离子交换色谱法对大肠杆菌表达的人重组骨形态发生蛋白-7的纯化

带有BMP 7基因的大肠杆菌可以用来高量表达重组的人骨形态发生蛋白 7。升温诱导表达后 ,每升培养液大约可得到菌体湿重 3g ,其中目的蛋白约占菌体总蛋白量的 40 %。裂解离心 ,用低浓度变性剂洗涤初步纯化包涵体 ,上清中无目的蛋白损失 ,目的蛋白纯度提高到 60 %,将包涵体溶解于高浓度变性剂溶液中 ,然后在不同条件下用离子交换色谱法对变性状态下的蛋白质进行纯化 ,绝大部分杂蛋白被除去 ,目的蛋白纯度达 95 %以上 ,改变条件 ,可以减少rhBMP 7损失。并做Westernblot对目的蛋白进行特异性鉴定。     

Pilot scale production of a recombinant human epidermal growth factor, secreted by Bacillus brevis, using expanded bed adsorption

Recombinant Bacillus brevis which carried an expression plasmid encoding the human epidermal growth factor (EGF) gene on a cryptic high-copy number plasmid, pHT926, extracellularly produced EGF in its biologically active form at a concentration of over 1.5 g L⁻¹ in the culture broth in a 30-L jar fermenter. The culture broth also contained some other EGF compounds, which mainly consisted of oligomeric and polymeric forms with disulfide bonds. We developed a simple purification method for EGF, without prior cell removal from the culture broth, comprising cation exchange expanded bed adsorption followed by ultrafiltration with UF 10 000 and 3000 membranes. The EGF compounds were efficiently separated from the EGF in its native form in the expanded bed adsorption step. With this purification method, only EGF in its native form was recovered from the culture broth, with a yield of nearly 80%, and 90% purity. This efficient and economic system has made it possible to use EGF as a pharmaceutical in the livestock industry. Received 10 June 1998/ Accepted in revised form 10 September 1998     

Production of glutamine synthetase in <Emphasis Type="Italic">Escherichia coli</Emphasis> using SUMO fusion partner and application to <Emphasis Type="SmallCaps">l</Emphasis>-glutamine synthesis

l-glutamine (Gln) is an important conditionally necessary amino acid in human body and potential demand in food or medicine industry is expected. High efficiency of l-Gln production by coupling genetic engineered bacterial glutamine synthetase (GS) with yeast alcoholic fermentation system has been developed. We report here first the application of small ubiquitin-related modifier (SUMO) fusion technology to the expression and purification of recombinant Bacillus subtilis GS. In order to obtain GS with high Gln-forming activity, safety and low cost for food and pharmaceutics industry, 0.1% (w/v) lactose was selected as inducer. The fusion protein was expressed in totally soluble form in E. coli, and expression was verified by SDS–PAGE and western blot analysis. The fusion protein was purified to 90% purity by nickel nitrilo-triacetic acid (Ni–NTA) resin chromatography with a yield of 625 mg per liter fermentation culture. After the SUMO/GS fusion protein was cleaved by the SUMO protease, the cleaved sample was reapplied to a Ni–NTA column. Finally, about 121 mg recombinant GS was obtained from 1 l fermentation culture with no less than 96% purity. The recombinant purified GS showed great transferase activity (23 U/mg), with 25 U recombinant GS in a 50 ml reaction system, a biosynthesis yield of 27.5 g/l l-Gln was detected by high pressure liquid chromatography (HPLC) or thin-layer chromatography. Thus, the application of SUMO technology to the expression and purification of GS potentially could be employed for the industrial production of l-Gln.     

Production of Bioactive γ-Glutamyl Transpeptidase in <Emphasis Type="Italic">Escherichia coli</Emphasis> Using SUMO Fusion Partner and Application of the Recombinant Enzyme to <Emphasis Type="SmallCaps">l</Emphasis>-Theanine Synthesis

