点状产气单胞菌脯氨酰内肽酶基因的克隆与表达

用活性筛选法从产气单胞菌点状亚种ST7833 (Aeromonas puctata subsp.puctata ST7833)的基因组中克隆了脯氨酰内肽酶 (Prolyl Endopeptidase,简称apPEP)的基因,测定了含有PEP基因的33kb DNA片段的序列,第202092bp编码了690个氨基酸组成的脯氨酰内肽酶,经检索是一种新的PEP基因。并构建了一株组成性高效表达PEP的基因工程菌BL21/pGEMPEP。BL21/pGEMPEP在 YH培养基中apPEP的表达量占菌体总蛋白的30%左右,活力是野生菌的112倍,表达产物主要为可溶性的胞内蛋白,约5%分泌到胞外。非还原SDSPAGE显示为单体,分子量为76kD,与基因序列预测的分子量一致。试管培养后纯化得到了纯度大于90%的重组脯氨酰内肽酶,比活力为67U/mg。     

人肿瘤坏死因子及其突变体的基因工程下游工艺研究

研究了重组人肿瘤坏死因子(rhTNFα)及其突变体[Lys²]-人肿瘤坏死因子[Lys²]-rhTNFα)的基因工程下游工艺。rhTNFα和[Lys²]-rbTNFα的温控表达工程菌株在B-BTaunE 10型15L自控罐中经发酵每升可得50g湿菌体。rhTNFα和[Lys²]-rhTNFα的表达水平仍能保持在50％以上,且表达产物为可溶性蛋白。所得菌体经超声破菌、硫酸铵沉淀,然后依次用DEAE—Sepharose FF、CM-Sepharose FF和Sephacryl S-200柱层析进行分离纯化,由每升发酵液菌体最终可得1g左右的纯品,纯度达到98％左右,rhTNFα的比活为～1.5×10⁸IU／mg,[Lys²]－rhTNα的比活为～6×10⁸IU／mg。     

高密度培养大肠杆菌YK537/pSBHL11生产重组人细胞白介素-3

在B.Braun ES-10型15L和NBS BioFlo 3000型5L发酵罐中,利用补料分批培养技术高密度表达培养含重组质粒pSBHL-11的大肠杆菌YK537,生产重组人白细胞介素-3(IL-3),发现在发酵过程中,限制性流加甘油,控制溶解氧在30%～40％左右、30℃生长11h,42℃诱导培养4h,能将发酵液中最终菌体密度从OD₁₆600提高到OD₅₃600(相当于每升发酵液含106克湿菌体),并且保持了白细胞介素-3的表达量,占菌体总蛋白的30%左右,含量超过3.3%g/L,使IL-3包涵体产量从湿重2.2g/L提高到8.5 g/L,纯化步骤比较简单,超声破菌后经两次洗涤纯度就达到70%以上。     

脯氨酰内肽酶培养条件的优化及高密度发酵

基因工程菌E.coliBL21/pGEMPEP可以组成型表达重组的点状产气单胞菌脯氨酰内肽酶(PEP),但培养条件极大地影响着酶的产量,为了获得高效表达,首先测定了工程菌表达PEP的稳定性并考察了培养温度、pH、发酵时间、碳源、氮源、无机盐等对产酶的影响,得到了优化的发酵条件,L9(3⁴)正交试验进一步明确了摇床转速、培养温度、pH值、培养时间对产酶量的影响都有高度的统计学意义。在此基础上利用NBSBioFlo3000型5L自控发酵罐进行了高密度、高表达发酵、经20h培养,最终菌体密度达OD₆₀₀60(相当于干菌体225g/L),PEP表达量为28%,每升发酵液中含PEP酶315g。     

抗真菌肽LP-1的分离纯化及特性分析

拮抗菌枯草芽孢杆菌(\%Bacillus subtilis)\%TG\|26分泌产生的小肽经两次盐酸沉淀、丙酮分级沉淀和Hi\|pore反相柱两次纯化,分离得到一种新的抗真菌的小肽,命名为LP\|1。经MALDI\|TOF质谱鉴定,分子 量为10573,等电聚焦测得其pI为475。LP\|1对温度有较高的稳定性,100℃保温30min,仍能保持75%的活性。抑菌谱表明,该抗菌肽对瓜果腐霉\%(Pythium aphanidermatum)\,玉蜀黍赤霉病菌(Gibberella zeae)\,长柄链格孢(Alternaria longipe)和番茄蔫萎座镰孢霉(Fusarium oxysporum \%f.\%lycopersici)等植物病原真菌有很强的抑制作用。LP1可造成绿色木霉(Trichoderma viride)\%菌丝生长形态异常：菌丝端部膨大,菌丝扭曲,分支加剧,菌丝内细胞质分布不均匀,发生凝聚。茚三酮反应以及测序结果均证实其为环肽。     

