Effect of pH on cell viability and product yields in d-xylose fermentations by Candida shehatae

 Candida shehatae were sequentially subjected to aerobic conditions for cellular growth, followed by anaerobic conditions for ethanol production from D-xylose at pH 2.5, 4.5 and 6.0. Ethanol yields increased from 0.25 g/g to 0.37 g/g and xylitol yields decreased from 0.33 g/g to 0.1 g/g as the pH was increased from 2.5 to 6.0. Cell viability, measured by plate counts and methylene blue staining, decreased in all of the fermentations, following the switch from aerobic to anaerobic conditions. However, pH 6.0 was shown to extend cell viability and increase the final ethanol concentration from 45 g/l to 55 g/l, compared to the yield at pH 4.5. Received: 25 April 1995/Received revision: 5 September 1995/Accepted: 20 September 1995     

Xylose metabolism by Candida shehatae in continuous culture

Summary Xylose metabolism by Candida shehatae in continuous culture was examined under both fully-aerobic and semi-aerobic conditions. Growth did not occur in the absence of respiration. Under fully-aerobic conditions, the cell yield was constant at 0.51 g/g and the specific respiration rate Q _{o 2} was linearly related to the specific growth rate with a slope of 15 mmol g^-1 and an intercept of 1.2 mmol g^-1 h^-1. Under semi-aerobic conditions, Q _{O 2} was proportional to with a slope consistent with a cell yield from oxygen Y _{O 2} of 35±7 g mol^-1. The specific xylose uptake rate was a constant independent of and equal to the maximum rate of xylose transport. Ethanol production was observed under semi-aerobic conditions only, and the specific fermentation rate was inversely related to .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 U.S. Department of Agriculture of any product or service to the exclusion of others which may be suitableMaintained in cooperation with the University of Wisconsin-Madison     

Ethanol production from d-xylose in batch fermentations with Candida shehatae: process variables

Summary These studies examined several process variables important in scaling up the fermentation of xylose by Candida shehatae. Inoculum age and cell density were particularly influential. Young (24-h) inocula fermented xylose to ethanol two to three times as fast as older (48- or 72-h) inocula. With all three inocula ages, the initial fermentation rates were essentially linear with cell density, up to 4 g dry wt cells L^-1. Above that cell density, the ethanol production rate appeared to be oxygen limited, particularly with 24-h old cells. Aeration also played a role in xylose utilization. The fermentation proceeded under both aerobic and anaerobic conditions, but xylose was not completely utilized anaerobically. With aeration, 25% more ethanol was formed in about one third the time than without aeration. Ethanol yields were similar under the two conditions. Cell growth on xylose was observed in the absence of oxygen. Cells went through essentially one doubling in 24 h. Based on the sugar consumed, a Y_ATP of 9.9 was obtained. Slow continuous feeding of glucose significantly increased the xylose utilization rate.Maintained in cooperation with the University of Wisconsin, Madison, Wisconsin, USA     

Oxygen starvation induces cell death in Candida shehatae fermentations of d-xylose, but not d-glucose

Candida shehatae cells, cultivated on d-glucose and d-xylose, were subjected to a shift from fully aerobic to anaerobic fermentative conditions. After anaerobic conditions were imposed, growth was limited to approximately one doubling or less as C. shehatae rapidly entered a stationary phase of growth. Following the shift to anoxia, cell viability rapidly declined and the total cell volume declined in the d-xylose fermentations. Moreover, the cell volume distribution shifted to smaller volumes. Cell viability, measured by plate counts, declined nine times faster for d-xylose fermentations than for d-glucose fermentations. Anaerobic growth did not occur on either d-glucose or d-xylose. Selected vitamins and amino acids did not stimulate anaerobic growth in C. shehatae, but did enhance anaerobic growth on d-glucose in S. cerevisiae. The decline in cell viability and lack of anaerobic growth by C. shehatae were attributed to oxygen deficiency and not to ethanol inhibition. The results shed light on why C. shehatae anaerobic fermentations are not currently practical and suggest that research directed towards a biochemical understanding of why C. shehatae can not grow anaerobically will yield significant improvements in ethanol fermentations from d-xylose. Received 26 October 1998 / Received revision: 26 January 1999 / Accepted: 12 February 1999     