The amino acid l-theanine (γ-glutamylethylamide) has potential important applications in the food and pharmaceutical industries and increased demand for this compound is expected. It is the major “umami” (good taste) component of tea and its favorable physiological effects on mammals have been reported. An enzymatic method for the synthesis of l-theanine involving recombinant Escherichia coli γ-glutamyltranspeptidase (GGT) has been developed. We report here the application of small ubiquitin-related modifier (SUMO) fusion technology to the expression and purification of recombinant Escherichia coli γ-GGT. In order to obtain γ-GGT with high theanine-forming activity, safety, and low cost for food and pharmaceutics industry, M9 (consisting of glycerol and inorganic salts) and 0.1% (w/v) lactose were selected as culture medium and inducer, respectively. The fusion protein was expressed in soluble form in E. coli, and expression was verified by SDS-PAGE and western blot analysis. The fusion protein was purified to 90% purity by nickel–nitrilotriacetic acid (Ni–NTA) resin chromatography with a yield of 115 mg per liter fermentation culture. After the SUMO/γ-GGT fusion protein was cleaved by the SUMO protease, the cleaved sample was reapplied to a Ni–NTA column. Finally, about 62 mg recombinant γ-GGT was obtained from 1 l fermentation culture with no less than 95% purity. The recombinant γ-GGT showed great transpeptidase activity, with 1500 U of purified recombinant γ-GGT in a 1-l reaction system, a biosynthesis yield of 41 g of l-theanine was detected by paper chromatography or high pressure liquid chromatography (HPLC). Thus, the application of SUMO technology to the expression and purification of γ-GGT potentially could be employed for the industrial production of l-theanine.     

重组人肠激酶轻链的原核表达、纯化及活性分析

【目的】在原核表达系统中实现人肠激酶轻链(Human enterokinase light chain,hEKL)的表达和纯化。【方法】通过PCR扩增得到编码hEKL的基因片段,利用基因重组技术构建原核表达质粒pMAL-s-hEKL,在Escherichia coli中进行诱导表达,菌体经超声破碎后利用Amylose亲和柱对目标蛋白进行纯化,并利用Tricine SDS-PAGE检测酶的切割活性。【结果】目的基因能够以可溶形式表达,每升发酵液可纯化得到40 mg纯度在97%以上的MBP-hEKL蛋白,活性检测表明该酶可以对含有肠激酶识别序列的蛋白进行特异性切割,酶活力达到6.0×105U/mol。     

重组低出血抗凝蛋白在毕赤酵母中的中试发酵工艺研究及其纯化与鉴定

目的:通过对毕赤酵母中试发酵工艺的改进,建立一种简便可行的重组低出血抗凝蛋白(EH)的中试发酵工艺,为EH蛋白的放大生产研究奠定基础。方法:首先通过摇瓶培养绘测毕赤酵母工程菌的生长曲线,然后根据生长曲线,将对数生长期的菌种经过两级摇瓶培养放大后,直接接种到500 L的发酵罐中放大培养,通过发酵液的D600nm值、溶氧值(DO2)及菌体湿重动态监测细菌的生长状态,并用流加甲醇的方法诱导表达目的蛋白;表达上清经超滤、两步离子交换层析纯化获得目的蛋白;用非还原型SDS-PAGE和HPLC检测目的蛋白的纯度;用SDS-PAGE和质谱方法分析目的蛋白的相对分子质量;用Western印迹验证目的蛋白;用凝块法检测目的蛋白的抗凝活性。结果:发酵结束时,上清中蛋白含量达1.41 g/L,经后期分离纯化,得到约21 g EH蛋白,SDS-PAGE分析可见EH蛋白在还原状态下表观相对分子质量约为13.2×103±0.2×103,质谱分析相对分子质量约为7.3×103±0.73×103;Western印迹表明检测条带为目的蛋白,能被抗水蛭素抗体特异性结合;非还原型SDS-PAGE和HPLC测得EH蛋白的纯度均高于95%;凝块法检测EH蛋白的抗凝比活性为512~1024 ATU/mg。结论:建立了一条简便可行的EH蛋白的中试放大发酵生产工艺。     

Countercurrent tangential chromatography for large-scale protein purification

Recent advances in cell culture technology have created significant pressure on the downstream purification process, leading to a "downstream bottleneck" in the production of recombinant therapeutic proteins for the treatment of cancer, genetic disorders, and cardiovascular disease. Countercurrent tangential chromatography overcomes many of the limitations of conventional column chromatography by having the resin (in the form of a slurry) flow through a series of static mixers and hollow fiber membrane modules. The buffers used in the binding, washing, and elution steps flow countercurrent to the resin, enabling high-resolution separations while reducing the amount of buffer needed for protein purification. The results obtained in this study provide the first experimental demonstration of the feasibility of using countercurrent tangential chromatography for the separation of a model protein mixture containing bovine serum albumin and myoglobin using a commercially available anion exchange resin. Batch uptake/desorption experiments were used in combination with critical flux data for the hollow fiber filters to design the countercurrent tangential chromatography system. A two-stage batch separation yielded the purified target protein at >99% purity with 94% recovery. The results clearly demonstrate the potential of using countercurrent tangential chromatography for the large-scale purification of therapeutic proteins.     

