重组毕赤酵母表达棘孢木霉几丁质酶Tachi1的酶学性质研究及表达条件优化

【目的】对转棘孢木霉几丁质酶基因tachi1的毕赤酵母工程菌GS-tachi1-K进行诱导表达,研究重组几丁质酶Tachi1的酶学性质,优化表达条件。【方法】对GS-tachi1-K进行甲醇诱导培养,纯化目的蛋白Tachi1进行几丁质酶酶学性质的研究;通过单因素和正交试验对GS-tachi1-K菌株产几丁质酶Tachi1表达条件进行优化。【结果】GS-tachi1-K表达的几丁质酶Tachi1表观分子量约为44 kDa,酶反应最适的温度和pH分别为50℃和5.5,具有较宽的温度、pH适用范围;50℃以下保持较高的酶活力,在碱性条件下稳定性较差;受Ag+、Hg2+、Cu2+、Fe2+和高浓度的SDS及β-巯基乙醇强烈抑制。该菌株的最佳表达条件为:pH为6.5,甲醇诱导浓度为0.5%,起始细胞浓度为OD600=2,甲醇诱导时间为180 h;几丁质酶Tachi1活力可达17.93 U/mL,蛋白表达量为6.19 g/L。【结论】成功实现了棘孢木霉新几丁质酶基因tachi1的毕赤酵母高效分泌表达,工程菌GS-tachi1-K具有高表达量和表达产物酶活性高两个特点,明确了几丁质酶Tachi1的酶学性质和最佳诱导表达条件,为该几丁质酶及其基因的深入研究和开发利用奠定了基础。     

重组巴斯德毕赤酵母发酵生产内切几丁质酶的培养条件优化

探讨重组巴斯德毕赤酵母发酵生产内切几丁质酶的最适培养条件,以期获得最佳的内切几丁质酶活力。以内切几丁质酶活力为指标,通过部分因子试验设计以及响应面法优化确定重组巴斯德毕赤酵母高产内切几丁质酶的最适培养条件。部分因子试验设计筛选的影响重组巴斯德毕赤酵母高产内切几丁质酶的3个关键因子为甲醇、油酸和吐温-80。响应面法优化的上述3个关键因子的最佳浓度分别为0.71%、0.086%和0.31%。重组巴斯德毕赤酵母发酵生产内切几丁质酶的最适培养条件为：酵母膏1%、酵母氮碱（YNB）1.34%、蛋白胨2%、甲醇0.71%、油酸0.086%、吐温-80 0.31%、PTM₁ 0.8%、pH 6.0。在上述培养条件下,重组巴斯德毕赤酵母产内切几丁质酶的活力高达30.92U/mL。与未优化前相比,酶活力提高了1.44倍。研究结果为内切几丁质酶的产业化生产和应用奠定了良好基础。     

嗜热子囊菌原变种Thermoascus aurantiacus var.aurantiacus热稳定几丁质酶的克隆表达及活性研究

研究通过RT-PCR和Tail-PCR技术从嗜热子囊菌原变种Thermoascus aurantiacus var.aurantiacus中克隆了一个几丁质酶同源基因。该基因全长1,253bp,包含一个由1,197个碱基构成的开放阅读框,编码398个氨基酸。序列比对分析表明,该基因编码蛋白属于糖苷水解酶18家族的几丁质酶。利用基因重组的方法构建酵母分泌型表达载体,并转化毕赤酵母。在甲醇的诱导下,重组蛋白得到了高效表达,第6天的表达量最高,达到0.433g/L,酶活力为28.96U/mg,同时对表达的几丁质酶进行了纯化,SDS-PAGE检测该蛋白的分子量为43.9kDa。该几丁质酶的最适反应温度为60℃,最适反应pH值为8.0,70℃处理30min仍有45%的相对酶活,具有较好的热稳定性及工业应用价值。     

响应面法优化重组巴斯德毕赤酵母合成ECH42的培养基组分及其重组酶降解几丁质的研究

采用响应面法在摇瓶水平对重组巴斯德毕赤酵母合成内切几丁质酶的培养基组分进行优化,并探讨重组内切几丁质酶降解几丁质的最佳反应条件。首先对培养基中显著影响内切几丁质酶活力的关键组分通过Plackett-Burman试验设计进行筛选;然后通过Box-Behnken试验设计和响应面法确定关键组分的最佳浓度。结果筛选出3个具有显著效应的关键组分为酵母膏、油酸和吐温-80,最佳浓度分别为：2.45%、0.17%和0.62%。优化后的最佳培养基组成为：2.45%酵母膏、2.00%蛋白胨、0.50%酵母氮碱（YNB）、0.50%甲醇、0.17%油酸、0.62%吐温-80和0.40% PTM₁。在该培养基中,重组巴斯德毕赤酵母在摇瓶水平（25mL/250mL）发酵生产内切几丁质酶的活力高达92.26U/mL。重组内切几丁质酶催化几丁质降解的最佳反应条件为：粉末几丁质浓度为4%,pH和温度分别为7.0和30℃,反应时间为10h。研究结果为后期在发酵罐中大规模生产内切几丁质酶和几丁寡糖提供了基础。     