嗜热毛壳菌内切β-葡聚糖酶的分离纯化及特性

探讨了液体发酵嗜热毛壳菌(Chaetomium thermophile)产生的内切β葡聚糖酶的分离纯化及特性。粗酶液经硫酸铵分级沉淀、DEAE\|Sepharose Fast Flow阴离子层析、Pheny1\|Sepharose疏水层析、Sephacry1 S\|100分子筛层析等步骤便可获得凝胶电泳均一的内切β\|葡聚糖酶。经125%SDS\|PAGE和凝胶过滤层析法分别测得所分离纯化酶蛋白的分子量约为67.8kD和69.8kD。该酶反应的最适温度和pH分别为60℃和40～45在pH50条件下,该酶在60℃下稳定;70℃保温1h后,仍保留30%的活性;在80℃的半衰期为25min。金属离子对内切β\|葡聚糖酶的活性影响较大,其中Na+对酶有激活作用;Fe2+、Ag+、Cu2+、Ba2+、Zn2+等对酶有抑制作用。该酶对结晶纤维素没有水解能力。     

50L规模中试发酵重组核苷二磷酸激酶A工程菌

中试规模发酵重组人核苷二磷酸激酶A（rhNDPK-A）工程菌,并对表达产物进行纯化。摇瓶培养一级种子至合适密度,以10%比例接种二级种子培养基,在7L发酵罐中培养至OD600为9.6～10.5,然后转入80L发酵罐中进行补料分批培养,所得菌体裂解后,经离子交换层析和亲和层析两步纯化得重组蛋白制品。结果表明,50L培养液经过10h培养后,湿菌收量为1560 g/批,NDPK-A表达量为23.8%。另外,补料方式对发酵密度有明显影响。与单纯补加碳源相比,同时补加碳源和氮源可以显著提高菌体产量,但对目的蛋白表达量地提高不明显。在较优条件下,菌体产量为(2220.00±169.71) g/批,蛋白表达量为(22.00±0.42) %,纯化后重组蛋白得率为510mg/L。产物可溶、密度适中、工艺简便的中试发酵条件的建立为高得率、大规模制备重组rhNDPK-A奠定了基础。     

绿色木霉MJ1产内切β-葡聚糖苷酶的分离纯化及酶学性质

利用KTAUPC-900快速蛋白液相色谱系统(FPLC)从绿色木霉MJ1固体发酵产物中分离纯化出内切β-葡聚糖苷酶。分离纯化后酶的比活力提高了28.6倍,回收率为19.7%。SDS-PAGE后经BIO-RAD凝胶成像系统分析该内切酶的分子量为64.7kD。酶学试验研究表明:该酶的最适反应温度53℃,最适pH为4.2,Lineweaver-Burk法求得动力学参数,K_m和V_max分别为1.230×10^{-2相似文献}   

离子注入花生四烯酸产生菌诱变选育

利用离子束注入生物技术对花生四烯酸产生菌(Mortierella alpina)进行诱变高产菌筛选。筛选到高产菌I₄₉N₁₈,该菌每升培养液可得生物量30.80g(约4%的含水量),干菌体油脂含量为25.8%,其中花生四烯酸的含量占总.脂的45.37%。30L和250L发酵罐发酵试验,该高产菌的花生.四烯酸得率为4.0g/L。     

尿酸氧化酶基因的克隆、表达及其产物的应用

克隆了产朊假丝酵母(Candida utilis)AS2-117尿酸氧化酶(Urate Oxidase,Uricase,EC1.7.3.3)的基因。将此基因插入原核表达质粒pET21a后转化大肠杆菌BL21(DE3),获得高表达的重组转化子菌株。经IPTG诱导,重组尿酸酶基因表达量可达菌体可溶性蛋白的40%。重组尿酸氧化酶为有酶活性的可溶蛋白。Western印迹分析证实表达产物有免疫学活性。经DEAE DE52纤维素离子交换柱层析纯化,目的蛋白纯度可达95%。重组蛋白和天然蛋白的理化特征比较证明重组蛋白的热稳定性有较大提高。酶盒配制和临床应用实验表明重组蛋白可代替天然蛋白进行临床血清尿酸的分析。     