Development of production and purification processes of recombinant fragment of pneumococcal surface protein A in <Emphasis Type="Italic">Escherichia coli</Emphasis> using different carbon sources and chromatography sequences

Pneumococcal surface protein A (PspA) is essential for Streptococcus pneumoniae virulence and its use either as a novel pneumococcal vaccine or as carrier in a conjugate vaccine would improve the protection and the coverage of the vaccine. Within this context, the development of scalable production and purification processes of His-tagged recombinant fragment of PspA from clade 3 (rfPspA3) in Escherichia coli BL21(DE3) was proposed. Fed-batch production was performed using chemically defined medium with glucose or glycerol as carbon source. Although the use of glycerol led to lower acetate production, the concentration of cells were similar at the end of both fed-batches, reaching high cell density of E. coli (62 g dry cell weight/L), and the rfPspA3 production was higher with glucose (3.48 g/L) than with glycerol (2.97 g/L). A study of downstream process was also carried out, including cell disruption and clarification steps. Normally, the first chromatography step for purification of His-tagged proteins is metal affinity. However, the purification design using anion exchange followed by metal affinity gave better results for rfPspA3 than the opposite sequence. Performing this new design of chromatography steps, rfPspA3 was obtained with 95.5% and 75.9% purity, respectively, from glucose and glycerol culture. Finally, after cation exchange chromatography, rfPspA3 purity reached 96.5% and 90.6%, respectively, from glucose and glycerol culture, and the protein was shown to have the expected alpha-helix secondary structure.     

Enhanced recovery of a secreted recombinant human growth factor using stabilizing additives and by co-expression of human serum albumin in the moss Physcomitrella patens

The production of pharmaceutical proteins in plants provides a valuable alternative to other traditional eukaryotic expression systems from economic and safety perspectives. The moss Physcomitrella patens allows the expression and secretion of complex target proteins into a simple aqueous maintenance medium, which facilitates downstream processing by rendering it less complex. To address the question of whether the addition of protein-stabilizing substances enhances the recovery of a target protein secreted into the culture medium, several additives at different concentrations were tested in a small-scale screening system. Although polyvinylpyrrolidone (PVP) and human serum albumin (HSA) showed a significant impact on protein levels, supplementation of the medium with these substances was accompanied by certain limitations in upstream processes, such as foam formation (HSA), and in downstream processes, such as reduced binding efficiency on chromatography columns (PVP), respectively. In order to reap the benefit of the enhancing effect and to avoid the given negative aspects, we developed a new strategy based on the recombinant expression of HSA in plants that are already capable of expressing a target protein. First, we analysed the expression and secretion of recombinant HSA in transiently and stably transformed wild-type (WT) plants. HSA was then co-expressed in Physcomitrella plants transgenic for human vascular endothelial growth factor (VEGF). Even with high expression levels of recombinant human VEGF (rhVEGF), the co-expression of recombinant HSA (rHSA) resulted in 48%-102% higher recovery of the target protein without concomitant negative effects on the upstream process. This strategy enables the enhanced recovery of target protein and does not require the addition of foreign components directly to the culture medium.     

Fermentative production of rhamnolipid and purification by adsorption chromatography

Glycolipids are one of the major classes of biosurfactants in which the rhamnolipids are best studied. The present work investigates the optimization of inoculum age and batch time for maximizing the yield of rhamnolipid from Pseudomonas aeruginosa (MTCC 2453). The yield and titer of rhamnolipids were maximum in the fermentation batch with an inoculum age of 24?hr. Batch time studies were performed on biomass production, rhamnolipid production, and sunflower oil utilization. The maximum yield of rhamnolipid was achieved at 96?hr when the culture cells were in the late exponential/early stationary phase. At optimum substrate concentration, maximum yield of 10.8?g/L was achieved. Further, downstream processing of crude rhamnolipid from broth using organic solvent extraction and subsequent purification using adsorption chromatography was done. In this study, chromatographic method was developed for purification of rhamnolipid by adsorption phenomena with more than 88.7% purity and 86.5% recovery. The present study provides new perspective on concepts involving separation by adsorption. Further antimicrobial properties and surfactant properties were studied for rhamnolipid production.     

