代谢改造热带假丝酵母发酵木糖母液生产木糖醇

木糖醇是一种在食品、医药、轻工等领域具有广泛用途的多元醇,目前主要通过酸水解木聚糖获得木糖并进一步化学催化加氢方法制备。提取木糖过程中会产生大量的木糖母液副产物,其中含有一定浓度的葡萄糖、木糖、阿拉伯糖等碳源,以及少量的糠醛、四氢呋喃等物质。研究微生物转化木糖母液生产高附加值化学品不仅能够提高木糖母液的利用价值,而且能够减少环境污染。热带假丝酵母不仅能够利用葡萄糖,也具有高效的木糖代谢途径。首先利用代谢工程技术删除了热带假丝酵母菌株的木糖醇脱氢酶基因,获得能够转化木糖积累木糖醇的突变株。在此基础上,评价了突变株在木糖母液培养基中的发酵性能。通过单因素优化实验确定了突变株发酵生产木糖醇较优的发酵工艺:培养基组成为木糖母液300g/L,玉米浆5g/L;最佳发酵条件为:发酵温度35℃,初始p H为5.0,接种量15%,200r/min摇床培养140h。利用优化后的发酵工艺,木糖醇产量达到83.01g/L。初步建立了转化木糖母液生产木糖醇的工艺,为进一步利用木糖母液奠定了基础。     

粗糙脉孢菌（Neurospora crassa）木糖发酵的研究

研究了不同通氧条件和培养基初始pH等对粗糙脉孢菌（Neurospora crassa）AS 3.1602木糖发酵的影响。结果表明,粗糙脉孢菌具有较强的发酵木糖产生乙醇及木糖醇的能力。通气量对木糖发酵有较大的影响。乙醇发酵适合在半好氧条件下进行,此时乙醇的转化率达到63.2%。木糖醇发酵适合在微好氧的条件下进行,转化率达到31.8%。木糖醇是在培养基中乙醇达到一定浓度后才开始积累。培养基的初始pH对木糖发酵产物有较大的影响,乙醇产生最适pH5.0,木糖醇产生最适pH4.0。在培养基pH为碱性条件时,木糖发酵受到很大的抑制。初始木糖浓度对产物乙醇及木糖醇的产率有很大的影响。葡萄糖的存在会抑制木糖的利用,对乙醇和木糖醇的产生也有很大的影响。     

粗糙脉孢菌(Neurospora crassa)木糖发酵的研究

研究了不同通氧条件和培养基初始pH等对粗糙脉孢菌(Neurospora crassa)AS3．1602木糖发酵的影响。结果表明,粗糙脉孢菌具有较强的发酵木糖产生乙醇及木糖醇的能力。通气量对木糖发酵有较大的影响。乙醇发酵适合在半好氧条件下进行,此时乙醇的转化率达到63．2％。木糖醇发酵适合在微好氧的条件下进行,转化率达到31．8％。木糖醇是在培养基中乙醇达到一定浓度后才开始积累。培养基的初始pH对木糖发酵产物有较大的影响,乙醇产生最适pH5．0,木糖醇产生最适pH4．0。在培养基pH为碱性条件时,木糖发酵受到很大的抑制。初始木糖浓度对产物乙醇及木糖醇的产率有很大的影响。葡萄糖的存在会抑制木糖的利用,对乙醇和木糖醇的产生也有很大的影响。     

假丝酵母发酵玉米芯半纤维素水解液生产木糖醇

采用一株驯化过的假丝酵母(Candida sp.)直接发酵经过简单脱毒处理的玉米芯半纤维素水解液生产木糖醇。确定了水解液的最适浓缩倍数在3.0～3.72的范围内。利用正交实验,确定了摇瓶分批发酵工艺条件的最适组合为：摇床转速180r/min,起始C/N为50,起始pH 5.5,接种量5% (体积比)。在此基础上,重点研究了在发酵罐中通气量对酵母发酵玉米芯水解液生产木糖醇的影响。结果表明采用先高后低的分段通气发酵在木糖醇得率方面明显优于恒定通气发酵;其中,在0～24h,3.75 L/min;24～108h,1.25 L/min的分段通气条件下(装液量为2.5L),木糖醇得率(木糖醇/木糖,g/g) 达到0.75 g/g。该结果将有助于建立一种高效的、大规模的利用玉米芯半纤维素水解液发酵生产木糖醇的工艺。     

