and Pichia-resembling segregants failed to acquire improved ethanol tolerance but expressed other novel properties of S. cerevisiae, suggesting that karyogamy was impaired after internuclear gene transfer.     

Comparison of different pretreatments in ethanol fermentation using corn cob hemicellulosic hydrolysate with Pichia stipitis and Candida shehatae

A hemicellulosic hydrolysate was prepared with 0.3 M H₂SO₄ at 98 °C for 1 h. The total initial reducing sugar was maintained at 45 g l^–1 by synthetic xylose supplementation. The seven detoxification methods were employed including either the single addition of solid CaO (to pH 10 or 6) or its combinations with zeolite shaking. Over-liming gave the hydrolysate that was most completely fermented by Pichia stipitis and Candida shehatae at 30 °C, pH 6, among the tested methods.     

The effect of pH on kinetic and yield parameters during the ethanolic fermentation of D-xylose with Pachysolen tannophilus

We have studied the ethanolic fermentation of D-xylose with Pachysolen tannophilus in batch cultures. We propose a model to predict variations in D-xylose consumed, and biomass and ethanol produced, in which we include parameters for the specific growth rate, for the consumption of D-xylose and production of ethanol either related or not to growth.The ideal initial pH for ethanol production turned out to be 4.5. At this pH value the net specific growth rate was 0.26 h^–1, biomass yield was 0.16 g.g^–1, the cell-maintenance coefficient was 0.073 g.g^–1.h^–1, the parameter for ethanol production non-related to growth was 0.064 g.g^–1,h^–1 and the maximum ethanol yield was 0.32 g.g^–1.List of Symbols A _c Carbon atomic weight - a _d1/h Specific cell-maintenance rate defined in Eq. (8) - c Mass fraction of carbon in the biomass - E g/l Ethanol concentration - f _x Correction factor defined in Eq. (13) - f _x Correction factor defined in Eq. (13) - f _xi Correction factor defined in Eq. (14) - k _d1/h Death constant - M _E Ethanol molecular weight - M _s Xylose molecular weight - M _xi Xylitol molecular weight - m g xylose/g biomass Maintenance coefficient for substrate - m _dg xylose/g biomass Maintenance coefficient when k _d - q _Eg ethanol/g biomass. Specific ethanol production rate - s g/l Residual xylose concentration - s ₀ g/l Initial xylose concentration - t h Time - x g/l Biomass concentration - x ₀ g/l Initial biomass concentration - Y _E/sg ethanol/g xylose Instantaneous ethanol yield - ¯Y _E/sg ethanol/g xylose Mean ethanol yield - Y _E ^s/T g ethanol/g xylose Theoretical ethanol yield - Y _E ^s/* g ethanol/g xylose Corrected instantaneous ethanol yield - ¯Y _E ^s/* g ethanol/g xylose Corrected mean ethanol yield - Y _x/sg biomass/g xylose Biomass yield - ¯Y _xi/sg xylitol/g xylose Mean xylitol yield Greek Letters g ethanol/g biomass Growth-associated product formation parameter - g ethanol/g biomass.h Non-growth-associated product formation parameter - _dg ethanol/g biomass.h Non-growth-associated product formation parameter when k _d0 - h Variable defined in Eq. (6) or Eq. (7) - 1/h Specific growth rate - _m1/h Maximum specific growth rate     

The effect of respiratory inhibitors on the fermentative ability of Pichia stipitis,Pachysolen tannophilus and Saccharomyces cerevisiae under various conditions of aerobiosis

Summary The growth and ethanol production by the d-xylose-fermenting yeasts Pichia stipitis and Pachysolen tannophilus under various conditions of aerobiosis responded similarly to the addition of the respiratory inhibitors potassium cyanide (KCN), antimycin A (AA), sodium azide and rotenone. However, the d-glucose-fermenting yeast Saccharomyces cerevisiae differed markedly from these yeasts in response to the inhibitors. In general the growth of the d-xylose-fermenting yeasts was inhibited by the respiratory inhibitors while ethanol production was either stimulated (especially when oxygen was available) or unaffected or inhibited by rotenone or AA or KCN and sodium azide, respectively. However, by exception KCN and AA stimulated ethanol production under aerobic conditions by Pichia stipitis and Pachysolen tannophilus respectively. Stimulatory or inhibitory effects by respiratory inhibitors were less marked in S. cerevisiae. These data suggest that unimpaired mitochondrial function is necessary for growth on d-xylose and optimal d-xylose fermentation. A requirement for membrane generated energy during d-xylose utilisation is indicated by 2,4-dinitrophenol inhibition of growth and fermentation.     

The role of alcohol dehydrogenase in the fermentation of D-xylose byCandida shehatae ATCC 22984

Summary When the oxygen supply to an aerobic chemostat culture ofCandida shehatae growing on D-xylose was reduced to oxygen-limited and anoxic conditions, accumulation of ethanol occurred, the specific activity of alcohol dehydrogenase (ADH) increased up to four-fold and the number of ADH isozymes detected increased from one to three. ADH in crude extracts prepared from anoxically-grown cells had a lower affinity for but was more tolerant to ethanol than in extracts prepared from aerobically grown cells. ADH activity appeared to be sufficient for ethanol production byC. shehatae under anoxic conditions.Maintained in cooperation with the University of Wisconsin-Madison. The use of trade, firm or corporation names in this publication is for the information and convenience of the reader. Such use does not constitute an official endorsement or approval by the US Department of any product or service to the exclusion of others which may be suitable.