Cloning,expression and characterization of xylose isomerase from the marine bacterium Fulvimarina pelagi in Escherichia coli

Production of a xylose isomerase (XI) with high tolerance to the inhibitors xylitol and calcium, and high activity at the low pH and temperature conditions characteristic of yeast fermentations, is desirable for a simultaneous isomerization/fermentation process for cellulosic ethanol production. A putative XI gene (xylA) from the marine bacterium Fulvimarina pelagi was identified by sequence analysis of the F. pelagi genome, and was PCR amplified, cloned, and expressed in Escherichia coli. The rXI was produced in shake flask and fed‐batch fermentations using glucose as the growth substrate. The optimum pH for rXI was approximately 7, although activity was evident at pH as low as 5.5. The purified rXI had a molecular weight in 160 kDA, a V_max of 0.142 U/mg purified rXI, and a K_M for xylose in the range of 1.75–4.17 mM/L at pH 6.5 and a temperature of 35°C. The estimated calcium and xylitol K_I values for rXI in cell‐free extracts were 2,500 mg/L and >50 mM, respectively. The low K_M of the F. pelagi xylose isomerase is consistent with the low nutrient conditions of the pelagic environment. These results indicate that Ca²⁺ and xylitol are not likely to be inhibitory in applications employing the rXI from F. pelagi to convert xylose to xylulose in fermentations of complex biomass hydrolysates. A higher V_max at low pH (<6) and temperature (30°C) would be preferable for use in biofuels production. © 2016 American Institute of Chemical Engineers Biotechnol. Prog., 32:1230–1237, 2016     

Effects of borate on isomerization and yeast fermentation of high xylulose solution and acid hydrolysate of hemicellulose

d-Xylose has been isomerized by immobilized d-glucose isomerase (EC nomenclature is now d-xylose isomerase, d-xylose ketol-isomerase, EC 5.3.1.5; EC 5.3.1.18 is a deleted EC entry). Temperature has a profound influence on the equilibrium concentration of d-xylulose. When 1 md-xylose was isomerized in the presence of various concentrations of borate, maximum conversion (80%) was observed at 0.2 m sodium tetraborate. Temperature (40–69°C) and pH (6.0–7.5) had an insignificant effect on the equilibrium when borate was present. d-Xylose (0.5 m) was isomerized by d-glucose isomerase in the presence of various concentrations of sodium tetraborate (0.0125–0.25 m). Based on the initial rate of ethanol production and the fraction of total sugar converted into ethanol after 24 h of yeast fermentation, an optimum tetraborate concentration of 0.05 m was determined for both isomerization and fermentation. At an acidic pH, the rate of fermentation was faster than at neutral pH when borate was included in the d-xylose—d-xylulose system. Acid hydrolysate of bagasse hemicellulose could not be fermented at a pH lower than 5. Therefore, a compromise condition, pH 6.0, was chosen for fermentation.     

木糖异构酶在酿酒酵母细胞表面的展示

将来源于嗜热细菌Thermus thermophilus的木糖异构酶基因xylA,与酿酒酵母(Sac-charomyces cerevisiae)a-凝集素表面展示载体pYD1的Aga2p亚基C端序列融合。编码融合蛋白的基因序列前接上半乳糖诱导型启动子。用LiAc完整细胞法转化酿酒酵母EBY100。含重组质粒的菌株EBY100/pYD-xylA经半乳糖诱导表达外源融合蛋白,免疫荧光显微镜结果显示外源蛋白被锚定在细胞壁上,木糖异构酶活性测定结果表明,细胞壁上酶活测定值为1.52U,木糖异构酶在酿酒酵母细胞壁上得到活性表达。     

在酿酒酵母中共表达XYLA和XKS1基因后利用木糖的初步研究

为了使酿酒酵母较好地利用木糖产生乙醇,将来自Thermus thermophilus的木糖异构酶基因XYLA和酿酒酵母自身的木酮糖激酶基因XKS1,构建到酵母表达载体pESC-LEU中,导入酿酒酵母YPH499中,同时成功表达了两种酶基因。该菌以木糖为唯一碳源进行限氧发酵,木糖的利用率为9.64%,为宿主菌的4.17倍,产生2.22 mmol.L-1的乙醇。同时初步探讨了两种酶基因的表达量对酿酒酵母发酵木糖生成乙醇的影响。木糖异构酶对木糖的利用起关键性的作用,木酮糖激酶的过量表达不利于乙醇生成。     

Overexpression of bacterial xylose isomerase and yeast host xylulokinase improves xylose alcoholic fermentation in the thermotolerant yeast Hansenula polymorpha