Expression and functional characterization of a recombinant targeted toxin with an uPA cleavable linker in Pichia pastoris

A recombinant targeted toxin (Disintegrin-Conj-Mel) was developed that contained a disintegrin connected to cytotoxic melittin by a urokinase plasminogen activator (uPA)-cleavable linker. This recombinant targeted toxin was designed to target tumor cells expressing integrin αvβ3. The fusion gene was expressed under the control of the promoter AOX1 in Pichia pastoris. Electrophoresis by SDS-PAGE and Western blotting assays of culture broth from a methanol-induced expression strain, demonstrated that an approximately 13 kDa fusion protein was secreted into the culture medium. The molecular weight was that calculated from the predicted amino acid sequence. After optimizing the growth and expression conditions of the transformant strain, about 160 mg/L of the recombinant protein was achieved. The recombinant protein was purified to more than 95% purity by SP Sepharose ion exchange chromatography and Sephadex G-75 gel filtration chromatography. The hemolysis bioactivity test revealed that the fusion had no hemolytic activity or cytotoxicity against uPA non-expressing 293 cells, but exerted dose-dependent inhibition on uPA-expressing A549 cell proliferation.     

Establishment of a hyper-protein production system in submerged Aspergillus oryzae culture under tyrosinase-encoding gene (melO) promoter control

UV-mediated mutagenesis generated a high glucoamylase-producing mutant of Aspergillus oryzae exhibiting strong melanization in solid-state culture. Expression of the glucoamylase-encoding gene (glaB), which is specifically expressed in solid-state culture, and the tyrosinase-encoding gene (melO), was analyzed using an E. coli beta-glucuronidase (GUS) reporter assay to investigate this phenomenon. Although no common regulation was found for melO and glaB expression, the former was greatly enhanced in submerged culture. Interestingly, the melO promoter was about four times stronger for GUS production than the powerful promoters amyB, glaA, and modified agdA, previously isolated for industrial heterologous gene expression in A. oryzae. These findings indicated that the melO promoter would be suitable for hyper-production of heterologous protein in Aspergillus. The glaB-type glucoamylase selected as the target protein was produced in a submerged culture of A. oryzae under the control of the melO promoter. The maximum yield was 0.8 g/l broth, and the total extracellular protein purity was 99%. Repeated batch culture, to improve productivity, gave a maximum yield of 3.3 g/l broth. The importance of this work is in the establishment of a both high-level and high-purity protein overproduction system in A. oryzae by use of the melO promoter.     

Sodium gluconate production byAspergillus niger with intermittent broth replacement

Intermittent broth replacement was carried out to enhance the productivity and purity of sodium gluconate usingAspergillus niger by reducing the concentration of unmetabolized glucose. As inoculum size increased, length of lag phase was shortened and high initial production rate of sodium gluconate was achieved. However, too high inoculum concentration lowered productivity during the later stage of fermentation and increased residual glucose at the end of cultivation. When culture broth was replaced intermittently with distilled water, fresh medium, or recycled medium for comparison with traditional fermentation method, production of sodium gluconate was enhanced more than 1.5 fold and active production period could be prolonged without residual glucose. In addition, productivity was maintained at a level higher than 6 g/L/nr. Therefore, it was found that the reduction of biomass and viscosity by intermittent broth replacement could enhance the productivity.     

