Microbial Production of Xylitol from Glucose

A microbiological method is described for the production of xylitol, which is used as a sugar substitute for diabetics. A sequential fermentation process yielded 9.0 g of xylitol from 77.5 g of glucose via D-arabitol and D-xylulose. Candida guilliermondii var. soya (ATCC 20216) consumed 5.1 g of D-xylulose and produced 2.8 g of xylitol per 100 ml. Pentitol production from D-xylulose by yeasts was divided into three types: I, yeast-produced xylitol; II, yeast-produced D-arabitol; and III, yeast-produced xylitol and D-arabitol. D-Xylulose, but not glucose, was dissimilated to xylitol by yeasts under aerobic conditions.     

Microbial production of xylitol from D-xylose and sugarcane bagasse hemicellulose using newly isolated thermotolerant yeast Debaryomyces hansenii

A thermotolerant yeast capable of fermenting xylose to xylitol at 40°C was isolated and identified as a strain of Debaryomyces hansenii by ITS sequencing. This paper reports the production of xylitol from D-xylose and sugarcane bagasse hemicellulose by free and Ca-alginate immobilized cells of D. hansenii. The efficiency of free and immobilized cells were compared for xylitol production from D-xylose and hemicellulose in batch culture at 40°C. The maximum xylitol produced by free cells was 68.6 g/L from 100 g/L of xylose, with a yield of 0.76 g/g and volumetric productivity 0.44 g/L/h. The yield of xylitol and volumetric productivity were 0.69 g/g and 0.28 g/L/h respectively from hemicellulosic hydrolysate of sugarcane bagasse after detoxification with activated charcoal and ion exchange resins. The Ca-alginate immobilized D. hansenii cells produced 73.8 g of xylitol from 100 g/L of xylose with a yield of 0.82 g/g and volumetric productivity of 0.46 g/L/h and were reused for five batches with steady bioconversion rates and yields.     

Xylitol production from D-xylose byCandida guillermondii: Fermentation behaviour

Summary The ability ofCandida guillermondii to produce xylitol from xylose and to ferment individual non xylose hemicellulosic derived sugars was investigated in microaerobic conditions. Xylose was converted into xylitol with a yield of 0,63 g/g and ethanol was produced in negligible amounts. The strain did not convert glucose, mannose and galactose into their corresponding polyols but only into ethanol and cell mass. By contrast, fermentation of arabinose lead to the formation of arabitol. On D-xylose medium,Candida guillermondii exhibited high yield and rate of xylitol production when the initial sugar concentration exceeded 110 g/l. A final xylitol concentration of 221 g/l was obtained from 300 g/l D-xylose with a yield of 82,6% of theoretical and an average specific rate of 0,19 g/g.h.Nomenclature Q_p average volumetric productivity of xylitol (g xylitol/l per hour) - q_p average specific productivity of xylitol (g xylitol/g of cells per hour) - So initial xylose concentration (g/l) - tf incubation time (hours) - Y_P/S xylitol yield (g of xylitol produced/g of xylose utilized) - Y_E/S ethanol yield (g of ethanol produced/g of substrate utilized) - Y_X/S cells yield (g of cells/g of substrate utilized) - specific growth rate coefficient (h^–1) - _max maximum specific growth rate coefficient (h^–1)     

Fermentation of D-xylose, xylitol, and D-xylulose by yeasts

Fifteen yeasts which can assimilate D-xylose were examined for the ability to convert this pentose to ethanol. In six of the seven genera investigated the conversion was enhanced when air had access to the medium. Therefore, the ability to convert D-xylose to ethanol under these conditions is probably common among yeasts. Growth under the same conditions on xylitol, a putative catabolite of D-xylose, led to only traces of ethanol. The effects of growth on another putative catabolite, D-xylose, were complex, but some of the strains which were among the better producers of ethanol from D-xylose produced less from D-xylulose.     

Conversion of pentoses by yeasts

The utilization and conversion of D-xylose, D-xylulose, L-arabinose, and xylitol by yeast strains have been investigated with the following results: (1) The majority of yeasts tested utilize D-xylose and produce polyols, ethanol, and organic acids. The type and amount of products formed varies with the yeast strains used. The most commonly detected product is xylitol. (2)The majority of yeasts tested utilize D-xylulose aerobically and fermentatively to produce ethanol, xylitol, D-arabitol, and organic acids. The type and amount of products varies depending upon the yeast strains used. (3) Xylitol is a poor carbon and energy source for most yeasts tested. Some yeast strains produce small amounts of ethanol from xylitol. (4) Most yeast strains utilize L-arabinose, and L-arabitol is the common product. Small amounts of ethanol are also produced by some yeast strains. (5) Of the four substrates examined, D-xylulose was the perferred substrate, followed by D-xylose, L-arabinose, and xylitol. (6) Mutant yeast strains that exhibit different metabolic product patterns can be induced and isolated from Candida sp. Saccharomyces cerevisiae, and other yeasts. These mutant strains can be used for ethanol production from D-xylose as well as for the study of metabolic regulation of pentose utilization in yeasts.     

