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。     

酵母发酵蔗渣半纤维素水解物生产木糖醇

采用二次正交旋转组合设计研究了蔗渣半纤维素水解过程中硫酸浓度与液/固比对木糖收率的影响。回归分析表明,这两个因素与木糖的收率之间存在显著的回归关系。通过回归方程优化水解条件,当硫酸浓度2.4g/L,液/固=6.2,在蒸汽压力2.5×10⁴ Pa的条件下水解2.5h,100g蔗渣可水解生成木糖约24g 。大孔树脂吸附层析处理蔗渣半纤维素水解物,能有效地减少其中的酵母生长抑制物含量,显著改善水解物的发酵性能。用大孔树脂在pH 2条件下处理过的蔗渣半纤维素水解物作基质,含木糖200g/L,产木糖醇酵母菌株Candida tropicalis AS2.1776发酵110h耗完基质中的木糖,生成木糖醇127g/L,产物转化率0.64（木糖醇g/木糖g）,产物生成速率1.15g/L·h.       

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。     

热带假丝酵母XYL1在Pichia pastoris中的表达及固定化细胞发酵生产木糖醇

利用克隆获得的具有双重辅酶依赖性的热带假丝酵母xyl1基因,通过表达载体pGAPZB转入巴斯德毕赤酵母X-33,采用海藻酸钙凝胶包埋法固定该重组菌,研究固定化条件下玉米芯水解液的发酵特性,实现对玉米芯等农业废弃物资源的利用。结果表明,转化xyl1基因的巴斯德毕赤酵母X-33的总酶活达到1.64U/mg。固定化细胞的最适发酵条件为pH 6.0、30℃、接种量20%、装液量28%、转速130r/min,木糖醇转化率为37.5%。为生物转化法大规模生产木糖醇以及乙醇提供新的选择途径。     

聚氨酯泡沫固定产脂肪酶粗状假丝酵母（Candidav alida T2）细胞的研究

对聚氨酯泡沫固定产脂肪酶粗状假丝酵母（Candida validaT2）细胞的固定化条件进行了研究。实验结果表明,聚氨酯泡沫颗粒经密度和粒径筛选,酸碱处理,以及固液比优化,载体固定细胞干质量比达到157lmg／g,细胞脂肪酶的酶活为每克干细胞1415U。电镜图片显示粗状假丝酵母菌（Candida validaT2）在载体孔隙内和脊壁上缠绕充盈,生长良好,固定结构稳定。固定化细胞连续催化水解桐籽油5批次,细胞相对水解酶活保持率达73％,固定细胞的损失率为12．5％。固定化细胞颗粒显示出良好的操作稳定性和酶活保持率,为进一步的应用研究提供了实验基础。     

聚氨酯泡沫固定产脂肪酶粗状假丝酵母(Candida valida T2)细胞的研究

对聚氨酯泡沫固定产脂肪酶粗状假丝酵母(Candida valida T2)细胞的固定化条件进行了研究.实验结果表明,聚氨酯泡沫颗粒经密度和粒径筛选,酸碱处理,以及固液比优化,载体固定细胞干质量比达到1571 mg/g,细胞脂肪酶的酶活为每克干细胞1415 U.电镜图片显示粗状假丝酵母菌(Candida valida T2)在载体孔隙内和脊壁上缠绕充盈,生长良好,固定结构稳定.固定化细胞连续催化水解桐籽油5批次,细胞相对水解酶活保持率达73%,固定细胞的损失率为12.5%.固定化细胞颗粒显示出良好的操作稳定性和酶活保持率,为进一步的应用研究提供了实验基础.     

半纤维素水解物生物转化生产木糖醇

木糖醇在食品、医药及化工行业中有着广泛的用途而深受关注。但是,传统的化学法生产木糖醇需要一系列复杂的分离纯化步骤,过高的生产成本限制了木糖醇的使用范围。发酵工艺生产木糖醇无需木糖的纯化步骤,是取代化学合成法的一条可行工艺路线。本文着重介绍产木糖醇的微生物,酵母对木糖的同化途径,半纤维素水解物的脱毒方法,影响木糖醇发酵的工艺条件等。     

利用蔗渣半纤维素水解液产油酵母的筛选、鉴定及发酵实验

对已分离到的产油酵母通过木糖摇瓶发酵,从中筛选到2株H2-1和J2-2利用蔗渣半纤维素水解液高产油脂酵母,其利用蔗渣半纤维素水解液油脂得率系数分别为13.49和10.28,均显示出对蔗渣半纤维素水解液的高转化率.根据常规生理生化特征和26S rDNA序列分析结果,确认H2-1为小红酵母(Rhodotorula minuta),J2-2为粘红酵母(Rhodotorula glutinis).     

D301树脂固定化假丝酵母脂肪酶

本研究选择7种吸附和离子交换树脂进行了假丝酵母脂肪酶(Candida sp.lipase)的固定化试验,通过测定固定化后各脂肪酶的酶活,筛选出固定化效果较好的弱碱性阴离子交换树脂D301;并通过扫描电镜将D301与脂肪酶Novozym 435的表面形貌做比较,进一步选定D301树脂作为载体,并对其采用戊二醛交联固定化,研究并优化了其固定化条件。结果表明,5%戊二醛溶液的加入量为8mL,处理时间为5h,酶液浓度为1.0g/L,磷酸缓冲盐溶液pH6.0,固定化处理10h效果最好,获得的固定化酶活力可达35U/mg,酶的固定化效率约为3.5U/(mg·h)。     

Biotin and Zn2+ Increase Xylitol Production by Candida tropicalis

In this study, the medium requirements to increase the production of xylitol by using Candida tropicalis (CT) have been investigated. The technique of single addition or omission of medium components was applied to determine the nutritional requirements. The addition of amino acids such as Asp, Glu, Gln, Asn, Thr, and Gly had no significant effect on CT growth. However, in the absence of other metal ions, there was a higher concentration of cell growth and xylitol production when only Zn²⁺ was present in the medium. The analysis of various vitamins unveiled that biotin and thiamine were the only vitamins required for the growth of CT. Surprisingly, when only biotin was present in the medium as a vitamin, there was less growth of CT than when the medium was complete, but the amount of xylitol released was significantly higher. Overall, this study will increase the xylitol production using the single omission or addtion technique.     