The thermotolerant methylotrophic yeast Hansenula polymorpha is able to ferment xylose to ethanol. To improve characteristics of xylose fermentation, the recombinant strain Delta xyl1 Delta xyl2-ADelta xyl2-B, with deletions of genes encoding first enzymes of xylose utilization (NAD(P)H-dependent xylose reductase and NAD-dependent xylitol dehydrogenases, respectively), was constructed and used as a recipient for co-overexpression of the Escherichia coli xylA gene coding for xylose isomerase and endogenous XYL3 gene coding for xylulokinase. The expression of both genes was driven by the H. polymorpha glyceraldehyde-3-phosphate dehydrogenase promoter. Xylose isomerase activities of obtained transformants amounted to approximately 80% of that of the bacterial host strain. Xylulokinase activities of the transformants increased twofold when compared with the parental strain. The recombinant strains displayed improved ethanol production during the fermentation of xylose.     

Identification and functional expression of a new xylose isomerase from the goat rumen microbiome in Saccharomyces cerevisiae

The current climate crisis demands replacement of fossil energy sources with sustainable alternatives. In this scenario, second-generation bioethanol, a product of lignocellulosic biomass fermentation, represents a more sustainable alternative. However, Saccharomyces cerevisiae cannot metabolize pentoses, such as xylose, present as a major component of lignocellulosic biomass. Xylose isomerase (XI) is an enzyme that allows xylose consumption by yeasts, because it converts xylose into xylulose, which is further converted to ethanol by the pentose-phosphate pathway. Only a few XI were successfully expressed in S. cerevisiae strains. This work presents a new bacterial XI, named GR-XI 1, obtained from a Brazilian goat rumen metagenomic library. Phylogenetic analysis confirmed the bacterial origin of the gene, which is related to Firmicutes XIs. After codon optimization, this enzyme, renamed XySC1, was functionally expressed in S. cerevisiae, allowing growth in media with xylose as sole carbon source. Overexpression of XySC1 in S. cerevisiae allowed the recombinant strain to efficiently consume and metabolize xylose under aerobic conditions.     

Crystal structure of Streptomyces diastaticus No. 7 strain M1033 xylose isomerase

The crystal structures of Streptomyces diastaticus No. 7 strain M1033 xylose isomerase (SDXyI) have been analysed and refined at 0.19nm. The crystal space group is I222, with unit cell dimensions of a=9.884 ran, b=9.393nm and c=8.798nm. Based on the coordinates of the Streptomyces rubiginosus xylose isomerase (SRXyI), the initial model of SDXyl was built up by the dose packing analysing and R-factor searching and refined by PROLSQ to a final R-factor of 0.177 with the rms deviations of bond lengths and bond angles of 0.001 9nm and 2.1°, respectively. No significant global conformation change existed between SRXyI and SDXyI except the local conformation in the active site.     

Purification and characterization of thermostable xylose(glucose) isomerase from Bacillus thermoantarcticus

Xylose isomerase produced by Bacillus thermoantarcticus was purified 73-fold to homogeneity and its biochemical properties were determined. It was a homotetramer with a native molecular mass of 200 kDa and a subunit molecular mass of 47 kDa, with an isoelectric point at 4.8. The enzyme had a K _m of 33 mM for xylose and also accepted D-glucose as substrate. Arrhenius plots of the enzyme activity of xylose isomerase were linear up to a temperature of 85°C. Its optimum pH was around 7.0, and it had 80% of its maximum activity at pH 6.0. This enzyme required divalent cations for its activity and thermal stability. Mn²⁺, Co²⁺ or Mg²⁺ were of comparable efficiency for xylose isomerase reaction, while Mg²⁺ was necessary for glucose isomerase reaction. Journal of Industrial Microbiology & Biotechnology (2001) 27, 234–240. Received 18 March 2001/ Accepted in revised form 03 July 2001     

Display of Clostridium cellulovorans xylose isomerase on the cell surface of Saccharomyces cerevisiae and its direct application to xylose fermentation

Xylose isomerase (XI) is a key enzyme in the conversion of d ‐xylose, which is a major component of lignocellulosic biomass, to d ‐xylulose. Genomic analysis of the bacterium Clostridium cellulovorans revealed the presence of XI‐related genes. In this study, XI derived from C. cellulovorans was produced and displayed using the yeast cell‐surface display system, and the xylose assimilation and fermentation properties of this XI‐displaying yeast were examined. XI‐displaying yeast grew well in medium containing xylose as the sole carbon source and directly produced ethanol from xylose under anaerobic conditions. © 2013 American Institute of Chemical Engineers Biotechnol. Prog., 29: 346–351, 2013     