Induction of NADPH-linked D-xylose reductase and NAD-linked xylitol dehydrogenase activities in Pachysolen tannophilus by D-xylose, L-arabinose, or D-galactose

Considerable interest in the D-xylose catabolic pathway of Pachysolen tannophilus has arisen from the discovery that this yeast is capable of fermenting D-xylose to ethanol. In this organism D-xylose appears to be catabolized through xylitol to D-xylulose. NADPH-linked D-xylose reductase is primarily responsible for the conversion of D-xylose to xylitol, while NAD-linked xylitol dehydrogenase is primarily responsible for the subsequent conversion of xylitol to D-xylulose. Both enzyme activities are readily detectable in cell-free extracts of P. tannophilus grown in medium containing D-xylose, L-arabinose, or D-galactose and appear to be inducible since extracts prepared from cells growth in media containing other carbon sources have only negligible activities, if any. Like D-xylose, L-arabinose and D-galactose were found to serve as substrates for NADPH-linked reactions in extracts of cells grown in medium containing D-xylose, L-arabinose, or D-galactose. These L-arabinose and D-galactose NADPH-linked activities also appear to be inducible, since only minor activity with L-arabinose and no activity with D-galactose is detected in extracts of cells grown in D-glucose medium. The NADPH-linked activities obtained with these three sugars may result from the actions of distinctly different enzymes or from a single aldose reductase acting on different substrates. High-performance liquid chromatography and gas-liquid chromatography of in vitro D-xylose, L-arabinose, and D-galactose NADPH-linked reactions confirmed xylitol, L-arabitol, and galactitol as the respective conversion products of these sugars. Unlike xylitol, however, neither L-arabitol nor galactitol would support comparable NAD-linked reaction(s) in cellfree extracts of induced P. tannophilus. Thus, the metabolic pathway of D-xylose diverges from those of L-arabinose or D-galactose following formation of the pentitol.     

Levels of enzymes of the pentose phosphate pathway in Pachysolen tannophilus Y-2460 and selected mutants

The compositions of intracellular pentose phosphate pathway enzymes have been examined in mutants of Pachysolen tannophilus NRRL Y-2460 which possessed enhanced D-xylose fermentation rates. The levels of oxidoreductive enzymes involved in converting D-xylose to D-xylulose via xylitol were 1.5–14.7-fold higher in mutants than in the parent. These enzymes were still under inductive control by D-xylose in the mutants. The D-xylose reductase activity (EC 1.1.1.21) which catalyses the conversion of D-xylose to xylitol was supported with either NADPH or NADH as coenzyme in all the mutant strains. Other enzyme specific activities that generally increased were: xylitol dehydrogenase (EC 1.1.1.9), 1.2–1.6-fold; glucose-6-phosphate dehydrogenase (EC 1.1.1.49), 1.9–2.6-fold; D-xylulose-5-phosphate phosphoketolase (EC 4.1.2.9), 1.2–2.6-fold; and alcohol dehydrogenase (EC 1.1.1.1), 1.5–2.7-fold. The increase of enzymatic activities, 5.3–10.3-fold, occurring in D-xylulokinase (EC 2.7.1.17), suggested a pivotal role for this enzyme in utilization of D-xylose by these mutants. The best ethanol-producing mutant showed the highest ratio of NADH- to NADPH-linked D-xylose reductase activity and high levels of all other pentose phosphate pathway enzymes assayed.     

