Effect of oxygen transfer rate on levels of key enzymes of xylose metabolism in Debaryomyces hansenii

The titers of key enzymes of xylose metabolism were measured and correlated with the kinetics of xylitol production by Debaryomyces hansenii under different oxygen transfer rates (OTR) in a batch reactor. An OTR change from 2.72 to 4.22 mmol O₂ l⁻¹ min⁻¹ resulted in a decrease in NADPH-dependent xylose reductase (XR) and NAD ± -dependent xylitol dehydrogenase (XDH) activities. For higher values of OTR (12.93 mmol O₂ l⁻¹ min⁻¹, the XDH titer increased twofold whereas the XR titer did not show a significant change. At the lowest OTR (2.72 mmol O₂ l⁻¹ min⁻¹), xylitol (and ethanol) production rates showed the highest values. However, xylitol specific productivity was twice as high as ethanol specific productivity. The titer of the NADPH-forming enzyme, glucose-6-phosphate dehydrogenase (GPDH), increased from 333 to 412 mU mg⁻¹ when the OTR was increased. However, 6-phosphogluconate dehydrogenase (PGDH) activity remained unchanged and at a lower level, which indicates that this enzyme is responsible for the carbon flux control of the oxidative branch of the pentose phosphate pathway. The activity of the alcohol-forming enzyme was repressed at the higher amount of oxygen, decreasing its activity more than 50%. The changes in ADH suggested that two different metabolic regions under oxygen-limited conditions can be hypothesized for xylose metabolism by D. hansenii. For low OTR values (up to 4.22 mmol O₂ l⁻¹ min⁻¹), a fermentative-type activity is displayed. At higher OTR values (above 4.22 mmol O₂ l⁻¹ min⁻¹), no significant fermentative activity is reported.     

Xylitol production in immobilized cultures: a recent review

Xylitol is a pentahydroxy sugar alcohol coming from xylose with many applications in the food and pharmaceutical industries as a low caloric sweetener suitable for diabetics and as an active ingredient in several biomedical applications. The microbial bioproduction of xylitol from natural xylose coming from lignocellulosic materials appears a sustainable and a promising alternative to chemical synthesis, which works at stronger reaction conditions and generates undesirable co-products which must be removed. There are several reviews that study the metabolic pathways in wild and transformed xylitol producing yeasts and the culture conditions that enhance xylitol accumulation, which are mainly related to the need of microaerobiose for the best producing wild yeasts. Nevertheless, there are relatively few studies focusing on the engineering aspects related to scalable systems and bioreactors that could result in a final industrial stage. This review explores recent advances on xylitol production using immobilized systems, which have been proposed to facilitate the reuse of the biocatalyst for extended periods and the main types of bioreactors available assayed for this purpose.     

Transaldolase/Glucose-6-phosphate Isomerase Bifunctional Enzyme and Ribulokinase as Factors to Increase Xylitol Production from D-Arabitol in Gluconobacter oxydans

Xylitol production from D-arabitol by the membrane and soluble fractions of Gluconobacter oxydans was investigated. Two proteins in the soluble fraction were found to have the ability to increase xylitol production. Both of these xylitol-increasing factors were purified, and on the basis of their NH₂-terminal amino acid sequences the genes encoding both of the factors were cloned. Expression of the cloned genes in Escherichia coli showed that one of the xylitol-increasing factors is the bifunctional enzyme transaldolase/glucose-6-phosphate isomerase, and the other is ribulokinase. Using membrane and soluble fractions of G. oxydans, 3.8 g/l of xylitol were produced from 10 g/l D-arabitol after incubation for 40 h, and addition of purified recombinant transaldolase/glucose-6-phosphate isomerase or ribulokinase increased xylitol to 5.4 g/l respectively, confirming the identity of the xylitol-increasing factors.     