Effects of acetic acid on the kinetics of xylose fermentation by an engineered, xylose-isomerase-based Saccharomyces cerevisiae strain

Acetic acid, an inhibitor released during hydrolysis of lignocellulosic feedstocks, has previously been shown to negatively affect the kinetics and stoichiometry of sugar fermentation by (engineered) Saccharomyces cerevisiae strains. This study investigates the effects of acetic acid on S. cerevisiae RWB 218, an engineered xylose-fermenting strain based on the Piromyces XylA (xylose isomerase) gene. Anaerobic batch cultures on synthetic medium supplemented with glucose–xylose mixtures were grown at pH 5 and 3.5, with and without addition of 3 g L⁻¹ acetic acid. In these cultures, consumption of the sugar mixtures followed a diauxic pattern. At pH 5, acetic acid addition caused increased glucose consumption rates, whereas specific xylose consumption rates were not significantly affected. In contrast, at pH 3.5 acetic acid had a strong and specific negative impact on xylose consumption rates, which, after glucose depletion, slowed down dramatically, leaving 50% of the xylose unused after 48 h of fermentation. Xylitol production was absent (<0.10 g L⁻¹) in all cultures. Xylose fermentation in acetic –acid-stressed cultures at pH 3.5 could be restored by applying a continuous, limiting glucose feed, consistent with a key role of ATP regeneration in acetic acid tolerance.     

木糖异构酶序列结构特点、耐热机理及分子改造研究进展

近年来,随着发展低碳经济的迫切需要,可再生资源利用研究方兴未艾,其中,构建充分利用木质纤维素水解产物木糖生产乙醇的重组菌成为研究热点.木糖异构酶由于不需要辅酶,成为构建利用木糖重组酵母的首选途径.文中对近年来木糖异构酶的研究进展进行了综述.首先介绍了木糖异构酶的基本性质、序列、结构和功能特性,然后对其耐热机理进行了总结归纳;重点阐述了基于序列及结构进行的酶分子改造研究,包括底物特异性改造、热稳定性改造等;同时,结合作者的研究经历,对如何提高嗜热木糖异构酶在常温下的活性进行了探讨.最后,对木糖异构酶的研究进展进行了总结和展望,对基于结构改善木糖异构酶催化活性及构建新型高效利用木糖生产乙醇的重组菌具有重要的指导意义.     

Characterization of enzymatic D-xylulose 5-phosphate synthesis

In this article we report on the characterization of the enzymatic synthesis of D-xylulose 5-phosphate using triosephosphate isomerase and transketolase. Two potential starting substrates are possible with this scheme. The data presented here allow a comparison of both routes for the synthesis, based on experimental information on reaction kinetics. Operational guidelines are proposed which should assist in the scale-up of such syntheses.     

Application of a compatible xylose isomerase in simultaneous bioconversion of glucose and xylose to ethanol

Simultaneous isomerisation and fermentation (SIF) of xylose and simultaneous isomerisation and cofermentation (SICF) of glucose-xylose mixture was carried out by the yeastSaccharomyces cerevisiae in the presence of a compatible xylose isomerase. The enzyme converted xylose to xylulose andS. cerevisiae fermented xylulose, along with glucose, to ethanol at pH 5.0 and 30°C. This compatible xylose isomerase fromCandida boidinii, having an optimum pH and temperature range of 4.5–5.0 and 30–50°C respectively, was partially purified and immobilized on an inexpensive, inert and easily available support, hen egg shell. An immobilized xylose isomerase loading of 4.5 IU/(g initial xylose) was optimum for SIF of xylose as well as SICF of glucose-xylose mixture to ethanol byS. cerevisiae. The SICF of 30 g/L glucose and 70 g xylose/L gave an ethanol concentration of 22.3 g/L with yield of 0.36 g/(g sugar consumed) and xylose conversion efficiency of 42.8%.     

Glucose-to-fructose conversion at high temperatures with xylose (glucose) isomerases from Streptomyces murinus and two hyperthermophilic Thermotoga species