Novel enzymatic method for the production of xylitol from D-arabitol by Gluconobacter oxydans

Microorganisms capable of producing xylitol from D-arabitol were screened for. Of the 420 strains tested, three bacteria, belonging to the genera Acetobacter and Gluconobacter, produced xylitol from D-arabitol when intact cells were used as the enzyme source. Among them, Gluconobacter oxydans ATCC 621 produced 29.2 g/l xylitol from 52.4 g/l D-arabitol after incubation for 27 h. The production of xylitol was increased by the addition of 5% (v/v) ethanol and 5 g/l D-glucose to the reaction mixture. Under these conditions, 51.4 g/l xylitol was obtained from 52.4 g/l D-arabitol, a yield of 98%, after incubation for 27 h. This conversion consisted of two successive reactions, conversion of D-arabitol to D-xylulose by a membrane-bound D-arabitol dehydrogenase, and conversion of D-xylulose to xylitol by a soluble NAD-dependent xylitol dehydrogenase. Use of disruptants of the membrane-bound alcohol dehydrogenase genes suggested that NADH was generated via NAD-dependent soluble alcohol dehydrogenase.     

Effect of hydrogen acceptors on D-xylose fermentation by anaerobic culture of immobilized Pachysolen tannophilus cells

The effect of hydrogen acceptors on the kinetic parameters of D-xylose fermentation under anaerobic conditions was studied in a transient culture of immobilized Pachysolen tannophilus cells. Addition of oxygen to a steady-state culture resulted in a rapid increase (up to fivefold) in the rates of ethanol production and D-xylose uptake, but the rate of xylitol production was unaffected. Furthermore, the molar ethanol yield increased from 0.97 to 1.43 in the presence of oxygen. The moles of ethanol produced per moles of oxygen utilized were considerably greater than would be predicted from the stoichiometry of D-xylose fermentation, which suggests that the organism required oxygen for other functions in addition to its role as a hydrogen acceptor in D-xylose metabolism. When the artificial hydrogen acceptors acetone, acetaldehyde, and acetoin were added to the culture, the rate of ethanol production increased while the xylitol production rate decreased but the rate of xylose uptake was unaffected. The molar ethanol yields increased from 1.03 to 1.63, 1.43, and 1.24 upon addition of acetaldehyde, acetone, and acetoin, respectively, at the expense of the molar xylitol yields. The hydrogen acceptors sodium acetate, methylene blue, benzyl viologen, phenazine methosulfate, indigo carmine, and tetrazolium chloride had no effect on ethanol production.     

Growth of yeasts on D-xylulose 1

Nine of eleven yeasts of different species or genera grew in the presence of air on the intermediate of D-xylose catabolism, D-xylulose (D-threo-pentulose). Growth on this substrate was efficient as judged by the optical density in stationary phase being generally similar to that after growth on glucose. Yeasts which grew on D-xylose also did so on D-xylulose, but among those which grew are included several which utilise neither D-xylose nor xylitol: Saccharomyces cerevisiae, Saccharomyces carlsbergensis, and Schizosaccharomyces pombe. Since catabolism of a sugar generally requires an initial phosphorylation step, growth of these strains suggests that they contain an enzyme which can function as a D-xylulose kinase. The D-xylulose-5-phosphate formed thereby is considered to enter the pentose-phosphate pathway. Glucose-grown inocula of S. carlsbergensis and Schizosaccharomyces pombe, and of several other yeasts, began to grow logarithmically when placed on D-xylulose with no apparent delay, or one which was minimal, suggesting that the D-xylulose kinase was already present in such cells, or was rapidly induced. Petites of S. cerevisiae did not grow on D-xylulose indicating that, in this species, mitochondria are involved in its utilisation.     

Optimization of D-xylose to xylitol biotransformation by Candida guilliermondii cells permeabilized with Triton X-100

Abstract

The effect of NADP⁺ and glucose-6-phosphate (G6P) on the biotransformation of D-xylose to xylitol by cells of Candida guilliermondii permeabilized with surfactant Triton X-100 was evaluated. The experimental runs were performed with 12 g L^?1 of permeabilized cells and a reaction medium composed of Tris–HCl buffer (0.1 M pH 7), D-xylose (57 g L^?1), and MgCl₂.6H₂O (5 mM). The levels of NADP⁺ (from 0.0 to 1.7 mM) and G6P (from 0.00 to 0.17 M) were varied according a 2²-full factorial composed design. Under optimized conditions (NADP⁺ 0.5 mM and 0.05 M G6P), the xylitol volumetric productivity (Q_P) and yield factor (Y_P/S) predicted were 1.86 ± 0.03 g L^?1 h^{? 1} and 0.64 ± 0.03 g g^?1, respectively. These values were 94% and 19% higher than those obtained with unpermeabilized cells under fermentation conditions (0.97 g L^?1 h^?1 and 0.53 g g^?1, respectively). On the basis of the results, it can be concluded that xylitol production by biotransformation with cells of C. guilliermondii permeabilized with Triton X-100 is a promising alternative to the fermentative process.     