最新专利文摘

生物转化玉米芯生产木糖醇的工艺方法 本发明提供了一种生物转化玉米芯生产木糖醇的工艺方法,属于功能糖生产技术领域。其工艺方法包括如下步骤：玉米芯的预处理、玉米芯的酶解、液体菌种的制备、木糖醇的发酵生产、发酵液的分离与提纯。采用生物转化玉米芯的工艺生产木糖醇,工序简单、无环境污染,符合环保要求;工艺过程条件温和,常压下操作,易于安全生产;生产收率高,降低了运行成本,提高了产品的市场竞争力,促进了行业的可持续发展。     

克隆木糖还原酶XYL1基因的工程菌YT发酵玉米芯水解液的研究

克隆毕赤氏酵母(Pichia stipitis)木糖还原酶基因XYL1,将其连接到适用于酿酒酵母工业菌株的多拷贝载体pYMIKP中,构建得到表达质粒pYMIKY-XYL1,转化酿酒酵母工业菌株Saccharomyces cerevisiae 6508.利用G418筛选转化子,得到含高拷贝木糖还原酶基因的酿酒酵母重组菌YT,以YT发酵玉米芯工业水解液生产木糖醇,研究其发酵特性和规律,为工业上生物转化法生产木糖醇提供参考.     

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。     

木糖醇大规模发酵生产策略

<正>发酵工艺是木糖醇生产的发展方向,其通过生物选择性催化,大幅度简化了原料预处理步骤和产物分离过程,有效提高从原料到产物的收率。文章对木糖醇大规模发酵生产中的主要技术环节,包括原料选择、水解方法、水解物脱毒与净化、微生物菌种选择、发酵过程与产物分离等问题进行了系统评述,并对这些关键环节的工艺策略选择提出了笔者的观点。     

发酵木糖产生木糖醇的酵母菌的筛选

木糖醇是天然产生的五碳多元醇,作为功能性的甜味剂,其甜度和能量均与蔗糖相当。木糖醇的代谢不需要胰岛素的促进,因而与一般糖类的代谢途径不同。木糖醇是糖尿病患者的理想的糖代用品,并能明显降低转氨酶,有助于治疗糖尿病、护肝和防龋齿的作用。木糖醇的国内外市场十分广阔,目前世界上生产木糖醇的原料主要是木糖,用化学还原或生物转化菌可生产木糖醇,但化学法生产工艺复杂、成本较高,而已对环保液有影响。用微生物发酵法生产木糖醇是发展的必然方向。我们进行了发酵木糖产生木糖醇的酵母菌种的筛选研究。本研究对分离收集到的４…     

食品上的应用

920754用季氏假丝醉母由O一木箱生产木精醉〔英万Meyr-ial,V.…厂Bioteehnol.Lett。一1991,13(4)。一251~256〔译自DBA,1991,10(12),91-06933〕 研究了在微需氧条件下季氏假丝酵母(C“-“dag即玄11哀e,劝。:d公云)NRC557s由木糖生产木糖醇,以及发酵个别的非木糖半纤维素衍生糖的能力。在30“C、搅拌速度15。印m和原始pH6的条件下进行发酵。木糖转化为木糖醇的转化率为。.63g/g,产生的乙醇量可忽略不计。季氏假丝醉母在原始搪浓超过1109/l的D一木糖培养基上培养时可获高转化率和木糖醇产率。由3009/lD一木糖获得的最终木糖醇浓度为221…     

Xylitol production in repeated fed batch cultivation

The ability of Candida parapsilosis to produce xylitol was tested using successive substrate supplies, and the importance of the amount of viable cells in enhancing the conversion rate was demonstrated. The suitability of this yeast for the production of xylitol was investigated in repeated fed-batch cultivation, using pure xylose or mixtures of xylose and glucose. The use of this process increased productivity by about 40% compared with simple batch cultivation without loss of yield of product on substrate. The presence of glucose in the culture medium seemed to stimulate the specific growth rate, but had no influence over other fermentative parameters.     