The conversion of glucose to fructose at elevated temperatures, as catalyzed by soluble and immobilized xylose (glucose) isomerases from the hyperthermophiles Thermotoga maritima (TMGI) and Thermotoga neapolitana 5068 (TNGI) and from the mesophile Streptomyces murinus (SMGI), was examined. At pH 7.0 in the presence of Mg(2+), the temperature optima for the three soluble enzymes were 85 degrees C (SMGI), 95 degrees to 100 degrees C (TNGI), and >100 degrees C (TMGI). Under certain conditions, soluble forms of the three enzymes exhibited an unusual, multiphasic inactivation behavior in which the decay rate slowed considerably after an initial rapid decline. However, the inactivation of the enzymes covalently immobilized to glass beads, monophasic in most cases, was characterized by a first-order decay rate intermediate between those of the initial rapid and slower phases for the soluble enzymes. Enzyme productivities for the three immobilized GIs were determined experimentally in the presence of Mg(2+). The highest productivities measured were 750 and 760 kg fructose per kilogram SMGI at 60 degrees C and 70 degrees C, respectively. The highest productivity for both TMGI and TNGI in the presence of Mg(2+) occurred at 70 degrees C, pH 7.0, with approximately 230 and 200 kg fructose per kilogram enzyme for TNGI and TMGI, respectively. At 80 degrees C and in the presence of Mg(2+), productivities for the three enzymes ranged from 31 to 273. A simple mathematical model, which accounted for thermal effects on kinetics, glucose-fructose equilibrium, and enzyme inactivation, was used to examine the potential for high-fructose corn syrup (HFCS) production at 80 degrees C and above using TNGI and SMGI under optimal conditions, which included the presence of both Co(2+) and Mg(2+). In the presence of both cations, these enzymes showed the potential to catalyze glucose-to-fructose conversion at 80 degrees C with estimated lifetime productivities on the order of 2000 kg fructose per kilogram enzyme, a value competitive with enzymes currently used at 55 degrees to 65 degrees C, but with the additional advantage of higher fructose concentrations. At 90 degrees C, the estimated productivity for SMGI dropped to 200, whereas, for TNGI, lifetime productivities on the order of 1000 were estimated. Assuming that the most favorable biocatalytic and thermostability features of these enzymes can be captured in immobilized form and the chemical lability of substrates and products can be minimized, HFCS production at high temperatures could be used to achieve higher fructose concentrations as well as create alternative processing strategies.     

Enhanced direct ethanol production by cofactor optimization of cell surface‐displayed xylose isomerase in yeast

Xylose isomerase (XylC) from Clostridium cellulovorans can simultaneously perform isomerization and fermentation of d ‐xylose, the main component of lignocellulosic biomass, and is an attractive candidate enzyme. In this study, we optimized a specified metal cation in a previously established Saccharomyces cerevisiae strain displaying XylC. We investigated the effect of each metal cation on the catalytic function of the XylC‐displaying S. cerevisiae. Results showed that the divalent cobalt cations (Co²⁺) especially enhanced the activity by 46‐fold. Co²⁺ also contributed to d ‐xylose fermentation, which resulted in improving ethanol yields and xylose consumption rates by 6.0‐ and 2.7‐fold, respectively. Utility of the extracellular xylose isomerization system was exhibited in the presence of mixed sugar. XylC‐displaying yeast showed the faster d ‐xylose uptake than the yeast producing XI intracellularly. Furthermore, direct xylan saccharification and fermentation was performed by unique yeast co‐culture system. A xylan‐degrading yeast strain was established by displaying two kinds of xylanases; endo‐1,4‐β‐xylanase (Xyn11B) from Saccharophagus degradans, and β‐xylosidase (XlnD) from Aspergillus niger. The yeast co‐culture system enabled fine‐tuning of the initial ratios of the displayed enzymes (Xyn11B:XlnD:XylC) by adjusting the inoculation ratios of Xylanases (Xyn11B and XlnD)‐displaying yeast and XylC‐displaying yeast. When the enzymes were inoculated at the ratio of 1:1:2 (1.39 × 10¹³: 1.39 × 10¹³: 2.78 × 10¹³ molecules), 6.0 g/L ethanol was produced from xylan. Thus, the cofactor optimization and the yeast co‐culture system developed in this study could expand the prospect of biofuels production from lignocellulosic biomass. © 2017 American Institute of Chemical Engineers Biotechnol. Prog., 33:1068–1076, 2017     

Control of xylose consumption by xylose transport in recombinant Saccharomyces cerevisiae

