麦白霉素发酵培养基的改进

研究了淀粉水解液全部替代葡萄糖作为碳源发酵麦白霉素的工艺条件。用正交实验得出摇瓶培养基消毒后的最佳基质浓度为总糖5.0g/100mL,还原糖3.8g/100mL,氨基氮60mg/mL,溶解磷300μg/mL。以50L发酵罐进行实验,得出了麦白霉素的发酵代谢曲线和淀粉的适宜水解条件。经30t发酵罐放大实验结果表明,与葡萄糖作碳源相比,用淀粉水解液作碳源发酵麦白霉素,发酵单位提高23.0％,生产成本降低38.0％。     

黑曲霉S1生淀粉糖化酶生物合成的调节研究

本文对黑曲霉S_1(Aspergillus niger S_1)生淀粉糖化酶生物合成调节进行了初步研究,认为该菌生淀粉糖化酶的合成与菌体生长呈负相关,即酶的合成过程是典型的选择性合成过程。该菌生淀粉糖化酶的合成受降解物阻遏调控,缓慢供给低浓度易利用碳源和添加环腺苷磷酸(cAMP)可使酶的合成消阻遏,通过研究放线菌素C_1(Actinomycin C_1)等抑制剂对酶合成的影响而推断黑曲霉S_1生淀粉糖化酶合成的阻遏调控发生在转录水平上。     

重组Bacillus subtilis产B.stearothermophilus环糊精葡萄糖基转移酶的发酵优化

利用本研究室已构建的重组菌Bacillus subtilis/pBSMuL3-α/β-CGTase对产B.stearothermophilus环糊精葡萄糖基转移酶的发酵产酶进行了优化,考察了培养基中重要成分:碳源、有机氮源、无机氮源、有机与无机氮源质量比、碳源与氮质量比、金属离子种类等单因素对该重组菌产α/β-CGTase的影响,并采用正交实验对发酵培养基进行优化,对优化结果分析可知,重组菌B.subtilis/pBSMuL3-α/β-CGTase发酵产α/β-CGTase的最优培养基成本为:葡萄糖5 g/L,氮源(鱼骨蛋白胨∶NH4Cl=3∶1)25 g/L,1 mmol/L Mg^2+。在最优条件下发酵培养,α/β-CGTase的酶活由原来TB发酵培养基的9.20 U/mL提高至20.32 U/mL,是优化前酶活的2.2倍,为α/β-环糊精葡萄糖基转移酶的工业应用提供了理论支持。     

一株降解生木薯淀粉的曲霉菌株的筛选、鉴定及其淀粉降解特性

本研究利用以生木薯淀粉为唯一碳源的筛选培养基,从腐烂木薯渣中分离筛选出一株可以降解生木薯淀粉的真菌菌株RSDF-7.根据RSDF-7形态和18S rDNA与28S rDNA之间的内转录间隔区(internal transcribed spacer,ITS)序列分析的结果,初步认定该菌株为曲霉属.菌株RSDF-7的粗酶液对多种不同的生淀粉底物均有水解效果;在以大米和玉米淀粉为底物时,其生淀粉分解活力比较高,分别为42%和40%.菌株RSDF-7的粗酶液具有良好的低pH稳定性,对生木薯淀粉的最适作用温度为50℃,最适作用pH为4.5.在30 min的吸附后,RSDF-7的粗酶液对生木薯淀粉的吸附力高达60%.使用HPLC对粗酶液的酶解产物进行检测,结果发现酶解产物中仅存在葡萄糖,表明菌株RSDF-7所产的生淀粉降解酶主要为糖化酶.扫描电镜观察结果发现,经RSDF-7粗酶液酶解后的生木薯粉颗粒破裂,形成空洞,说明RSDF-7粗酶液对生淀粉有较强的水解作用.可以预见,经纯化后的曲霉菌株RSDF-7生淀粉酶将来可以用于基于酶解的木薯淀粉转化.     