Integrated production of xylitol and ethanol using corncob

Xylitol production from corncob hemicellulose is a popular process in China. Microbial conversion of xylose to xylitol, as a biological process with many advantages, has drawn increasing attention. As a by-product from the manufacturing of xylitol, corncob cellulosic residues are produced in very large amounts and represent an environmental problem. As a result, considering the large amount of xylitol production in China, the conversion of corncob cellulosic residues has become a widespread issue having to be tackled. After the hemicellulose in corncob has been hydrolyzed for xylitol production, the corncob cellulosic residue is porous and can easily be hydrolyzed by cellulases into glucose and further converted to ethanol, another high-added-value chemical. Based on the latest technology advancements in xylitol, cellulase, and ethanol production, the integrated production of ethanol from corncob cellulosic residues appears as a promising way to improve the profit of the whole xylitol production process.     

Evaluation of cotton stalk hydrolysate for xylitol production

Cotton stalk is a widely distributed and abundant lignocellulosic waste found in Turkey. Because of its rich xylose content, it can be a promising source for the production of xylitol. Xylitol can be produced by chemical or biotechnological methods. Because the biotechnological method is a simple process with great substrate specificity and low energy requirements, it is more of an economic alternative for the xylitol production. This study aimed to use cotton stalk for the production of xylitol with Candida tropicalis Kuen 1022. For this purpose, the combined effects of different oxygen concentration, inoculum level and substrate concentration were investigated to obtain high xylitol yield and volumetric xylitol production rate. Candida tropicalis Kuen 1022 afforded different concentrations of xylitol depending on xylose concentration, inoculum level, and oxygen concentration. The optimum xylose, yeast concentration, and airflow rate for cotton stalk hydrolysate were found as 10.41 g L^?1, 0.99 g L^?1, and 1.02 vvm, respectively, and under these conditions, xylitol yield and volumetric xylitol production rate were obtained as 36% and 0.06 g L^?1 hr^?1, respectively. The results of this study show that cotton stalk can serve as a potential renewable source for the production of xylitol.     

Xylitol bioproduction: state-of-the-art,industrial paradigm shift,and opportunities for integrated biorefineries

Abstract

Recent advances in biomass conversion technologies have shown a promising future toward fermentation during xylitol production. Xylitol is one of the top 12 renewable added-value chemicals that can be obtained from biomass according to US Department of Energy (USDOE). Currently, xylitol accounts for approximately US$823.6 million of annual sales in the market, and this amount is expected to reach US$1.37 billion by 2025. This high demand has been achieved owing to the chemical conversion of hemicellulosic hydrolysates from different lignocellulosic biomasses, which is a costly and non-ecofriendly process. Xylose-rich hemicellulosic hydrolysates are the major raw materials for xylitol production through either chemical or biotechnological routes. Economic production of a clean hemicellulosic hydrolysate is one of the major bottlenecks for xylitol production on the commercial scale. Advancements in biotechnology, such as the isolation of novel microorganisms, genetic manipulation of xylose metabolizing strains, and modifications in the fermentation process, can enhance the economic feasibility of xylitol production on the large scale. Furthermore, xylitol production in integrated biorefineries can be even more economic, given the readily available raw materials and the co-use of steam, electricity, and water, among others. Exploring new biotechnology techniques in integrated biorefineries would open new markets and opportunities for sustainable xylitol production to fulfill the market’s growing demands for this sugar alcohol. This article is a review of the advancements reported in the whole biotechnological process for xylitol production, and involve pretreatment technologies, hemicellulosic hydrolysate preparation, xylose conversion into xylitol, and product recovery. Special attention is devoted to current metabolic engineering strategies to improve this bioprocess, as well as to the importance of xylitol production processes in biorefineries.     

Xylitol production from high xylose concentration: evaluation of the fermentation in bioreactor under different stirring rates