Xylitol Production by a Corynebacterium Species

The washed cells of a gluconate-utilizing Corynebacterium strain grown in a gluconate- xylose medium produced xylitol from D-xylose in the presence of gluconate. The amount of xylitol was progressively increased with increasing gluconate concentration.

An extract of cells grown in the gluconate-xylose medium showed NADPH-dependent D-xylose reductase activity and NADP-dependent 6-phosphogluconate dehydrogenase activity.

These enzymes in the cell-free extract were purified by Sephadex G–100 gel filtration.

The reduction of D-xylose to xylitol was demonstrated by the coupling the D-xylose reductase activity to the 6-phosphogluconate dehydrogenase activity with NADP as a cofactor using the cell-free extract and the fractionated enzymes.     

Enzymatic Regeneration of NAD in Enantioselective Oxidation of Secondary Alcohols: Glutamate Dehydrogenase Versus NADH Dehydrogenase

To improve yield and productivity of ketose in NAD-dependent polyol oxidations, two enzymatic methods for regeneration of the oxidized coenzyme form have been compared and partly optimized for the batch conversion of xylitol into D-xylulose and D-sorbitol into D-fructose. Polyol oxidation was catalyzed by xylitol dehydrogenase from the yeast Galactocandida mastotermitis. Reduction of OM₂ (apparently to H₂O) by partially purified NADH dehydrogenase complex from Corynebacterium callunae could drive alcohol oxidations better than reductive amination of EaL-ketoglutarate by glutamate dehydrogenase. A fed-batch procedure was developed that overcame inhibition of glutamate dehydrogenase by α-ketoglutarate (K_is 25 mM), thus increasing the productivity of ketose almost 2-fold. For D-fructose production from D-sorbitol (0.1-0.3M) yields of < 90% and productivities up to 1.30g/(L.h) have been obtained. High conversion of up to 50g/L xylitol into D-xylulose for which xylitol dehydrogenase exhibits an about 80-fold higher specificity constant than for D-fructose required complexation of the ketose product with borate. In comparison with reductive amination by glutamate dehydrogenase, advantages of using NADH-dehydrogenase catalyzed regeneration of NAD for ketose production are (i) avoidance of byproduct formation, (ii) cheaper substrate (02 versus α-ketoglutarate), and (iii) easier process control (batch versus fed-batch).     

D-xylulose-induced depletion of ATP and Pi in isolated rat hepatocytes

Xylitol is known to cause hepatic ATP catabolism by inducing the trapping of Pi in the form of glycerol 3-P as a consequence of an increase in the NADH:NAD+ ratio, resulting from the oxidation of xylitol to D-xylulose. The question was therefore raised whether D-xylulose also depletes hepatic ATP. In isolated rat hepatocytes, 5 mM D-xylulose decreased ATP by 80% within 5 min compared to 40% with 5 mM xylitol. Intracellular Pi decreased by 70% within the same time interval with both compounds, but was restored three-fold faster with D-xylulose. The rate of utilization of D-xylulose reached 5 mumol.min-1.g-1 of cells, as compared with 1.5 for xylitol, indicating that reduction of xylitol into D-xylulose is a rate-limiting step in the metabolism of the polyol. D-Xylulose barely modified the concentration of glycerol 3-P but increased xylulose 5-P from 0.02 to 0.5 mumol/g within 5 min. The main cause of the ATP- and Pi-depleting effects of D-xylulose was found to be an accumulation of sedoheptulose 7-P from a basal value of 0.1 to 5 mumol/g of cells after 10 min. Ribose 5-P increased from 0.03 to 0.5 mumol/g at 5 min. Ribose 1-P also accumulated, albeit outside of the cells. This extracellular accumulation can be explained by the release of intracellular purine nucleoside phosphorylase from damaged hepatocytes acting on inosine that had diffused out of the cells. Smaller increases in the concentrations of sedoheptulose 7-P and pentose phosphates were recorded after incubations of the cells with xylitol.     

D-xylose catabolizing enzymes in Neurospora crassa and their relationship to D-xylose fermentation

Summary The induction of xylose reductase (XR) and xylitol dehydrogenase (XD) activities by D-xylose under different fermentation conditions was investigated in Neurospora crassa. The induction of NADPH-linked XR preceded NADH-linked XR and the ratio of NADH to NADPH-linked XR activity displayed variation from 0.02 to 0.2 suggesting the presence of two separate enzymes. Aerobic conditions were required by N. crassa for cell growth but not for ethanol production. Maximum ethanol of 0.3 g/g of D-xylose was produced when shifted to semiaerobic condition, where high NADH-linked XR and NAD-linked XD activities were observed.     