Effect of xylitol on the metabolism and viability of Candida shehatae

Anaerobic D-xylose fermentations were performed with C. shehatate in the presence of 0, 25, and 50 g/L of xylitol. D-Xylose was preferentially utilized over xylitol and ethanol yields (Y _Etoh/S 0.26 g/g) were unaffected by xylitol. Added xylitol did inhibit conversion of xylose to xylitol at an external xylitol concentration of 50 g/L; Y _Xylitol/S was reduced from 0.21 to 0.14. Cell viability declined in all of the fermentations, but was not due to the presence of xylitol. The decline in viability was attributed to oxygen deprivation, since ethanol levels only reached 10.5 g/L and the decline cell viability was the same in each fermentation, regardless of the xylitol concentration.     

Ethanol and sugar tolerance of Candida shehatae

Summary Candida shehatae ATCC 22984 fermented solutions of up to 260 g/L sugars derived by hydrolysis of whole barley. These solutions contained hexose: pentose 7030, the hexose being mainly glucose from the barley starch and the pentose being mainly xylose. At sugar concentrations of 180 g/L, fermentation was complete in 72 h, yielding 84 g/L ethanol, 0.47 g ethanol/g sugar. At 260 g/L, fermentation ceased when ethanol concentration reached 100 g/L, but resumed when the ethanol was removed by vacuum distillation, to yield finally 0.50 g ethanol/g sugar.     

Unstable petite and grande variants of Candida shehatae

Summary Two strains of Candida shehatae (ATCC 22984 and CSIR Y492) exhibit marked variability in colony size (petite, grande) and respiratory activity (tetrazolium reaction) when grown on glucose, xylose, and--especially--xylitol agar. The transitions occur in both directions at high frequency. Strains showing a negative or weak tetrazolium reaction on xylitol ferment xylose better than those showing a strong tetrazolium reaction. The type strain (ATCC 34887) shows stable colonial morphology with moderate respiratory and fermentative activities. The objective of this report is to demonstrate these variations.     

Assessment of Candida shehatae viability by flow cytometry and fluorescent probes

Quantification of different physiological states of Candida shehatae cells was performed by flow cytometry associated with two fluorescent probes. Propidium iodide and carboxyfluorescein diacetate acetoxymethyl ester fluorescent dyes were chosen based on data from the literature. A staining procedure, developed from the previous works was applied to the yeast. Then, the protocol was improved to fit with fermentation constraints such as no physiological interference between the staining procedure and the cells, shortest preparation time and small amounts of dyes. From this optimisation, propidium iodide was included in the sample at 8mg/L whereas carboxyfluorescein was first diluted in Pluronic? agent and used at 3mg/L, samples were incubated for 10min at 40°C. Repeatability and accuracy were evaluated to validate this flow cytometry procedure for viability determination.     

休哈塔假丝酵母发酵木糖制乙醇过程研究

木质纤维素原料水解产物的主要成分是葡萄糖和木糖,其中葡萄糖很容易发酵,致使木糖成为木质纤维素发酵的关键,休哈塔假丝酵母(Candida shehatae)1766是自然界木糖发酵性能较好的天然酵母之一。研究了发酵温度、发酵时间、接种量、初始pH值、摇床转速等因素对休哈塔假丝酵母1766发酵木糖生产乙醇的影响,由正交试验初步确定了休哈塔假丝酵母发酵木糖制乙醇工艺的适宜条件为好氧条件,发酵时间为2d,发酵温度为28℃,摇床转速为150r/min,初始pH值为5,此时乙醇收率最高可达68.62%。     

Simultaneous utilization of glucose and D-xylose by Candida shehatae in a chemostat

The kinetics of biomass formation, D-xylose utilization, and mixed substrate utilization were determined in a chemostat using the yeast Candida shehatae. The maximum growth rate of C. shehatae grown aerobically on D-xylose was 0.42 h⁻¹ and the Monod constant, K _s, was 0.06 g L⁻¹. The biomass yield, Y _{X/S}, ranged from 0.40 to 0.50 g g⁻¹ over a dilution rate range of 0.2–0.3 h⁻¹, when C. shehatae was grown on pure D-xylose. Mixtures of D-xylose and glucose (∼1 : 1) were simultaneously utilized over a dilution rate from 0.15 to 0.35 h⁻¹ at pH 3.5 and 4.5, but pH 3.5 reduced μ_max and reduced the dilution rate range over which D-xylose was utilized in the presence of glucose. At pH 4.5, μ_max was not reduced with the mixed sugar feed and the overall or lumped K _s value was not significantly increased (0.058 g L⁻¹ vs 0.06 g L⁻¹), when compared to a pure D-xylose feed. Kinetic data indicate that C. shehatae is an excellent candidate for chemostat production of value added products from renewable carbon sources, since simultaneous mixed substrate utilization was observed over a wide range of growth rates on a 1 : 1 mixture of glucose and D-xylose. Received 21 August 1997/ Accepted in revised form 28 May 1998     