Integrated bioprocess for production of human proinsulin C-peptide via heat release of an intracellular heptameric fusion protein

An integrated bioprocess has been developed suitable for production of recombinant peptides using a gene multimerization strategy and site-specific cleavage of the resulting gene product. The process has been used for production in E. coli of the human proinsulin C-peptide via a fusion protein BB-C7 containing seven copies of the 31-residues C-peptide monomer. The fusion protein BB-C7 was expressed at high level, 1.8 g l(-1), as a soluble gene product in the cytoplasm. A heat treatment procedure efficiently released the BB-C7 fusion protein into the culture medium. This step also served as an initial purification step by precipitating the majority of the host cell proteins, resulting in a 70% purity of the BB-C7 fusion protein. Following cationic polyelectrolyte precipitation of the nucleic acids and anion exchange chromatography, native C-peptide monomers were obtained by enzymatic cleavage at flanking arginine residues. The released C-peptide material was further purified by reversed-phase chromatography and size exclusion chromatography. The overall yield of native C-peptide at a purity exceeding 99% was 400 mg l(-1) culture, corresponding to an overall recovery of 56%. The suitability of this process also for the production of other recombinant proteins is discussed.     

幽门螺旋杆菌重组尿素酶B亚基的纯化及其免疫学性质的研究

目的:幽门螺旋杆菌(Hp)尿素酶是Hp重要的定制因子和致病因子,Hp尿素酶活性位点位于Hp尿素酶B亚基(UreB),研发基于UreB的Hp疫苗是一种很有前景的防治Hp感染的策略。方法:主要利用基因克隆技术从幽门螺旋杆菌标准菌株SS1(Hp SS1)获得Hp尿素酶B亚基基因,并构建含有重组Hp尿素酶B亚基(rUreB)基因的重组表达载体pET-rUreB及其重组菌株;重组菌株经蛋白表达和优化后,利用Ni-NTP镍离子亲和层析和DEAE Sepharose FF阴离子交换层析纯化重组尿素酶B亚基(rUreB),并进一步通过腹腔注射免疫BALB/c小鼠,研究rUreB的免疫学性质。结果:通过基因克隆技术成功获得了Hp尿素酶B亚基基因,并成功构建了重组表达载体pET-rUreB及其重组菌株BL21(DE3)/pET-rUreB,经蛋白表达优化及纯化,可获得高纯度(96.5%)的重组蛋白rUreB。重组蛋白rUreB辅以弗氏佐剂腹腔注射免疫BALB/c小鼠,经间接ELISA鉴定小鼠能够产生针对天然Hp尿素酶和UreB的高滴度特异性抗体,且能够显著性抑制Hp尿素酶的活性。结论:重组Hp尿素酶B亚基能够在大肠杆菌表达系统中获得较高水平的表达,具有较高的免疫学特异性,其抗体能够有效抑制Hp尿素酶活性。为研究基于尿素酶的防治Hp感染的Hp疫苗奠定了一定的实验基础。     

Protein secretion in Corynebacterium glutamicum

Corynebacterium glutamicum, a Gram-positive bacterium, has been widely used for the industrial production of amino acids, such as glutamate and lysine, for decades. Due to several characteristics – its ability to secrete properly folded and functional target proteins into culture broth, its low levels of endogenous extracellular proteins and its lack of detectable extracellular hydrolytic enzyme activity – C. glutamicum is also a very favorable host cell for the secretory production of heterologous proteins, important enzymes, and pharmaceutical proteins. The target proteins are secreted into the culture medium, which has attractive advantages over the manufacturing process for inclusion of body expression – the simplified downstream purification process. The secretory process of proteins is complicated and energy consuming. There are two major secretory pathways in C. glutamicum, the Sec pathway and the Tat pathway, both have specific signal peptides that mediate the secretion of the target proteins. In the present review, we critically discuss recent progress in the secretory production of heterologous proteins and examine in depth the mechanisms of the protein translocation process in C. glutamicum. Some successful case studies of actual applications of this secretory expression host are also evaluated. Finally, the existing issues and solutions in using C. glutamicum as a host of secretory proteins are specifically addressed.     

Optimization of ectoine synthesis through fed-batch fermentation of Brevibacterium epidermis