拟康氏木霉(Trichoderma psudodoningii)UV III产纤维素酶液体发酵研究

以拟康氏木霉(Trichoderma psudodoningii)TH为出发菌株,经紫外诱变荻得一抗高浓度葡萄糖阻遏突变株uV III,其液体发酵最适产酶培养基为(w/V)豆皮粉3%,硝酸铵0.6%,磷酸二氢钠0.65%,硫酸镁0.25%,氯化钙0.15%,pH5.0;最佳发酵条件为30℃,125r/min发酵7d CMCase活力可达103.55 IU/mL,滤纸酶活可达5.51 IU/mL,β一葡萄糖苷酶活可达0 96IU/mL,分别比出发菌株TH提高了1.40、2.34、0.60倍.     

地衣芽抱杆菌A.4041耐高温α-淀粉酶的研究

地衣芽抱杆菌A.4041是一株产生耐高温α-淀粉酶的突变株。本文研究了A.4041发酵培养基的成份,发现用天然碳源原料产酶优于葡萄塘、乳糖和淀粉。葡萄糖对发酵产酶有一定程度的抑制作用。此外还发现A.4041所产生的耐高温α-淀粉酶的热稳定性与Ca²⁺浓度有关,高浓度氯化钠与淀粉能促进该酶的耐热性。     

米曲霉木聚糖酶生产菌的理性选育及发酵优化

目的：米曲霉木聚糖酶生产菌的理性选育及发酵优化。方法：以米曲霉FS018为出发菌株,采用紫外和激光诱变先后处理3代,以抗高浓度葡萄糖阻遏效应为筛选模型获得一株高产木聚糖酶菌株FST036,并对该菌株的发酵培养基进行了初步优化。结果：突变株FST036产酶水平可达4200．57U／mL,产酶水平比出发菌株提高了24％。对该菌株的发酵培养基初步优化结果表明：培养基的最适氮源为牛肉膏;最适碳源为麸皮与玉米芯组合,总浓度为4％。二者最适比例为7：3;对该菌株的发酵条件初步优化结果表明：最适接种量1％,初始pH6．78,250mL三角瓶装液量为45mL,培养72h酶活可达5404．24U／mL。结论：反复多次诱变处理,并结合抗高浓度葡萄糖阻遏效应作为一种理性筛选模型,为通过诱变育种来获得曲霉木聚糖酶高产菌株提供了一条有效的途径。     

Agarivorans albus RZW1-1产琼胶酶的发酵条件优化

为了提高菌株Agarivorans albus RZW1-1的产琼胶酶能力,本研究通过单因素实验探究碳源、氮源、海盐浓度、琼脂浓度、初始pH、装液量、培养时间、培养温度等因素对产酶的影响,得到该菌株的最佳发酵条件。在单因素实验的基础之上,运用正交试验的方法,得到菌株RZW1-1产酶最高的培养基组分。综合单因素实验和正交设计,最终确定了最佳产酶条件为:葡萄糖0.2 g/L、酵母粉9 g/L、海盐浓度4%、琼脂粉浓度0.1%,在装液量25 m L (250 m L三角瓶)、初始pH7.0、28℃、130 r/min条件下培养48 h酶活力达到最高为23.020 U/mL,较基础培养基提高了2.01倍。     

产紫青霉中β-葡萄糖醛酸苷酶的诱导表达

针对产紫青霉(Penicillium purpurogenum)Li-3发酵生产β-葡萄糖醛酸苷酶存在的碳代谢阻遏现象,研究β-葡萄糖醛酸苷酶的高效诱导表达策略。在发酵条件优化的基础上,建立了新的产酶诱导工艺:葡萄糖的初始质量浓度5 g/L,在葡萄糖耗尽时加入20%诱导剂(10 g/L GL+1.2%Tween80)进行诱导,每24 h添加1次诱导剂,诱导72 h后立即转到40℃摇床发酵48 h。采用该工艺进行发酵,菌体出现了"二次生长"现象,比酶活从647.99 U/mL提高至2 356 U/mL,提高了近3倍。     

纳豆激酶产生菌——纳豆菌对木糖和葡萄糖的利用

在纳豆激酶 (Nattokinase,简称NK)发酵条件研究中 ,我们发现木糖是较葡萄糖更佳的产酶碳源。进一步的试验证明 ,NK的发酵菌种———Bacillussubtilisvar.natto在混合碳源中没有二次生长现象 ,对木糖和葡萄糖的吸收是同时的 ,且互不干扰 ,葡萄糖对木糖的吸收利用没有分解代谢阻遏。     