AIMS: To investigate the production of xylitol by the yeast Candida guilliermondii FTI 20037, in a bioreactor, from rice straw hemicellulosic hydrolysate with a high xylose concentration. METHODS AND RESULTS: Batch fermentation was carried out with rice straw hemicellulosic hydrolysate containing about 85 g xylose l(-1), in a stirred-tank bioreactor at 30 degrees C, under aeration of 1.3 vvm (volume of air per volume of medium per min) and different stirring rates (200, 300 and 500 rev min(-1)). The bioconversion of xylose into xylitol by the yeast depended on the stirring rate, the maximum xylitol yield (YP/S = 0.84 g g(-1)) being achieved at 300 rev min-1, with no need to pretreat the hydrolysate for purification. CONCLUSIONS: To determine the most adequate oxygen transfer rate is fundamental to improving the xylose-to-xylitol bioconversion by C. guilliermondii. SIGNIFICANCE AND IMPACT OF THE STUDY: For the microbial production of xylitol to be economically viable, the initial concentration of xylose in the lignocellulosic hydrolysate should be as high as possible, as with high substrate concentrations it is possible to increase the final product concentration. Nevertheless, there are few reports on the use of high xylose concentrations. Considering a process in bioreactor, from rice straw hemicellulosic hydrolysate, this is an innovator work.     

Stoichiometric network constraints on xylose metabolism by recombinant Saccharomyces cerevisiae

Metabolic pathway engineering is constrained by the thermodynamic and stoichiometric feasibility of enzymatic activities of introduced genes. Engineering of xylose metabolism in Saccharomyces cerevisiae has focused on introducing genes for the initial xylose assimilation steps from Pichia stipitis, a xylose-fermenting yeast, into S. cerevisiae, a yeast traditionally used in ethanol production from hexose. However, recombinant S. cerevisiae created in several laboratories have used xylose oxidatively rather than in the fermentative manner that this yeast metabolizes glucose. To understand the differences between glucose and engineered xylose metabolic networks, we performed a flux balance analysis (FBA) and calculated extreme pathways using a stoichiometric model that describes the biochemistry of yeast cell growth. FBA predicted that the ethanol yield from xylose exhibits a maximum under oxygen-limited conditions, and a fermentation experiment confirmed this finding. Fermentation results were largely consistent with in silico phenotypes based on calculated extreme pathways, which displayed several phases of metabolic phenotype with respect to oxygen availability from anaerobic to aerobic conditions. However, in contrast to the model prediction, xylitol production continued even after the optimum aeration level for ethanol production was attained. These results suggest that oxygen (or some other electron accepting system) is required to resolve the redox imbalance caused by cofactor difference between xylose reductase and xylitol dehydrogenase, and that other factors limit glycolytic flux when xylose is the sole carbon source.     

Effect of acetic acid present in bagasse hydrolysate on the activities of xylose reductase and xylitol dehydrogenase in <Emphasis Type="Italic">Candida guilliermondii</Emphasis>

The first two steps in xylose metabolism are catalyzed by NAD(P)H-dependent xylose reductase (XR) (EC 1.1.1.21) and NAD(P)-dependent xylitol dehydrogenase (XDH) (EC 1.1.1.9), which lead to xylosexylitolxylulose conversion. Xylitol has high commercial value, due to its sweetening and anticariogenic properties, as well as several clinical applications. The acid hydrolysis of sugarcane bagasse allows the separation of a xylose-rich hemicellulosic fraction that can be used as a substrate for Candida guilliermondii to produce xylitol. However, the hydrolysate contains acetic acid, an inhibitor of microbial metabolism. In this study, the effect of acetic acid on the activities of XR and XDH and on xylitol formation by C. guilliermondii were studied. For this purpose, fermentations were carried out in bagasse hydrolysate and in synthetic medium. The activities of XR and XDH were higher in the medium containing acetic acid than in control medium. Moreover, none of the fermentative parameters were significantly altered during cell culture. It was concluded that acetic acid does not interfere with xylitol formation since the increase in XR activity is proportional to XDH activity, leading to a greater production of xylitol and its subsequent conversion to xylulose.     

Metabolic engineering strategies for improving xylitol production from hemicellulosic sugars

Xylitol is a five-carbon sugar alcohol with potential for use as a sweetener. Industrially, xylitol is currently produced by chemical hydrogenation of d-xylose using Raney nickel catalysts and this requires expensive separation and purification steps as well as high pressure and temperature that lead to environmental pollution. Highly efficient biotechnological production of xylitol using microorganisms is gaining more attention and has been proposed as an alternative process. Although the biotechnological method has not yet surpassed the advantages of chemical reduction in terms of yield and cost, various strategies offer promise for the biotechnological production of xylitol. In this review, the focus is on the most recent developments of the main metabolic engineering strategies for improving the production of xylitol.     

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.