Xylitol production by <Emphasis Type="Italic">Debaryomyces hansenii</Emphasis> in brewery spent grain dilute-acid hydrolysate: effect of supplementation

A brewery spent-grain hemicellulosic hydrolysate was used for xylitol production by Debaryomyces hansenii. Addition of 6 g yeast extract/l increased the xylitol yield to 0.57 g/g, and productivity to 0.51 g/l h that were, respectively, 1.4 -and 1.8-times higher than the values obtained with non-supplemented hydrolysate. When corn steep liquor was combined with 3 g yeast extract/l, the highest xylitol yield, 0.58 g/g, was obtained with a similar productivity.     

Xylitol production from non-detoxified corncob hemicellulose acid hydrolysate by Candida tropicalis

The interest on use of lignocellulose for producing chemicals is increasing as these feedstocks are low cost, renewable and widespread sources of sugars. Corncob is an attractive raw material for xylitol production due to its high content of xylan. In this study, hemicellulose hydrolysate from corncobs without detoxification was used for xylitol production by Candida tropicalis CCTCC M2012462. Compared with prepared xylose medium, xylitol production with dilute acid hydrolysate medium does not seem to influence specific xylose reductase activity. The decrease in xylitol productivity with dilute acid hydrolysate medium is a result of a lower biomass concentration and lag-phase time. It appears that biomass growth rate is essential for xylitol production. In xylitol fermentation with a low initial inhibitors concentration and substrate feeding strategy, a maximal xylitol concentration of 38.8 g l⁻¹ was obtained after 84 h of fermentation, giving a yield of 0.7 g g⁻¹ xylose and a productivity of 0.46 g l⁻¹ h⁻¹.     

木糖醇微生物转化的研究

一、引言 木糖醇是一种被广泛用于国防、医药、食品和化学等工业的五碳糖醇。木糖醇也是一种具有营养价值的甜味剂,由于它的代谢不需胰岛素,可作为糖尿病人的食糖代用品。另外木糖醇还可以作为防龋食品。目前国内外生产木糖醇的方法是化学法,即由农业纤维废料如玉米芯和甘蔗渣等经酸水解和提     

Xylitol production from a mutant strain of Candida tropicalis

Aims: To characterize the kinetics of growth, sugar uptake and xylitol production in batch and fed‐batch cultures for a xylitol assimilation‐deficient strain of Candida tropicalis isolated via chemical mutagenesis. Methods and Results: Chemical mutagenesis using nitrosoguanidine led to the isolation of the xylitol‐assimilation deficient strain C. tropicalis SS2. Shake‐flask fermentations with this mutant showed a sixfold higher xylitol yield than the parent strain in medium containing 25 g l^?1 glucose and 25 g l^?1 xylose. With 20 g l^?1 glycerol, replacing glucose for cell growth, and various concentrations of xylose, the studies indicated that the mutant strain resulted in xylitol yields from xylose close to theoretical. Under fully aerobic conditions, fed‐batch fermentation with repeated addition of glycerol and xylose resulted in 3·3 g l^?1 h^?1 xylitol volumetric productivity with the final concentration of 220 g l^?1 and overall yield of 0·93 g g^?1 xylitol. Conclusions: The xylitol assimilation‐deficient mutant isolated in this study showed the potential for high xylitol yield and volumetric productivity under aerobic conditions. In the evaluation of glycerol as an alternative low‐cost nonfermentable carbon source, high biomass and xylitol yields under aerobic conditions were achieved; however, the increase in initial xylose concentrations resulted in a reduction in biomass yield based on glycerol consumption. This may be a consequence of the role of an active transport system in the yeast requiring increasing energy for xylose uptake and possible xylitol secretion, with little or no energy available from xylose metabolism. Significance and Impact of the Study: The study confirms the advantage of using a xylitol assimilation‐deficient yeast under aerobic conditions for xylitol production with glycerol as a primary carbon source. It illustrates the potential of using the xylose stream in a biomass‐based bio‐refinery for the production of xylitol with further cost reductions resulting from using glycerol for yeast growth and energy production.     

The influence of pH and dilution rate on continuous production of xylitol from sugarcane bagasse hemicellulosic hydrolysate by C. guilliermondii

Continuous fermentation of sugarcane bagasse hemicellulosic hydrolysate by the yeast Candida guilliermondii FTI 20037 was used for xylitol production from xylose. Experiments were carried out in a reactor with 1.25 l of treated hydrolysate, at 30 °C and 300 rpm. A 2² full-factorial central composite design was employed for experimental study and analysis of the results. A statistical analysis of the results showed that the effects of the pH and dilution rate (D), the interactions between these variables and the second-order effect of D on the xylitol volumetric productivity (Q_p) were significant at a 95% confidence level. The second-order effect of pH was also significant at a 90% confidence level. The k_La effect on the Q_p was not significant. A volumetric productivity of 0.68 g/l h, representing 95.8% of the predicted value (0.72 g/l h), was obtained.