SCX separation of recombinant thrombolytic protein from complex biological feeds

The purification of recombinant thrombolytic protein from a crude fermentation broth mixture was examined in strong cation exchange (SCX) Chromatographic system. SCX system was shown to exhibit unique selectivity for the recombinant protein broth mixture. While SCX system showed lower total binding capacity for the recombinant protein than Anti-body Exchange system, it showed sharper separation boundaries in both displacement and step gradient module. The research with the SCX indicated that this separating system could be successfully employed in the displacement mode using DEAE-dextran as the displacer.     

Optimized gene synthesis, expression and purification of active salivary plasminogen activator alpha2 (DSPAalpha2) of Desmodus rotundus in Pichia pastoris

Vampire bat salivary plasminogen activators (DSPAs) are thrombolytic agents that are under clinical investigation for the treatment of acute ischemic stroke. In this study, the synthetic active salivary plasminogen activator alpha2 (DSPAalpha2) gene optimized for the preferred codons of Pichia pastoris was assembled from 48 oligonucleotides, and cloned into the yeast expression vector pPIC9 with a strong enhancer from human cytomegalovirus (HCMV). This system achieved high expression of an active DSPAalpha2 in P. pastoris yeast GS115. Secreted active DSPAalpha2 recombinant protein was purified from broth supernatant by a simple one-step procedure on Sephadex chromatography and was confirmed by SDS-PAGE and Western blot analysis. ELISA showed that 2.5mg of recombinant protein could be obtained from 100-ml culture broth supernatant. The fibrinolytic activity of the recombinant DSPAalpha2 was 1.28 x 10(5)IU/mg.     

Extracellular production of human parathyroid hormone as a thioredoxin fusion form in Escherichia coli by chemical permeabilization combined with heat treatment

A pET system encoding the fusion protein gene of thioredoxin (Trx) and human parathyroid hormone (hPTH) was introduced into Escherichia coli BL21 (DE3). Recombinant Trx-hPTH fusion protein was expressed in soluble form in the cytoplasm of the E. coli transformant. To recover Trx-hPTH from the E. coli culture efficiently, a novel tactic was developed by adding Triton X-100 into the fermentation culture at the exponential growth phase of E. coli and by heat treatment of the culture at the end of the fermentation. A concentration of 1% (v/v) Triton X-100 was added into the culture at the same time as IPTG addition after optimization. Under these conditions, addition of Triton X-100 had little effect on the cell growth, but more than 75% of the total recombinant Trx-hPTH was released into the fermentation broth. Also, a much higher volumetric yield of recombinant Trx-hPTH could be obtained with protein release compared to yield without protein release. Simultaneously, owing to the highly thermal stability of Trx-hPTH fusion protein, heat treatment of the fermentation broth at 80 degrees C for 15 min at the end of fermentation was employed for primary purification. Results demonstrated that heat treatment not only boosted further release of the recombinant Trx-hPTH fusion protein into the fermentation broth but also precipitated/denatured most of the nontarget proteins released in the broth. The tactics described herein integrated the fermentation process with subsequent recovery steps and thus provided a valuable and economical method for the production of Trx-hPTH and maybe some other Trx fusions in E. coli.     

High density fermentation and activity of a recombinant lumbrokinase (PI239) from Pichia pastoris

A system for the expression of recombinant lumbrokinase (rPI239) was developed in the yeast Pichia pastoris. A total supernatant protein content of 0.174 g/L of high density fermentation broth was obtained. The rPI239 exhibited in vitro fibrinolytic activity. The in vivo activity of rPI239 was measured by prothrombin time, kaolin part thrombin time, thrombin time, and fibrinolytic activity. This work presents the high-density fermentation of rPI239 from P. pastoris and shows that the recombinant protein has similar fibrinolytic activity both in vivo and in vitro.     

Using a two species competitive binding model to predict expanded bed breakthrough of a recombinant protein expressed in a high cell density fermentation

Expanded Bed experiments were conducted using a mixed mode (MM) resin to capture and purify a recombinant protein produced in yeast fermentation. Expanded bed breakthrough profiles show an overshoot in column effluent concentration of the target protein in the presence of cells and other broth proteins, similar to that seen by other researchers when loading two competing species onto packed beds. In this research, a numerical model assuming negligible axial dispersion is developed and first validated for columns loads that contain only the target protein. This model is solved by finite differences in a unique way that uses an embedded analytical-solution to increase solution speed and stability. To model expanded bed breakthrough of the target protein in the actual cell broth, it was assumed that the other non-product proteins in the broth compete for MM resin binding sites and might be represented as a second “average” species via a traditional two-component competitive Langmuir isotherm. Estimates of the Langmuir constant and broth concentration of this second species were then calculated from batch adsorption data. Using these parameters for the second species, and other batch-derived parameters for the target protein with this resin, this unique numerical modeling approach provided results that compare favorably to experimental breakthrough data at various flow rates. Finally, the model was employed for a parameter sensitivity analysis that shows which process variables are most important in determining breakthrough time and the shape and magnitude of the concentration overshoot.     