A production process for ectoine has been developed, using Brevibacterium epidermis DSM20659 as the producer strain. First, the optimal conditions for intracellular synthesis of ectoine were determined. The size of the intracellular ectoine pool is shown to be dependent on the external salt concentration, type of carbon source, and yeast extract concentration. Under the optimized conditions of 1 M NaCl, 50 g/L monosodium glutamate, and 2.5 g/L yeast extract, a maximum concentration of intracellular ectoine of 0.9 g/L was obtained in shake flask cultures. After optimizing the batch fermentation parameters of temperature, pH, agitation, and aeration, the yield could be further increased by applying the fed-batch fermentation principle in 1.5- to 2-L fermentors. Glutamate and yeast extract were fed to the bacterial cells such that the total glutamate concentration in the broth remained constant. A total yield of 8 g ectoine/L fermentation broth was obtained with a productivity of 2 g ectoine/L/day. After the bacterial cells were harvested from the culture broth, the ectoine was recovered from them by a two-step extraction with water and ethanol. Crystallization of the product was obtained after concentration of the extract via evaporation under reduced pressure. After this downstream process, 55% of the ectoine produced in the fermentor could be crystallized in four fractions. The first fractions were of very high purity (98%). This production process can compete with other described production processes for ectoine in productivity and simplicity. Further advantages are the relatively low amounts of NaCl needed and the absence of hydroxyectoine, often a byproduct, in the final product.     

Improved process for production of recombinant yeast-derived monomeric human G-CSF

The human granulocyte colony-stimulating factor (hG-CSF) was efficiently secreted at high levels in fed-batch cultures of recombinant Saccharomyces cerevisiae. However, the secreted recombinant hG-CSF (rhG-CSF) was shown to exist as large multimers in the culture broth due to strong hydrophobic interaction. It was hardly monomerized even by urea at high concentration. This multimer has been reported to diminish specific receptor-binding activity of hG-CSF and causes undesirable problems in the downstream process. When the rhG-CSF was secreted to extracellular broth in the presence of a non-ionic surfactant (Tween 80) in the culture media, the multimerization of the secreted rhG-CSF was efficiently prevented in the fed-batch cultures. Also, the monomer fraction and secretion efficiency of rhG-CSF were significantly increased at the higher culture pH (6.5). Without using any denaturing agents, the secreted rhG-CSF monomer was easily purified with high recovery yield and purity via a simple purification process under acidic conditions, consisting of diafiltration, cation exchange, and gel filtration chromatography. A lyophilization process devoid of intermonomer aggregation was also designed using effective stabilizing agents. Received: 2 March 1999 / Received revision: 16 April 1999 / Accepted: 23 April 1999     

重组人纤溶酶原基因的酵母表达、产物纯化及鉴定

目的: 研究重组人纤溶酶原丝氨酸蛋白酶结构域（rhPLG-SP）的酵母表达、纯化及理化性质。 方法:采用7.5 L发酵罐对巴斯德毕赤酵母(Pichia pastoris)工程菌 rhPLG-SP/GS115 进行高密度培养、甲醇诱导表达rhPLG-SP,培养液经三步纯化：超滤、Sephacryl S-100、SP-Sepharose FF,将活性组分透析后冷冻干燥。等点聚焦电泳、HPLC、质谱分别检测 rhPLG-SP等电点、纯度和分子量;纤维蛋白平板、肽底物S-2403 分别测定 rhPLG-SP激活后的纤维蛋白溶解和酰胺水解活性。结果: 7.5 L高密度发酵可获得约为400mg/L培液的表达量,经三步纯化后制备的rhPLG-SP纯度大于96%。理化分析显示 rhPLG-SP的等电点为7.5~7.8,分子量：27 877 Da,比活性：23.6U/mg。结论: 初步建立了rhPLG-SP酵母工程菌的高密度培养、表达及纯化工艺,所制备半成品活性与血浆提取的PLG相近,具备放大生产和应用的潜力。     

Production of Taxol from Phyllosticta spinarum,an endophytic fungus of Cupressus sp.

Taxol production during the cultivation on a modified liquid and potato dextrose broth medium was indicated for the first time to occur in Phyllosticta spinarum, an endophytic fungus isolated from the needles of Cupressus sp. The presence of taxol in the fungal culture filtrate was confirmed by chromatographic and spectroscopic methods of analysis. The amount of taxol produced by this fungus was quantified by high performance liquid chromatography. The maximum amount of taxol production was obtained in this fungus when grown on M1D medium (235 μg/L) followed by PDB medium (125 μg/L). The results indicate that P. spinarum is an excellent candidate for taxol production . The production rate was 4.7 × 10³‐fold higher than that found in the culture broth of an earlier reported fungus, Taxomyces andreanae. The fungal taxol extracted also showed a strong cytotoxic activity in the in vitro culture of human cancer cells tested in an apoptotic assay.