Regulation of beta-1, 4-Glucosidase Expression by Candida wickerhamii

Candida wickerhamii NRRL Y-2563 expressed beta-glucosidase activity (3 to 8 U/ml) constitutively when grown aerobically in complex medium containing either glycerol, succinate, xylose, galactose, or cellobiose as the carbon source. The addition of a high concentration of glucose (>75 g/liter) repressed beta-glucosidase expression (<0.3 U/ml); however, this yeast did produce beta-glucosidase when the initial glucose concentration was 相似文献   

Penicillinamidohydrolase inEscherichia coli

Synthesis of penicillinamidohydrolase (penicillin acylase, EC 3.5.1.11) in Escherichia coli is subjected to the absolute catabolite repression by glucose and partial repression by acetate. Both types of catabolite repression of synthesis of the enzyme in Escherichia coli are substantially influenced by cyclic 3',5'-adenosinemonophosphate (cAMP). Growth diauxie in a mixed medium containing glucose and phenylacetic acid serving as carbon and energy sources is overcome by cAMP. cAMP does not influence the basal rate of the enzyme synthesis (without the inducer). Derepression of synthesis of penicillinamidohydrolase by cAMP in a medium with glucose and inducer (phenylacetic acid) is associated with utilization of the inducer, due probably to derepression of other enzymes responsible for degradation of phenylacetic acid. Lactate can serve as a "catabolically neutral" source of carbon suitable for the maximum production of penicillinamidohydrolase. The gratuitous induction of the enzyme synthesis in a medium with lactate as the carbon and energy source and with phenylacetic acid is not influenced by cAMP; however, cAMP overcomes completely the absolute catabolite repression of the enzyme synthesis by glucose.     

Improvement in raw sago starch degrading enzyme production from Acremonium sp. endophytic fungus using carbon and nitrogen sources

Attempts were made to improve the growth of endophytic fungus Acremonium sp. and its raw sago starch degrading enzyme (RSSDE) production using different nitrogen and carbon sources at varying pH values and temperatures. It was observed that growth and enzyme activity levels were highest with peptone and sodium nitrate as the nitrogen sources and raw sago starch as the carbon source of which the optimum concentrations were 0.5 g/l, 3 g/l, and 20 g/l, respectively. Cell growth and RSSDE production reached their optimum at pH 5.0 and incubation temperature of 30 degrees C. Under these conditions, the enzyme production was significantly increased by 19- to 22-folds compared to the activity obtained in the original basal medium.     

Control mechanisms operative in a natural microbial population selected for its ability to degrade L-lysine. I. Effect of glucose in batch systems

A natural microbial population was selected in a medium containing L-lysine as the sole carbon source and ammonia as a nitrogen source. Cells were harvested from a batch-operated fermentor containing lysine and were grown through one transfer on lysine, glucose, or a mixture of lysine and glucose. By comparing the substrate removal rates and enzymatic capabilities of the cells, it was determined that the inducible enzyme system responsible for lysine degradation was subject to catabolic repression. Inhibition of the activity of preformed enzyme(s) played only a minor role. Preinduction by lysine offered only a small degree of protection against repression. The removal of ammonia nitrogen from the system did not overcome the effect of glucose.     

Regulation of β-1, 4-Glucosidase Expression by Candida wickerhamii

Candida wickerhamii NRRL Y-2563 expressed β-glucosidase activity (3 to 8 U/ml) constitutively when grown aerobically in complex medium containing either glycerol, succinate, xylose, galactose, or cellobiose as the carbon source. The addition of a high concentration of glucose (>75 g/liter) repressed β-glucosidase expression (<0.3 U/ml); however, this yeast did produce β-glucosidase when the initial glucose concentration was ≤50 g/liter. When grown aerobically in medium containing glucose plus the above-listed carbon sources, diauxic utilization of the carbon source was observed and the expression of β-glucosidase was glucose repressed. Surprisingly, glucose repression did not occur when the cells were grown anaerobically. When grown anaerobically in medium containing 100 g of glucose per liter, C. wickerhamii produced 6 to 9 U of enzyme per ml and did not demonstrate diauxic utilization of glucose-cellobiose mixtures. To our knowledge, this is the first report of apparent derepression of a glucose-repressed enzyme by anaerobiosis.     