Characterization of Genes Involved in D-Sorbitol Oxidation in Thermotolerant Gluconobacter frateurii

A microbial screening indicated that two fungal strains, Beauveria bassiana DSM 1344=ATCC 7159 and Cunninghamella elegans DSM 1908=ATCC 9245, as well as four bacterial strains belonging to the genus Streptomyces were able to hydroxylate 4,5-dianilinophthalimide (DAPH, CGP52411) to 4-(4′-hydroxyanilino)-5-anilinophthalimide. Cunninghamella elegans DSM 1908 turned out to be the most active biocatalyst and was also able to form the dihydroxy derivative, 4,5-bis(4′-hydroxyanilino)phthalimide. The reaction for the monohydroxylated biotransformation product was carried out on a preparative scale, and the culture conditions for the formation of 4-(4′-hydroxy- anilino)-5-anilinophthalimide with this strain were op-timized.     

可同化阿拉伯糖的木糖还原酿酒酵母菌株构建

[目的] 以秸秆等木质纤维素类生物质为原料生产液体生物燃料乙醇,目前生产成本高,大规模工业化生产尚有较大难度。构建能同化阿拉伯糖进行木糖还原生产木糖醇的重组酿酒酵母菌株,以实现原料中全糖利用、生产高附加值产品,实现产品多元化。[方法] 首先,利用CRISPR/Cas9基因编辑技术依次向出发菌株中导入阿拉伯糖代谢途径和木糖还原酶基因,使菌株获得代谢阿拉伯糖和将木糖转化为木糖醇的能力;其次,通过适应性驯化的进化工程手段,提高重组菌株对阿拉伯糖的利用效率;最后,通过混合糖发酵验证重组菌株利用阿拉伯糖和还原木糖产木糖醇的能力。[结果] 通过导入植物乳杆菌的阿拉伯糖代谢途径,酿酒酵母菌株获得了较好的利用阿拉伯糖生长繁殖的能力;进一步导入假丝酵母的木糖还原酶基因后,重组菌株在葡萄糖作为辅助碳源条件下可高效还原木糖产木糖醇,但阿拉伯糖的利用能力下降。利用以阿拉伯糖为唯一碳源的培养基进行反复批次驯化,阿拉伯糖的利用能力得以恢复和提升,得到表型较好的重组菌株KAX3-2。该菌株在木糖（50 g/L）和阿拉伯糖（20 g/L）混合糖发酵条件下发酵72 h时,对阿拉伯糖和木糖利用率分别达到42.1%和65.9%,木糖醇的收率为64%。[结论] 本研究成功构建了一株能有效利用阿拉伯糖并能将木糖转化为木糖醇的重组酿酒酵母菌株KAX3-2,为后续构建、获得阿拉伯糖代谢能力更强、木糖醇积累效率更高菌株的工作奠定了基础。     

Reduction of xylose to xylitol catalyzed by glucose–fructose oxidoreductase from Zymomonas mobilis

Genetic improvements of Zymomonas mobilis for pentose utilization have a huge potential in fuel ethanol production. The production of xylitol and the resulting growth inhibition by xylitol phosphate have been considered to be one of the important factors affecting the rates and yields from xylose metabolism by the recombinant Z. mobilis , but the mechanism of xylitol formation is largely unknown. Here, we reported that glucose–fructose oxidoreductase (GFOR), a periplasmic enzyme responsible for sorbitol production, catalyzed the reduction of xylose to xylitol in vitro , operating via a ping-pong mechanism similar to that in the formation of sorbitol. However, the specific activity of GFOR for sorbitol was higher than that for xylitol (68.39 vs. 1.102 μmol min⁻¹ mg⁻¹), and an apparent substrate-induced positive cooperativity occurred during the catalyzed formation of xylitol, with the Hill coefficient being about 2. While a change of the potential acid–base catalyst Tyr269 to Phe almost completely abolished the activity toward xylose as well as fructose, mutant S116D, which has been shown to lose tight cofactor binding, displayed an even slower catalytic process against xylose.     