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     

Oxidative d-xylose metabolism of Gluconobacter oxydans

Summary Gluconobacter oxydans subsp. suboxydans ATCC 621 oxidizes d-xylose to xylonic acid very efficiently, although it cannot grow on xylose as sole carbon source. The oxidation of xylose was found to be catalyzed by a membrane-bound xylose dehydrogenase. The xylono--lactone formed in the oxidation reaction is subsequently hydrolyzed to xylonic acid by a -lactonase. The complete oxidation pathway of d-xylose in G. oxydans is evidently located in the periplasmic space.     

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 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 vitamin requirements of Candida shehatae for xylose fermentation

Abstract The vitamin requirements of a strain of Candida shehatae for the fermentation of d -xylose was determined using a statistical procedure with a 2³ factorial design. Biotin as well as thiamine exerted a dramatic stimulatory effect on the rate of ethanol production, coupled with a significant improvement in the ethanol yield. The greatest enhancement of the fermentation was found in the presence of both these vitamins. Pyridoxine exerted only a minor effect, but was essential for complete substrate utilization in the absence of either biotin or thiamine. Only biotin caused a significant increase in the growth rate.     

Detoxification of sugarcane bagasse hydrolysate improves ethanol production by Candida shehatae NCIM 3501

Sugarcane bagasse hydrolysis with 2.5% (v/v) HCl yielded 30.29g/L total reducing sugars along with various fermentation inhibitors such as furans, phenolics and acetic acid. The acid hydrolysate when treated with anion exchange resin brought about maximum reduction in furans (63.4%) and total phenolics (75.8%). Treatment of hydrolysate with activated charcoal caused 38.7% and 57.5% reduction in furans and total phenolics, respectively. Laccase reduced total phenolics (77.5%) without affecting furans and acetic acid content in the hydrolysate. Fermentation of these hydrolysates with Candida shehatae NCIM 3501 showed maximum ethanol yield (0.48g/g) from ion exchange treated hydrolysate, followed by activated charcoal (0.42g/g), laccase (0.37g/g), overliming (0.30g/g) and neutralized hydrolysate (0.22g/g).     

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.     

Continuous alcoholic fermentation of glucose/xylose mixtures by co-immobilized Saccharomyces cerevisiae and Candida shehatae

Viable Saccharomyces cerevisiae and Candida shehatae cells were co-immobilized in a composite agar layer/microporous membrane structure. This immobilized-cell structure was placed in a vertical position between the two halves of a double-chambered, stainless-steel bioreactor of original design and applied to the continuous alcoholic fermentation of a mixture of glucose (35 g dm⁻³) and xylose (15 g dm⁻³). Various dilution rates and initial cell loadings of the gel layer were tested. Simultaneous consumption of the two sugars was always observed. The best fermentation performance was obtained at low dilution rate (0.02 h⁻¹) with an excess of C. shehatae over S. cerevisiae in the initial cell loading of the gel (5.0 mg dry weight and 0.65 mg dry weight cm⁻³ gel respectively): 100% of glucose and 73% of xylose were consumed with an ethanol yield coefficient of 0.48 g g total sugars⁻¹. In these conditions, however, the ethanol production rate per unit volume of gel remained low (0.37 g h⁻¹ dm⁻³). Viable cell counts in gel samples after incubation highlighted significant heterogeneities in the spatial distribution of the two yeast species in both the vertical and the transverse directions. In particular, the overall cell number decreased from the bottom to the top of the agar sheet, which may explain the low ethanol productivity relative to the total gel volume. Received: 26 February 1998 / Received revision: 15 April 1998 / Accepted: 19 April 1998