啤酒废酵母中β-1，3-葡聚糖的提取工艺

研究采用酶-碱法从经超声波处理的废酵母残渣中提取β-1,3-葡聚糖的工艺,通过正交试验得出理想的酶处理工艺条件：酶添加量208U／g,温度50℃、pH6,酶解8h,蛋白质去除率为62．82％,每L废酵母液中可回收0．348g多肽、氨基酸的蛋白水解液;碱处理工艺条件：用30mL质量分数为2％ NaOH溶液在70℃处理酶解后的沉淀物5h。所得β-1,3-葡聚糖纯度为90．50％,得率为11．00％,经紫外光谱、薄层层析和性质分析为高纯度的β-1,3-葡聚糖。     

红酵母COS—5产胡萝卜素条件的研究

研究碳源、氮源和添加剂对红酵母（Rhodotorulasp．）COS－5产胡萝卜素的影响,并通过正交试验优化其产胡萝卜素的培养基组成。结果表明,COS－5产胡萝卜素的适宜培养基：蔗糖50g、蛋白胨5g、酵母膏5g、桔子皮15g、盐酸硫胺素0．002g、定容1L,pH6．0.250mL三角瓶装培养基30mL。在上述条件下28℃振荡培养96h,细胞生物量为27．5mg干重／mL发酵液,胡萝卜素含量达492．7μg／g干重细胞。COS－5胡萝卜素在474．4nm、338．6nm和310．2nm处有     

用连续发酵工艺由味精废液制取单细胞蛋白

用谷氨酸发酵液经一步冷冻等电法提取后的废液生产饲料酵母,经15m3气升式反应器连续发酵试验,其菌体干物质浓度平均为24．88g／L,稀释率0.187h-1,生产干酵母能力为4．65kg／m3·h,发酵单位电耗2．872kW·h／m3,生产成本在1700元,吨(饲料酵母)左右。饲料酵母粗蛋白含量在60％以上,18种氨基酸齐全,氨基酸总量达50％,达到部颁一级饲料酵母的标准。味精废液经酵母菌处理后,COD去除率74．7％。经试验统计,每开废液中获得1g菌体干物质需消耗COD 1625mg／L。     

酿酒酵母培养基中主要因素对海藻糖积累的影响

在对实验室保藏菌种Saccharomyces cerevisiae HY01优化前的摇瓶发酵观察的基础上,采用单因子与响应曲面相结合的实验设计方法研究了酿酒酵母培养基中的初始葡萄糖浓度、无机氮源硫酸铵浓度、酵母浸出粉浓度、碳源与无饥氮源的交互作用以及无机盐和微量元素浓度对海藻糖积累的影响。实验证明碳氮源交互作用明显,并得到了以上各因素的最优值,即初始葡萄糖浓度为20g／L,(NH4)2SO4浓度为4．5g／L,酵母浸出粉浓度为5g／L,微量元素溶液5．0ml／L;硫酸镁0．3g／L;磷酸氢二钠3．67g／L;磷酸二氢钾0．76g／L时,酿酒酵母中海藻糖的干重含量可以达到14．74％,比优化前海藻糖的干重含量12．24％提高了20．41％．     

海藻糖生产过程中产酶发酵条件的研究

研究了产酶的培养基组分和比例以及最佳培养条件对微球菌生产麦芽寡糖基海藻糖合成酶(MTSase)和麦芽寡糖基海藻糖海藻糖水解酶(MTHase)的影响,得到最优培养基组成为：葡萄糖2．0％,酵母膏2．0％,蛋白胨1．0％,磷酸氢二钾0．1％,硫酸镁0．05％;优化后的培养条件为：以15％的接种量接种至250mL的锥形瓶中,装液量为50mL,初始pH值7．5～8．5,培养温度为30℃,摇床培养4d。经优化后菌体干重由原来的1．938g／L增加到18．5g／L,生物量几乎增长了10倍;而酶活也由原来的30．64U／g增加到206．11U／g,酶活提高了接近7倍。     

酵母酶系合成三磷酸鸟苷的研究

研究了利用啤酒酵母细胞酶系催化鸟苷酸(GMP)合成三磷酸鸟苷(GTP)的工艺过程。采用分式析因及响应面实验设计对其工艺条件进行优化,分析了温度、pH、酵母、无机盐和表面活性剂等因素对GTP积累的影响,得到了一个可以较好预测实际反应的二次方模型以及优化条件即：GMP 7．16g/L,葡萄糖55g/L,酵母270g/L,硫酸氨1．5g/L,硫酸镁2g/L,磷酸二氢钾27．2g/L,表面活性剂8川L,氯化十六烷基吡啶1．5g/L,pH6．74,温度37．4℃。经过优化,反应得率从71．3％增至92．7％,较国内外报道的水平(80％)提高了12．7％.     