玉米赤霉烯酮降解酶多拷贝毕赤酵母菌株的构建及高效表达

通过密码子优化、体外多拷贝构建实现玉米赤霉烯酮(Zearalenone,ZEN)降解酶基因(zlhy-6)在毕赤酵母GS115菌株中的高效表达。按酵母密码子偏好性优化zlhy-6基因的密码子,与α因子信号肽编码序列一起合成,插入到pAO815质粒中,通过酶切酶连构建含1–6个表达盒的表达质粒,将其转入毕赤酵母GS115菌中,获得ZEN降解酶重组菌株。重组蛋白分子量为28.9 kDa,与预期一致。重组菌用甲醇诱导3 d,蛋白浓度达最高,之后下降;在pH 5.0、4.5条件下诱导培养,表达量最高;每天添加0.8%的甲醇、接种量10%表达水平最高;4拷贝的转化子表达水平最高,三角瓶发酵3 d,酶活性达到10 U/mL。在1 g玉米渣中添加0.1–0.5 mL发酵上清液,水解24 h,玉米渣中ZEN的降解率为44.08%–75.51%。研究结果为ZEN降解酶工业生产及在食品饲料中的应用奠定了基础。     

毕赤嗜甲醇酵母工程菌高密度培养表达黑曲霉菊粉内切酶的研究

目的:对毕赤嗜甲醇酵母工程菌inu-26高密度培养表达黑曲霉菊粉内切酶的条件进行优化,找出最佳的外源蛋白表达条件。方法:在摇瓶优化培养的基础上进行发酵罐高密度培养,优化最佳产酶条件。结果:以葡萄糖为碳源、微量元素添加量100～200mL/L、甲醇浓度1g/L、pH6.0～7.0、诱导时间96h时酶的表达量最高;摇瓶模拟高密度培养表明影响酵母生长的最主要因素葡萄糖和硫酸铵的最佳浓度分别为20～45和11.5g/L;利用培养基F1进行高密度培养优于其他培养基,工程菌生长符合指数生长曲线,细胞生长延迟期为1.36h,比生长速率μ为0.4846h-1。结论:以葡萄糖为碳源,采用葡萄糖-甲醇混合诱导和100%甲醇单一诱导相结合,在菌体鲜重约为280g/L时连续诱导96h,菌体生长良好,不会出现自溶,且酶的表达量最高,为摇瓶培养的3倍多,酶活最高可达540 U/mL。     

嗜热真菌Thermomyces lanuginosus热稳定几丁质酶基因的cDNA克隆及表达

根据Thermomyces lanuginosus热稳定几丁质酶Chit的N-端氨基酸序列和同源保守序列设计简并引物,通过RT-PCR及快速扩增cDNA末端(RACE)的方法,克隆了该几丁质酶的编码基因chit,全长cDNA为1500bp,包含一个由442个氨基酸组成的开放阅读框。该基因已在GenBank中注册,登录号为DQ092332。将成熟肽几丁质酶Chit阅读框与酵母表达载体pPIC9K连接,构建重组质粒pPIC9K/chit,转化毕赤酵母GS115,在甲醇的诱导下,成功地分泌出具生物活性的几丁质酶,诱导6d后酶活性达2.261U/mL,酶蛋白表达量为0.36mg/mL。该酶的最适反应温度和pH值分别为60℃和5.5,该酶在50℃以下稳定;65℃的半衰期为40min。     