Characteristics of alanine: glyoxylate aminotransferase from Saccharomyces cerevisiae, a regulatory enzyme in the glyoxylate pathway of glycine and serine biosynthesis from tricarboxylic acid-cycle intermediates.

Alanine: glyoxylate aminotransferase (EC 2.6.1.44), which is involved in the glyoxylate pathway of glycine and serine biosynthesis from tricarboxylic acid-cycle intermediates in Saccharomyces cerevisiae, was highly purified and characterized. The enzyme had Mr about 80 000, with two identical subunits. It was highly specific for L-alanine and glyoxylate and contained pyridoxal 5'-phosphate as cofactor. The apparent Km values were 2.1 mM and 0.7 mM for L-alanine and glyoxylate respectively. The activity was low (10 nmol/min per mg of protein) with glucose as sole carbon source, but was remarkably high with ethanol or acetate as carbon source (930 and 430 nmol/min per mg respectively). The transamination of glyoxylate is mainly catalysed by this enzyme in ethanol-grown cells. When glucose-grown cells were incubated in medium containing ethanol as sole carbon source, the activity markedly increased, and the increase was completely blocked by cycloheximide, suggesting that the enzyme is synthesized de novo during the incubation period. Similarity in the amino acid composition was observed, but immunological cross-reactivity was not observed among alanine: glyoxylate aminotransferases from yeast and vertebrate liver.     

Direct production of L-lysine from raw corn starch by Corynebacterium glutamicum secreting Streptococcus bovis alpha-amylase using cspB promoter and signal sequence

Corynebacterium glutamicum is an important microorganism in the industrial production of amino acids. We engineered a strain of C. glutamicum that secretes α-amylase from Streptococcus bovis 148 (AmyA) for the efficient utilization of raw starch. Among the promoters and signal sequences tested, those of cspB from C. glutamicum possessed the highest expression level. The fusion gene was introduced into the homoserine dehydrogenase gene locus on the chromosome by homologous recombination. L-Lysine fermentation was conducted using C. glutamicum secreting AmyA in the growth medium containing 50 g/l of raw corn starch as the sole carbon source at various temperatures in the range 30 to 40°C. Efficient L-lysine production and raw starch degradation were achieved at 34 and 37°C, respectively. The α-amylase activity using raw corn starch was more than 2.5 times higher than that using glucose as the sole carbon source during L-lysine fermentation. AmyA expression under the control of cspB promoter was assumed to be induced when raw starch was used as the sole carbon source. These results indicate that efficient simultaneous saccharification and fermentation of raw corn starch to L-lysine were achieved by C. glutamicum secreting AmyA using the cspB promoter and signal sequence.     

Use of sugarcane bagasse and grass hydrolysates as carbon sources for xylanase production by Bacillus circulans D1 in submerged fermentation

The use of sugarcane bagasse and grass as low cost raw material for xylanase production by Bacillus circulans D1 in submerged fermentation was investigated. The microorganism was cultivated in a mineral medium containing hydrolysate of bagasse or grass as carbon source. High production of enzyme was obtained during growth in media with bagasse hydrolysates (8.4 U/mL) and in media with grass hydrolysates (7.5 U/mL). Xylanase production in media with hydrolysates was very close to that obtained in xylan containing media (7.0 U/mL) and this fact confirm the feasibility of using this agro-industrial byproducts by B. circulans D1 as an alternative to save costs on the enzyme production process.     

枯草芽孢杆菌ccpA基因敲除及对其核黄素产量的影响

CcpA蛋白是介导枯草芽孢杆菌碳分解代谢物阻遏(CCR)的全局调控因子,由ccpA基因编码。CCR效应的存在影响B.subtilis对葡萄糖的利用,降低B.subtilis生产发酵产品的效率。采用基因重组技术敲除了核黄素发酵菌株B.subtilis24/pMX45的ccpA基因,构建了CcpA缺陷株B.subtilis24A1/pMX45。发酵结果显示:B.subtilis24A1/pMX45能够在70h内基本耗尽10%的葡萄糖,生物量达到1.5×109个细胞/mL,溢流代谢产物积累量减少,在8%和10%葡萄糖浓度下,B.subtilis24A1/pMX45核黄素产量分别比B.subtilis24/pMX45提高了62%和95%。CcpA的缺陷,可以缓解葡萄糖引起的CCR效应,显著提高菌株的核黄素产量。