几种食用菌菌丝体液体培养条件的研究

研究了鲍鱼菇、黑灵芝、猴头菇和羊肚菌等4种食用菌菌丝体的最佳液体培养条件。结果各食用菌适宜的培养条件为：鲍鱼菇：果糖20g／L,酵母浸膏2g／L,KHP040．5g／L,VC0．001g／L,适宜培养温度28℃,pH5;黑灵芝：葡萄糖20g／L,蛋白胨2g／L,K2HP040．5g／L,VB20．001g／L,适宜培养温度35℃,pH6;猴头菇：麦芽糖20g／L,酵母浸膏2g／L,K2HID040．5g／L,MgSO,0．5g／L,VB10．001g／L,适宜培养温度28℃,pH7;羊肚菌：蔗糖20g／L,蛋白胨2g／L,K2HP040．5g／L,VB10．001g／L,适宜培养温度28℃,pH7。     

响应面法优化毛霉菌发酵培养基

采用响应面分析方法优化毛霉菌B的发酵培养基,首先通过单因素试验筛选出葡萄糖为最适碳源,酵母膏和玉米浆为最适氮源,用Plackett—Burman试验对葡萄糖、酵母膏、玉米浆、MgSO4、FeSO4、NILCl/、HPO4进行评估并筛选出具有显著效应的3个因素：葡萄糖、酵母膏、玉米浆,再通过最陡爬坡试验逼近其最大响应区域,最后采用Box—Behnken试验对其用量进行优化,得到毛霉菌最佳发酵培养基（g/L）：葡萄糖51．54,酵母膏5．22,玉米浆14．31,MgSO40．5,FeSO40．1,NH4Cl3,k2HPO43,pH6．0～6．5。培养基优化后,毛霉生物量由23．51g／L提高至31．13g/L,比对照组提高32．41％,腺嘌呤转化率由53．59％提高至59．97％,ATP产率由6．56g／L提高至7．34g／L,比对照组提高11．89％。     

响应面法优化产酰胺酶发酵培养基

采用响应面分析方法,对阿萨希丝孢酵母（Trichosporon asahii）ZZB-1产酰胺酶的发酵培养基进行了优化。运用单N子试验筛选出麦芽糖和酵母浸膏为最适碳源、氮源,金属离子Ca^2＋、Mn^2＋可提高发酵酰胺酶产量;通过最陡爬坡实验逼近以上4个因子的最大响应区域后,采用Box—Behnken响应面分析法,确定产酰胺酶最佳发酵培养基为麦芽糖18．84g／L、酵母浸膏9．55g／L、NaC15g／L、KH2PO41g／L、MgSO4·7H2O0．2g／L、FeS040．001g／L、CaC0370．84μmol／L、MnS0465．39肚mo[／L（1％丙烯酸诱导）,NH4·H2O调节pH至7．0。培养基优化后酰胺酶产量由初始2554U／L提高到4156U／L,为原始发酵培养基配方酶活产量的1．63倍。     

红酵母类胡萝卜素高产菌株的筛选及其发酵生理学条件研究

从数株红酵母中选出了1株产类胡萝卜素能力较强的红酵母RY－98（生物量,类胡萝卜素含量和产量分别为19．9g/L,334.8ug/g和6．7mg/L);研究了该菌株产类胡萝卜素的最适营养与环境条件,获得了最佳的发酵生理学条件;葡萄糖40g/L,(NH4)2SO4 10g/L,酵母膏3g/L,蕃茄汁2mL/L,花生油0.5mL/L,接种量30mLL初始pH6.0和通气量（培养基装置040ml/250mL:,在此初步优化的培养条件下,红酵母RY－98经72小时摇瓶发酵其生物量,类胡萝卜素含量和产量分别可达26．8g/L,386.9ug/g和10．4mg/L,依次比初筛中提高了34．7％,15．6％,和55．2％。     

十三烷1,13—二羧酸的发酵研究

热带假丝酵母(C.tropicalis)NP-6-126是经过紫外线和亚硝酸反复诱变筛选培育出来的,它是生产十三烷1,13一二羧酸(DC_(15)的优良生产突变株,尿素和硝酸钾浓度对其产酸有明显影响。尿素浓度在0.15％～0.21％范围内对产酸有利,尤其是0.18％最佳,浓度增大,明显抑制DC_(15)的产生和积累;硝酸钾的加入,也明显促进DC_(15)产量的提高,0.6％～0.9％硝酸钾浓度较合适。于16L自动控制罐发酵7d,DC_(15)达到130g/L,放大到2500L罐,在最佳条件下,连续5批,发酵6d,DC_(15)产量平均达到176g/L,正十五烷(nC_(15)转化率平均为52.5％,后处理总收率平均为80.6％,DC_(15)的纯度平均为95.83％。     