Study of the potential of the air lift bioreactor for xylitol production in fed-batch cultures by Debaryomyces hansenii immobilized in alginate beads

Cell immobilization has shown to be especially adequate for xylitol production. This work studies the suitability of the air lift bioreactor for xylitol production by Debaryomyces hansenii immobilized in Ca-alginate operating in fed-batch cultures to avoid substrate inhibition. The results showed that the air lift bioreactor is an adequate system since the minimum air flow required for fluidization was even lower than that leading to the microaerobic conditions that trigger xylitol accumulation by this yeast, also maintaining the integrity of the alginate beads and the viability of the immobilized cells until 3 months of reuses. Maximum productivities and yields of 0.43 g/l/h and 0.71 g/g were achieved with a xylose concentration of 60 g/l after each feeding. The xylose feeding rate, the air flow, and the biomass concentration at the beginning of the fed-batch operation have shown to be critical parameters for achieving high productivities and yields. Although a maximum xylitol production of 139 g/l was obtained, product inhibition was evidenced in batch experiments, which allowed estimating at 200 and 275 g/l the IC₅₀ for xylitol productivity and yield, respectively. The remarkable production of glycerol in the absence of glucose was noticeable, which could not only be attributed to the osmoregulatory function of this polyol in conditions of high osmotic pressure caused by high xylitol concentrations but also to the role of the glycerol synthesis pathway in the regeneration of NAD⁺ in conditions of suboptimal microaeration caused by insufficient aeration or high oxygen demand when high biomass concentrations were achieved.     

Aerobic and sequential anaerobic fermentation to produce xylitol and ethanol using non-detoxified acid pretreated corncob

Background

For economical bioethanol production from lignocellulosic materials, the major technical challenges to lower the production cost are as follows: (1) The microorganism should use efficiently all glucose and xylose in the lignocellulose hydrolysate. (2) The microorganism should have high tolerance to the inhibitors present in the lignocellulose hydrolysate. The aim of the present work was to combine inhibitor degradation, xylitol fermentation, and ethanol production using a single yeast strain.

Results

A new process of integrated aerobic xylitol production and anaerobic ethanol fermentation using non-detoxified acid pretreated corncob by Candida tropicalis W103 was proposed. C. tropicalis W103 is able to degrade acetate, furfural, and 5-hydromethylfurfural and metabolite xylose to xylitol under aerobic conditions, and the aerobic fermentation residue was used as the substrate for ethanol production by anaerobic simultaneous saccharification and fermentation. With 20% substrate loading, furfural and 5-hydroxymethylfurfural were degraded totally after 60 h aerobic incubation. A maximal xylitol concentration of 17.1 g l^-1 was obtained with a yield of 0.32 g g^-1 xylose. Then under anaerobic conditions with the addition of cellulase, 25.3 g l^-1 ethanol was produced after 72 h anaerobic fermentation, corresponding to 82% of the theoretical yield.

Conclusions

Xylitol and ethanol were produced in Candida tropicalis W103 using dual-phase fermentations, which comprise a changing from aerobic conditions (inhibitor degradation and xylitol production) to anaerobic simultaneous saccharification and ethanol fermentation. This is the first report of integrated xylitol and ethanol production from non-detoxified acid pretreated corncob using a single microorganism.

     

Effect of nitrogen sources on xylitol production from D-xylose by Candida Sp. L-102

Summary The production of extracellular xylitol from D-xylose by an efficient xylitol-producing yeast, Candida sp. L-102, was studied in shake flask cultures with different nitrogen sources in the basic salt medium. Maximum xylitol production was obtained with urea as the nitrogen source. A final concentration of 100 g/L of xylitol from 114 g/L D-xylose was obtained from the yeast with an indicated yield of 87.7% (based on D-xylose consumed). The average specific xylitol production rate of 0.46 g/g.h was achieved within 65 hours of incubation using 0.3% urea.     

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.     

D-xylulose fermentation in yeasts

Summary With pure D-xylulose as substrate, Schizosaccharomyces pombe produced ethanol in good yield with low quantities of polyols as by-products. Saccharomyces cerevisiae was found to be a good alcohol producer in glucose but not as good in D-xylulose. Other yeast cultures converted D-xylulose to xylitol, or D-arabitol or both, with lower ethanol yield.