美洲大蠊几丁质酶基因的原核表达及蛋白纯化

昆虫几丁质酶是昆虫几丁质代谢不可或缺的关键酶类。本研究旨在构建美洲大蠊几丁质酶Pa Cht1基因原核表达载体,纯化并鉴定Pa Cht1重组蛋白,为后续酶活等测定奠定基础。定向克隆Pa Cht1基因成熟肽序列至原核表达载体pET32a(+)上,将构建成功的pET32a-Cht1重组表达质粒导入大肠埃希菌Rosetta中,分别对诱导剂IPTG浓度和诱导时间进行优化,确定最佳诱导浓度和诱导时间,并对表达产物进行可溶性分析。表达产物经镍离子柱纯化后通过Western Blot鉴定。结果表明,美洲大蠊几丁质酶Pa Cht1成熟肽基因编码区长1 083 bp,编码360个氨基酸。最佳诱导浓度和诱导时间分别为0.2 mmol/L和4 h。所得重组蛋白大小约60 k D,与预期结果大小一致,重组蛋白主要以包涵体的形式存在。Western Blot鉴定重组蛋白可与6×His-tag单克隆抗体特异性结合。说明成功构建了原核表达载体pET32a-Cht1,并诱导表达获得了重组几丁质酶蛋白。     

嗜热真菌Thermomyces lanuginosus热稳定几丁质酶基因的cDNA克隆及表达

根据Thermomyces lanuginosus热稳定几丁质酶Chit的N端氨基酸序列和同源保守序列设计简并引物,通过RTPCR及快速扩增cDNA末端（RACE）的方法,克隆了该几丁质酶的编码基因chit,全长cDNA为1500bp,包含一个由442个氨基酸组成的开放阅读框。该基因已在GenBank中注册,登录号为DQ092332。将成熟肽几丁质酶Chit阅读框与酵母表达载体pPIC9K连接,构建重组质粒pPIC9K/chit,转化毕赤酵母GS115,在甲醇的诱导下,成功地分泌出具生物活性的几丁质酶,诱导6d后酶活性达2.261U/mL,酶蛋白表达量为0.6mg/mL。该酶的最适反应温度和pH 值分别为60℃和5.5,该酶在50℃以下稳定;65℃的半衰期为40min。     

多拷贝毕赤酵母重组菌表达GCL摇瓶优化和高密度发酵

目的:构建高效表达白地霉脂肪酶的毕赤酵母重组菌株,并对筛选得到的菌株进行摇瓶发酵条件优化和分批补料高密度发酵工艺研究。方法:将诱导型表达载体pPIC9K-gcl电转化至毕赤酵母GS115。通过橄榄油-罗丹明B平板和摇瓶发酵筛选高脂肪酶活力的重组菌株,运用基于TaqMan探针的实时荧光定量PCR 法确定其拷贝数,并对菌株进行摇瓶发酵条件优化。在此基础上,研究重组菌在3L 发酵罐中的高密度发酵工艺。结果:筛选得到一株具有3 个白地霉脂肪酶基因拷贝的菌株GS115/pPIC9K-gcl 78#,初始酶活力为220 U/ml。当摇瓶发酵条件为甲醇诱导96 h,每24 h甲醇添加量1 %,接种量2 %,培养基初始pH 7.0,500 ml摇瓶装液量50 ml,甲醇诱导温度25℃ 时酶活力达735 U/ml。3L 发酵罐高密度发酵176.5 h,酶活力达到3360 U/ml,总蛋白含量达到4.30 g/L,且发酵过程中细胞活性一直保持在96 % 以上。结论:基因拷贝数与重组菌株的产酶水平呈正相关,摇瓶优化可显著提高重组菌株的产酶能力,为白地霉脂肪酶的工业化生产奠定了技术基础。     

重组人抗凝血酶发酵条件的优化

目的:通过实验室发酵条件优化工作,实现在巴斯德毕赤酵母中高效表达重组人抗凝血酶。方法:在摇瓶培养条件下,应用正交实验方法考查人抗凝血酶重组毕赤酵母菌pPIC9K-AT-02的培养温度、培养基pH值、接种比例、甲醇补加间隔时间及甲醇补加浓度等5种因素对重组人抗凝血酶活性的影响,确定最优发酵条件。结果与结论:筛选出的最终发酵条件为培养温度30℃、培养基pH6.0、接种比例20%、甲醇补加间隔时间24 h、甲醇补加浓度2%,重组人抗凝血酶在巴斯德毕赤酵母中表达活性为4098 U/L,比原始活性提高了150%。     