Computational design of Candida boidinii xylose reductase for altered cofactor specificity

In this study we introduce a computationally‐driven enzyme redesign workflow for altering cofactor specificity from NADPH to NADH. By compiling and comparing data from previous studies involving cofactor switching mutations, we show that their effect cannot be explained as straightforward changes in volume, hydrophobicity, charge, or BLOSUM62 scores of the residues populating the cofactor binding site. Instead, we find that the use of a detailed cofactor binding energy approximation is needed to adequately capture the relative affinity towards different cofactors. The implicit solvation models Generalized Born with molecular volume integration and Generalized Born with simple switching were integrated in the iterative protein redesign and optimization (IPRO) framework to drive the redesign of Candida boidinii xylose reductase (CbXR) to function using the non‐native cofactor NADH. We identified 10 variants, out of the 8,000 possible combinations of mutations, that improve the computationally assessed binding affinity for NADH by introducing mutations in the CbXR binding pocket. Experimental testing revealed that seven out of ten possessed significant xylose reductase activity utilizing NADH, with the best experimental design (CbXR‐GGD) being 27‐fold more active on NADH. The NADPH‐dependent activity for eight out of ten predicted designs was either completely abolished or significantly diminished by at least 90%, yielding a greater than 10⁴‐fold change in specificity to NADH (CbXR‐REG). The remaining two variants (CbXR‐RTT and CBXR‐EQR) had dual cofactor specificity for both nicotinamide cofactors.     

Purification and characterisation of NAD+-dependent xylitol dehydrogenase from Fusarium oxysporum

An NAD⁺-dependent xylitol dehydrogenase (XDH) from Fusarium oxysporum, a key enzyme in the conversion of xylose to ethanol, was purified to homogeneity and characterised. It was homodimeric with a subunit of M _r 48 000, and pI 3.6. It was optimally active at 45 °C and pH 9–10. It was fully stable at pH 6–7 for 24 h and 30 °C. K _m values for d-xylitol and NAD⁺ were 94 mM and 0.14 mM, respectively. Mn²⁺ at 10 mM increased XDH activity 2-fold and Cu²⁺ at 10 mM inhibited activity completely.     

Influence of temperature and pH on xylitol production from xylose by Debaryomyces hansenii

The production of xylitol from concentrated synthetic xylose solutions (S(o) = 130-135 g/L) by Debaryomyces hansenii was investigated at different pH and temperature values. At optimum starting pH (pH(o) = 5.5), T = 24 degrees C, and relatively low starting biomass levels (0.5-0.6 g(x)/L), 88% of xylose was utilized for xylitol production, the rest being preferentially fermented to ethanol (10%). Under these conditions, nearly 70% of initial carbon was recovered as xylitol, corresponding to final xylitol concentration of 91.9 g(P)/L, product yield on substrate of 0.81 g(P)/g(S), and maximum volumetric and specific productivities of 1.86 g(P)/L x h and 1.43 g(P)/g(x) x h, respectively. At higher and lower pH(o) values, respiration also became important, consuming up to 32% of xylose, while negligible amounts were utilized for cell growth (0.8-1.8%). The same approach extended to the effect of temperature on the metabolism of this yeast at pH(o) = 5.5 and higher biomass levels (1.4-3.0 g(x)/L) revealed that, at temperatures ranging from 32-37 degrees C, xylose was nearly completely consumed to produce xylitol, reaching a maximum volumetric productivity of 4.67 g(P)/L x h at 35 degrees C. Similarly, both respiration and ethanol fermentation became significant either at higher or at lower temperatures. Finally, to elucidate the kinetic mechanisms of both xylitol production and thermal inactivation of the system, the related thermodynamic parameters were estimated from the experimental data with the Arrhenius model: activation enthalpy and entropy were 57.7 kJ/mol and -0.152 kJ/mol x K for xylitol production and 187.3 kJ/mol and 0.054 kJ/mol x K for thermal inactivation, respectively.     

Xylitol production by <Emphasis Type="Italic">Candida tropicalis</Emphasis> in a chemically defined medium

A chemically defined medium that included urea (5 g l(-1)) as a nitrogen source and various vitamins was substituted for a complex medium containing yeast extract (10 g l(-1)) in the production of xylitol by Candida tropicalis. In a fed-batch culture with the chemically defined medium, 237 g xylitol l(-1) was produced from 270 g xylose l(-1) after 120 h. The volumetric rate of xylitol production and the xylitol yield from xylose were 2 g l(-1) h(-1) and 89%, respectively. These values were about 5% lower and 4% higher, respectively, than those obtained using the complex medium. These results indicate that xylitol can be produced effectively in a chemically defined medium.