Saccharomyces cerevisiae TMB3001 has previously been engineered to utilize xylose by integrating the genes coding for xylose reductase (XR) and xylitol dehydrogenase (XDH) and overexpressing the native xylulokinase (XK) gene. The resulting strain is able to metabolize xylose, but its xylose utilization rate is low compared to that of natural xylose utilizing yeasts, like Pichia stipitis or Candida shehatae. One difference between S. cerevisiae and the latter species is that these possess specific xylose transporters, while S. cerevisiae takes up xylose via the high-affinity hexose transporters. For this reason, in part, it has been suggested that xylose transport in S. cerevisiae may limit the xylose utilization.We investigated the control exercised by the transport over the specific xylose utilization rate in two recombinant S. cerevisiae strains, one with low XR activity, TMB3001, and one with high XR activity, TMB3260. The strains were grown in aerobic sugar-limited chemostat and the specific xylose uptake rate was modulated by changing the xylose concentration in the feed, which allowed determination of the flux response coefficients. Separate measurements of xylose transport kinetics allowed determination of the elasticity coefficients of transport with respect to extracellular xylose concentration. The flux control coefficient, C(J) (transp), for the xylose transport was calculated from the response and elasticity coefficients. The value of C(J) (transp) for both strains was found to be < 0.1 at extracellular xylose concentrations > 7.5 g L(-1). However, for strain TMB3260 the flux control coefficient was higher than 0.5 at xylose concentrations < 0.6 g L(-1), while C(J) (transp) stayed below 0.2 for strain TMB3001 irrespective of xylose concentration.     

Kinetic modeling of Candida shehatae ATCC 22984 on xylose and glucose for ethanol production

Candida shehatae ATCC 22984, a xylose-fermenting yeast, showed an ability to produce ethanol in both glucose and xylose medium. Maximum ethanol produced by the yeast was 48.8?g/L in xylose and 52.6?g/L in glucose medium with ethanol yields that varied between 0.3 and 0.4?g/g depended on initial sugar concentrations. Xylitol was a coproduct of ethanol production using xylose as substrate, and glycerol was detected in both glucose and xylose media. Kinetic model equations indicated that growth, substrate consumption, and product formation of C. shehatae were governed by substrate limitation and inhibition by ethanol. The model suggested that cell growth was totally inhibited at 40?g/L of ethanol and ethanol production capacity of the yeast was 52?g/L, which were in good agreement with experimental results. The developed model could be used to explain C. shehatae fermentation in glucose and xylose media from 20 to 170?g/L sugar concentrations.     

HPLC determination of xylulose formed by enzymatic xylose isomerization in lignocellulose hydrolysates

Summary In the concentration range appropriate for enzymatic xylose isomerization, xylulose was measured in a lignocellulose hydrolysate using HPLC with two hydrogen loaded ion exchange columns in series. Spent sulphite liquour (SSL) was used as a model for lignocellulose hydrolysates. In buffer the separation took 22 minutes and in SSL the analysis time was 47 minutes due to the presence of ethanol. The enzymatic isomerization of xylose to xylulose was followed directly in SSL, providing a method for the direct determination of xylose isomerase activity in lignocellulose hydrolysates.     

The xylose isomerase gene from Thermoanaerobacterium thermosulfurogenes allows effective selection of transgenic plant cells using D-xylose as the selection agent

The xylose isomerase gene (xylA) from Thermoanaerobacterium thermosulfurogenes (formerly Clostridium thermosulfurogenes) has been expressed in three plant species (potato, tobacco, and tomato) and transgenic plants have been selected on xylose-containing medium. The xylose isomerase gene was transferred to the target plant by Agrobacterium-mediated transformation. The xylose isomerase gene was expressed using the enhanced cauliflower mosaic virus (CaMV) 35S promoter and the translation enhancer sequence from tobacco mosaic virus. Unoptimized selection studies showed that, in potato and tomato, the xylose isomerase selection was more efficient than the established kanamycin resistance selection, whereas in tobacco the opposite was observed. Efficiency may be increased by optimization. The xylose isomerase system enables the transgenic cells to utilize xylose as a carbohydrate source. It is an example of a positive selection system because transgenic cells proliferate while non-transgenic cells are starved but still survive. This contrasts to antibiotic or herbicide resistance where transgenic cells survive on a selective medium but non-transgenic cells are killed. The results give access to a new selection method which is devoid of the disadvantages of antibiotic or herbicide selection.     

地芽孢杆菌Y565-5分离鉴定及其木糖异构酶基因xylA的克隆表达和酶学性质

从甘肃玉门油田地表土中分离到一株嗜热木糖利用菌,地芽孢杆菌Y565-5。利用PCR方法从该菌株中克隆得到一个木糖异构酶基因,xylA。该基因开放阅读框长1182 bp,编码394个氨基酸,XylA氨基酸序列与Geobacillus sp.Y412MC52相似性达到99%。将xylA基因克隆到原核表达载体pET-28a(+)上,得到重组质粒pET-28a(+)-xylA,然后将此重组质粒转化至BL21(DE3)中,经IPTG诱导后,通过SDS-PAGE电泳检测出明显的45 kD(相对分子质量)特异性蛋白质条带,并且通过半胱氨酸咔唑法检测出表达产物具有木糖异构酶的活性。对其酶学性质的研究发现,XylA最适温度为90°C,最适pH值为8.0。