Production of butanol by Clostridium puniceum in batch and continuous culture

Summary The pink-pigmented, amylolytic and pectinolytic bacterium Clostridium puniceum in anaerobic batch culture at pH 5.5 and 25–30°C produced butan-1-ol as the major product of fermentation of glucose or starch. The alcohol was formed throughout the exponential phase of growth and surprisingly little acetone was simultaneously produced. Furthermore, acetic and butyric acids were only accumulated in low concentrations, and under optimal conditions were completely re-utilised before the fermentation ceased. Thus, in a minimal medium containing 4% w/v glucose as sole source of carbon and energy, after 65 h at 25°C, pH 5.5 all of the glucose had been consumed to yield (g product/100 g glucose utilised) butanol 32, acetone 3 and ethanol 2. Butanol was again the major product of glucose fermentation during phosphate-limited chemostat culture wherein, although the organism eventually lost its capacity to sporulate and to synthesize granulose, production of butanol continued for at least 100 volume changes. Under no growth condition was the organism capable of producing more than 13.3 g l^-1 of butanol. At pH 5.5, growth on pectin was slow and yielded a markedly lesser biomass concentration than when growth was on glucose or starch; acetic acid was the major fermentation product with lower concentrations of methanol, acetone, butanol and butyric acid. At pH 7, growth on all substrates produced virtually no solvents but high concentrations of both acetic and butyric acids.     

毕赤氏酵母工程菌高密度发酵表达恶性疟原虫融合抗原的研究

疟疾目前仍是危害人类健康的主要传染病,现全球每年新增疟疾病例3～5亿人,其中约300万人死于该病.特别是病原虫抗药性的产生和扩散已给疟疾防治工作带来极大困难,因此研制新的预防措施已成为当务之急.研制有效的疟疾疫苗被认为是人类控制乃至消灭疟疾的重要途径,已越来越受到重视,并已构建和鉴定多个疫苗候选抗原[1,2].本研究进行高密度优化表达的融合抗原就是一个疫苗候选抗原.     

Production and purification of extracellular chitinases from Penicillium aculeatum NRRL 2129 under solid-state fermentation

Fourteen Penicillium strains have been screened on wheat bran–crude chitin mixture medium for extracellular chitinase production in solid-state fermentation. Under the experimental conditions tested, Penicillium aculeatum NRRL 2129 (=ATCC 10409) was selected as the best enzyme producer. The optimum incubation period for chitinase production by the potent organism was found to be 72 h. Chromatofocusing was performed as the first step in the purification scheme, but high amount of contaminating proteins interfered with the method. Hence, ion-exchange chromatography experiments were carried out followed by gel filtration to separate and isolate chitinase isoenzymes. Four major chitinase peaks of molecular weight 82.7, 44.6, 28.2 and 26.9 kDa were observed after gel filtration chromatography while, on SDS-PAGE, three protein bands of molecular weights 82.6, 33.9 and 29.1 kDa were identified. The purified enzyme showed optimal temperature and pH at 50 and 5.5 °C, respectively.     

Influence of bioprocess variables on the production of extracellular chitinase under submerged fermentation by Streptomyces pratensis strain KLSL55

Chitinases are the enzymes which are capable of hydrolyzing chitin to its monomer N-acetyl glucosamine (GlcNac). Present study emphasizes on the impact of critical process variables on the production of chitinase from Streptomyces pratensis strain KLSL55. Initially the isolate was noticed to produce 84.67?IU chitinase in basal production medium. At optimization of bioprocess variables, the physical parameters pH of 8.00, 40?°C of incubation temperature, agitation speed of 160?rpm and 1.25?mL of spore suspension were found optimum for improved production of chitinase. Further, formulated production medium with 1.5% colloidal chitin, 1.25% fructose greatly influenced the chitinase production. At all described optimum conditions with formulated production media, a total of 14.30-fold increment was achieved in the chitinase production with final activity of 1210.67?IU when compared to the initial fermentation conditions in basal production medium.     

Hydrogen production conditions from food waste by dark fermentation with Clostridium beijerinckii KCTC 1785

The optimum conditions for biological hydrogen production from food waste by Clostridium beijerinckii KCTC 1875 were investigated. The optimum initial pH and fermentation temperature were 7.0 and 40°C, respectively. When the pH of fermentation was controlled to 5.5, a maximum amount of hydrogen could be obtained. Under these conditions, about 2,737 mL of hydrogen was produced from 50 g COD/L of food waste for 24 h, and the hydrogen content in the biogas was 38%. Hydrogen production rate and yield were about 108 mL/L·h and 128 mL/g COD_degraded, respectively. High concentrations of acetic (< 5,000 mg/L) or butyric acid (< 3,000 mg/L) significantly inhibited hydrogen production.     

以玉米秸秆为原料同步糖化发酵生产燃料乙醇

以玉米秸秆为原料,经酸法预处理后,采用同步糖化发酵SSF工艺生产燃料乙醇。正交试验获得的最佳体系为:培养温度34℃、发酵pH值5.5、发酵的液固比8:1、当发酵108h后,乙醇浓度可达8.33g/L。该实验为纤维质燃料乙醇的产业化生产提供技术依据。