Production of poly(3-hydroxybutyric acid) by fed-batch culture of Alcaligenes eutrophus with glucose concentration control

Alcaligenes eutrophus NCIMB 11599 was cultivated to produce poly(3-hydroxybutyric acid) (PHB) from glucose by the automatic fed-batch culture technique. The glucose concentration of the culture broth was controlled at 10 to 20 g/L by two methods: using exit gas data obtained from a mass spectrometer and using an on-line glucose analyzer. The effect of ammonium limitation on PHB synthesis at different culture phases was studied. The final cell concentration, PHB concentration, and PHB productivity increased as ammonia feeding was stopped at a higher cell concentration. High concentrations of PHB (121 g/L) and total cells (164 g/L) were obtained in 50 h when ammonia feeding was stopped at the cell concentration of 70 g/L. The maximum PHB content reached 76% of dry cell weight and the productivity was 2.42 g/L h with the yield of 0.3 g PHB/g glucose.     

2，3-丁二醇的发酵及盐析分离工艺

采用克雷伯氏菌（Klebsiella pneumoniae CICC 10011）发酵生产2,3-丁二醇,并对2,3-丁二醇的盐析分离工艺进行了考察。通过实验确定了以葡萄糖为底物微氧批式流加发酵的条件,发酵液中2,3-丁二醇和3-羟基丁酮的质量浓度分别为90．98g/L和12．40g/L,2,3-丁二醇的摩尔转化率为82．7％,生产强度达到2．1g/（L·h）。对发酵液中2,3-丁二醇的盐析分离研究表明,K2HPO4和K3PO4对2,3-丁二醇的盐析效果优于K2CO3。当发酵液浓缩70％后,加入质量分数为45％的K,HPO4,2,3-丁二醇的分配系数达到9．10,回收率为79．37％;上相中2,3-丁二醇的质量浓度达到420g／L;此时3-羟基丁酮的分配系数和回收率分别为11．9和83．48％。     

毕赤酵母发酵生产T4溶菌酶的中试研究

研究了T4溶菌酶的中试发酵放大生产。在200L发酵罐中毕赤酵母诱导表达T4溶菌酶蛋白,发酵液蛋白表达量达到1.69g/L,酶活达到192U/mg;制得冻干酶粉211.1g。经测定粗酶粉中T4溶菌酶的含量达到68.9%,酶活为182U/mg,总收率达到66%,成功建立了一条T4溶菌酶的中试发酵生产工艺线路。     

Interfacing Pichia pastoris cultivation with expanded bed adsorption

For improved interfacing of the Pichia pastoris fed-batch cultivation process with expanded bed adsorption (EBA) technique, a modified cultivation technique was developed. The modification included the reduction of the medium salt concentration, which was then kept constant by regulating the medium conductivity at low value (about 8 mS/cm) by salt feeding. Before loading, the low conductivity culture broth was diluted only to reduce viscosity, caused by high cell density. The concept was applied to a one-step recovery and purification procedure for a fusion protein composed of a cellulose-binding module (CBM) from Neocallimastix patriciarum cellulase 6A fused to lipase B from Candida antarctica (CALB). The modified cultivation technique resulted in lower cell death and consequently lower concentration of proteases and other contaminating proteins in the culture broth. Flow cytometry analysis showed 1% dead (propidium-stained) cells compared to 3.5% in the reference process. During the whole process of cultivation and recovery, no proteolysis was detected and in the end of the cultivation, the product constituted 87% of the total supernatant protein. The lipase activity in the culture supernatant increased at an almost constant rate up to a value corresponding to 2.2 g/L of CBM-CALB. In the EBA process, no cell-adsorbent interaction was detected but the cell density had to be reduced by a two-times dilution to keep a proper bed expansion. At flow velocity of 400 cm/h, the breakthrough capacity was 12.4 g/L, the product yield 98%, the concentration factor 3.6 times, the purity about 90%, and the productivity 2.1 g/L x h.     