Degradation of phenol by aerobic granules and isolated yeast Candida tropicalis

Aerobic granules effectively degrade phenol at high concentrations. This work cultivated aerobic granules that can degrade phenol at a constant rate of 49 mg-phenol/g x VSS/h up to 1,000 mg/L of phenol. Fluorescent staining and confocal laser scanning microscopy (CLSM) tests demonstrated that an active biomass was accumulated at the granule outer layer. A strain with maximum ability to degrade phenol and a high tolerance to phenol toxicity isolated from the granules was identified as Candida tropicalis via 18S rRNA sequencing. This strain degrades phenol at a maximum rate of 390 mg-phenol/g x VSS/h at pH 6 and 30 degrees C, whereas inhibitory effects existed at concentrations >1,000 mg/L. The Haldane kinetic model elucidates the growth and phenol biodegradation kinetics of the C. tropicalis. The fluorescence in situ hybridization (FISH) and CLSM test suggested that the Candida strain was primarily distributed throughout the surface layer of granule; hence, achieving a near constant reaction rate over a wide range of phenol concentration. The mass transfer barrier provided by granule matrix did not determine the reaction rates for the present phenol-degrading granule.     

Cadmium biosorption by yeast, Candida tropicalis CBL-1, isolated from industrial wastewater

The present study is aimed at assessing the ability of metal-resistant yeast, Candida tropicalis CBL-1, to uptake metal from liquid medium. The minimum inhibitory concentration of Cd(II) against Candida tropicalis CBL-1 was 2,800 mg/L. The yeast could also tolerate Zn(II) (3,100 mg/L), Hg(II) (2,400 mg/L), Ni(II) (2,200 mg/L), Cr(VI) (2,000 mg/L), Pb(II) (1,100 mg/L), and Cu(II) (2,200 mg/L). The yeast isolate showed typical growth curves but lag and log phases extended in the presence of cadmium. The yeast isolate showed optimum growth at 30oC and pH 7. The metal processing ability of the isolate was determined in a medium containing 100 mg/L of Cd(II). Candida tropicalis CBL-1, could reduce Cd(II) 59%, 64% and 70% from the medium after 48, 96 and 144 h, respectively. C. tropicalis CBL-1 was also able to remove Cd(II) 46% and 60% from the wastewater after 6 and 12 days, respectively. Cd produced an increase in glutathione and non-protein thiols level by 37% (17.50±0.8-24.0±1.2) and 18% (3.30±0.7- 3.90±0.8) at 100 mg/L concentration, respectively. Metal tolerance and accumulation together with changes in the GSH status and non-protein thiols under Cd exposure were studied in C. tropicalis.     

微生物发酵生产十三碳二元酸的研究

分类号ＴＱ９２０．１文献标识码Ｂ文章编号０００１６２０９（１９９９）０３０２７９８１十三碳二元酸（ＤＣ１３）是化学合成麝香Ｔ香料和尼龙１３１３工程塑料的重要原料。ＤＣ１３在自然界中不单独存在,用化学方法难以合成,只能从菜籽油中提出甘油芥酸酯再经…     

丙烯酸对十六碳二元酸发酵的影响和16L罐扩试

本文报道丙烯酸对发酵生产十六碳二元酸(DC_(16))的影响,加入0.1%丙烯酸,DC_(16)产量提高20—30%.在16L自动控制罐上,在最佳条件下,加入20%(v/v)正十六烷(nC_(16)),发酵5天,DC_(16)高达120g/L,nC_(16)的转化率高达79%.     

液蜡发酵制取混合二元酸的研究

A mutant of Candida tropicalis FYD-2 was obtained from its parental strain SFP-1186 by ultraviolet treatments.On shaking flask,the yield of mixed dicarboxylic acid(DCA) by the mutant was 21.4% higher than that by its ancestor.The amount of mixed DCA reached 156g/L for 120h incubation in a 10 L autoconrolled fermentor where the culture medium contained 25% n-paraffin.The process of induced and screening mutant was introduced and the time course of fermentation in 10 L fermentor was discussed.     