天蓝色链霉菌海藻糖合酶的异源表达、活性分析及重组菌全细胞转化合成海藻糖的条件优化

从天蓝色链霉菌Streptomyces coelicolor克隆得到海藻糖合酶基因 (ScTreS),在大肠杆菌Escherichia coli BL21(DE3) 中进行了异源表达,通过 Ni-NTA 亲和柱对表达产物进行分离纯化得到纯酶,经 SDS-PAGE 测定其分子量约为62.3 kDa。研究其酶学性质发现该酶最适温度35 ℃;最适pH 7.0,对酸性条件比较敏感。通过同源建模和序列比对分析,对该基因进行定点突变。突变酶K246A比酶活比野生酶提高了1.43倍,突变酶A165T相对提高了1.39倍,海藻糖转化率分别提高了14%和10%。利用突变体重组菌K246A进行全细胞转化优化海藻糖的合成条件并放大进行5 L罐发酵,结果表明：在麦芽糖浓度300 g/L、初始反应温度和pH分别为35 ℃和7.0的条件下,转化率最高达到71.3%,产量为213.93 g/L;当底物浓度增加到700 g/L时,海藻糖产量仍可达到465.98 g/L。     

里氏木霉液体发酵产纤维素酶的研究

在摇瓶试验基础上,采用里氏木霉(Trichoderma reesei)HC-415菌株进行5L自控罐产纤维素酶深层发酵试验。在通气量为 0.2—0.6vvm、搅拌速度为 400r/min、发酵液pH控制在5.8—6.1的条件下,发酵液的羧甲基纤维素(CMC)酶酶活最高为325.0mg糖/ml,滤纸糖酶(FPA)酶活最高达17.9mg糖/ml。发酵周期为108h。所得冻干纤维素酶粉CMC酶活最高3111IU/g,FPA最高135IU/g ,对发酵液得率平均6.7g/L。酶活总收率CMC酶活平均78.2％,FPA酶活平均73.5％。     

以糙米为原料流加L-蛋氨酸的S-腺苷蛋氨酸发酵优化

研究了S-腺苷甲硫氨酸(SAM)高产菌啤酒酵母S-W55的廉价培养基及分批补料发酵过程优化.对啤酒酵母S-W55生长和SAM产量影响最为重要的糙米水解糖和酵母粉进行了响应面优化,得到了最优化的配方为糙米水解糖51.4g/L、酵母粉4.74g/L,此条件下啤酒酵母S-W55的SAM产量达2.61 g/L.不同分批补料发酵...     

Effect of nutritional factors on cellulase enzyme and microbial protein production by Aspergillus terreus and its evaluation

The biomass yield, cellulolytic activity, and protein recovery using Aspergillus terreus GN1 with alkali-treated sugarcane bagasse was studied using different levels (250-600 mg of N/L of broth) of organic and inorganic nitrogen sources. e.g., cattle urine, urea, cornsteep liquor, ammonium sulfate, ammonium nitrate, ammonium iron sulfate, ammonium chloride, and sodium nitrate. Among different levels of alkali-treated bagasse substrate concentrations (0.5-4.0% w/v) tested, 1.0% substrate yielded the highest crude protein content, protein recovery, and cellulolytic activity. The biomass recovery with 1.0% substrate ranged from 290-380 mg/500 mg bagasse substrate in a 50-mL broth with a nitrogen level of 250-600 mg of N/L in all the sources except ammonium iron sulfate, which yielded 402-439 mg/500 mg bagasse substrate. However, crude protein content of biomass obtained with an ammonium iron sulfate nitrogen source was the lowest. Cornsteep liquor nitrogen source at the rate of 600 mg of N/L yielded the maximum crude protein of 32.9%, protein recovery of 22.2 g/100 g of bagasse, and carboxymethyl cellulase and filter paper enzyme activities of 1.1 and 0.09 units/mL, among the organic and inorganic nitrogen sources studied. In general, the organic nitrogen sources and inorganic nonammonium nitrogen sources were utilized preferentially for protein production over the inorganic ammonium nitrogen sources. The fermentation time required under optimum cultural and nutritional conditions for A. terreus GN1 was also evaluated. The crude protein content of the biomass increased gradually up to the seventh day of fermentation, but the protein recovery rate was high up to two or three days. It was observed that the cellulose utilization rate increased after an initial lag of one day up to the third day and gradually increased further, which corresponded positively with protein content, biomass protein recovery, and cellulase enzyme activity. On the seventh day of fermentation, the crude protein content, biomass protein recovery, water-soluble carbohydrate, bagasse cellulose utilization, CMCase, and FPase activities were 32.8%, 20.1 g/100 g of bagasse, 6.2%, 82.7%, 1.0. and 0.08 U/mL, respectively. The final biomass recovered contained 32.8% crude protein content and had an in vitro rumen digestibility (IVRD) coefficient of 68.8%. The biomass contained almost all the essential and nonessential amino acids and was comparable with FAO reference protein. It is concluded that a fermentation time of 72 h gave a faster rate of protein production of 16.9 g/100 g of bagasse with 69.8% bagasse cellulose utilization with 76.0% IVRD. and contained almost all the essential and nonessential amino acids.