Xylitol production is increased by expression of codon-optimized Neurospora crassa xylose reductase gene in Candida tropicalis

Xylose reductase (XR) is the first enzyme in D: -xylose metabolism, catalyzing the reduction of D: -xylose to xylitol. Formation of XR in the yeast Candida tropicalis is significantly repressed in cells grown on medium that contains glucose as carbon and energy source, because of the repressive effect of glucose. This is one reason why glucose is not a suitable co-substrate for cell growth in industrial xylitol production. XR from the ascomycete Neurospora crassa (NcXR) has high catalytic efficiency; however, NcXR is not expressed in C. tropicalis because of difference in codon usage between the two species. In this study, NcXR codons were changed to those preferred in C. tropicalis. This codon-optimized NcXR gene (termed NXRG) was placed under control of a constitutive glyceraldehyde-3-phosphate dehydrogenase (GAPDH) promoter derived from C. tropicalis, and integrated into the genome of xylitol dehydrogenase gene (XYL2)-disrupted C. tropicalis. High expression level of NXRG was confirmed by determining XR activity in cells grown on glucose medium. The resulting recombinant strain, LNG2, showed high XR activity (2.86 U (mg of protein)(-1)), whereas parent strain BSXDH-3 showed no activity. In xylitol fermentation using glucose as a co-substrate with xylose, LNG2 showed xylitol production rate 1.44 g L(-1) h(-1) and xylitol yield of 96% at 44 h, which were 73 and 62%, respectively, higher than corresponding values for BSXDH-3 (rate 0.83 g L(-1) h(-1); yield 59%).     

氟康唑对热带念珠菌活性氧和线粒体膜电位的影响

为了探讨氟康唑作用机制,观察它对热带念珠菌作用后存活率、活性氧(Reactive oxygen species,ROS)、线粒体膜电位(Mitochondrial membrane potential,△Ψm)和细胞周期的变化。参照NCCLS M27-A方案的微量稀释法测定氟康唑对热带念珠菌的最低抑菌浓度(MIC);热带念珠菌与不同浓度氟康唑共同培养后用流式细胞术(Flow cytometry,FCM)分析热带念珠菌存活率、ROS、线粒体膜电位△Ψm和细胞周期的变化。结果表明,氟康唑作用后,热带念珠菌氟康唑耐药株的存活率、ROS、线粒体膜电位△Ψm和细胞周期各期比例均没有明显变化;而热带念珠菌氟康唑敏感株的存活率和线粒体膜电位△Ψm明显下降,ROS明显升高,而且大部分热带念珠菌阻滞于G2/M期,并出现明显凋亡峰,呈一定的时间剂量依赖关系。自由基清除剂谷胱甘肽抑制热带念珠菌ROS的产生,阻止细胞周期G2/M期阻滞和降低凋亡。由此可见,氟康唑可能通过刺激热带念珠菌产生过多ROS,并使线粒体膜电位△Ψm下降,从而诱导热带念珠菌凋亡。     

Production of xylitol from D-xylose by Candida tropicalis: optimization of production rate

The effect of culture conditions on xylitol production rate was investigated using Candida tropicalis IFO 0618. From the variance analysis of xylitol production rate, it was found that initial yeast extract concentration was highly significant (99%), while the interaction between D-xylose concentration and aeration rate was significant (95%). These results show the importance of initial yeast extract concentration and of the balance between D-xylose concentration and aeration in the production of xylitol. It was also clearly shown that C. tropicalis needed more yeast extract concentration for efficient xylitol production than for its growth. In order to enhance xylitol production rate, culture conditions were optimized by the Box-Wilson method. In this respect, initial D-xylose concentration, yeast extract concentration, and K(L)a were chosen as the independent factors in 2(3)-factorial experimental design. As the result of experiments, a maximum xylitol production rate of 2.67 g/L . h was obtained when initial D-xylose concentration and yeast extract concentration were 172.0 and 21.0 g/L, respectively, and K(L)a was 451.50 h(-1) by 90% oxygen gas. (c) 1992 John Wiley & Sons, Inc.     

聚氨酯固定化热带假丝酵母发酵木糖醇

固定在多孔聚氨酯载体中的热带假丝酵母(Candida tropicalis), 可有效地利用玉米芯半纤维素水解液生产木糖醇。在摇瓶条件下, 采用分批发酵方式, 确立了适宜的发酵工艺参数为: 接种量7%, 聚氨酯加入量1.0 g/100 mL, 温度30°C, 初始pH值6.0, 分段改变摇床转速进行溶氧调节, 其中0~24 h 为200 r/min; 24 h~46 h为140 r/min。聚氨酯固定化提高了菌体对发酵抑制物的耐受力, 固定化细胞密度高, 发酵性能稳定, 发酵产率和体积生产速率都有所提高。水解液未经脱色与离子交换便可转化成木糖醇, 大幅降低了成本, 显示了良好的应用前景。固定化细胞连续重复进行12批次21 d的发酵, 木糖醇得率平均为67.6%, 体积生产速率平均为1.92 g/(L·h)。