Isolation of recombinant proteins from culture broth by co‐precipitation with an amino acid carrier to form stable dry powders

Protein‐coated microcrystals can be generated by co‐precipitation of protein and a water‐soluble crystalline carrier by addition to excess water miscible organic solvent. We have investigated this novel process for its utility in the concentration and partial purification of a recombinant protein exported into the culture broth during expression by Pichia pastoris. Co‐precipitation with a L ‐glutamine carrier selectively isolated the protein content of the culture broth, with a minimal number of steps, and simultaneously removed contaminants including a novel yeast metabolite. This pigment co‐elutes during aqueous chromatography but its elucidation as a benzoylated glycosamine suggested a simple route of removal by partition during the co‐precipitation process. Scale‐up of the process was readily achieved through in‐line mixing and subsequent reconstitution of the dried protein‐coated microcrystals yielded natively folded, bioactive protein. Additional washing of the crystals with saturated L ‐glutamine facilitated further purification of the recombinant protein immobilized on the L ‐glutamine carrier. Thus, we present a novel method for the harvesting of recombinant protein from culture broth as a dry powder, which may be of general applicability to bioprocessing. Biotechnol. Bioeng. 2010;106: 764–773. © 2010 Wiley Periodicals, Inc.     

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

重组大肠杆菌高量表达重组人骨形态发生蛋白-7(rhBMP-7),每升培养液约得到湿菌体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;将包涵体溶解于高浓度变性剂溶液中,目的蛋白纯度提高到60％;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;用Western blot对目的蛋白进行特异性鉴定。     

毕赤酵母工程菌高密度发酵中氨态氮含量的测定

首次尝试将钠氏法应用于毕赤酵母高密度发酵中,并与靛酚蓝检测法进行了比较,证实钠氏法在0~10 mg/L的范围内,相关性好(r2=0.996 5),精确度(RSD=2.14%~5.32%)和精密度(Prec ision=97%~105%)高,更适合于毕赤酵母发酵中氨态氮含量的检测。并对其检测条件进行优化,确定检测波长为400 nm,最佳的显色反应为10 min。该方法用于毕赤酵母高密度发酵表达重组人血清白蛋白胸腺肽的结果表明,在发酵液氨基氮含量低于1.5 mg/kg,重组目的蛋白的表达出现了明显的降解,改善并控制发酵液中氨态氮的含量后,可以明显控制目的蛋白的降解,提高产品的产率。结果证实该方法用于发酵液中氨态氮的检测时,准确可靠,切实可行。     

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。     

The 5-enolpyruvylshikimate-3-phosphate synthase of glyphosate-tolerant soybean expressed in Escherichia coli shows no severe allergenicity

The recombinant gene was amplified from the chromosomal DNA of genetically-modified (GM) soybeans and identified as epsps encoding 5-enolpyruvylshikimate-3-phosphate synthase (EPSPS) which renders glyphosate resistance. The epsps structural gene was introduced in the pET28(a) plasmid for its expression in Escherichia coli BL21(DE3). It was confirmed that the maximal productivity of the EPSPS protein was achieved when cultivating the recombinant strain in a LB broth for 2 h after supplementing 1 mM isopropylbeta-D-thiogalactopyranoside (IPTG) in a 2 h-culture broth. Since the expressed EPSPS protein was found as an insoluble form in the inclusion body, it was extracted by 6 M urea after sonication, and then purified through immobilized nickel-affinity column chromatography to isolate EPSPS having a molecular mass of 57 kDa. When incubated in simulated gastric fluid containing pepsin at pH 1.5, the purified EPSPS protein was completely digested within 1 min. In addition, the passive cutaneous anaphylaxis reaction of the purified EPSPS protein was not observed in the Sprague Dawley rat system that was administered either orally or subcutaneously. Furthermore, treatment of the EPSPS protein to the culture of the sensitized peritoneal mast cells, or unsensitized but antisera-labeled mast cells, showed neither a remarkable change in the histamine release nor a cytokine production, including interleukin-4 (IL-4) and tumor necrosis factor-alpha (TNF-alpha). Thus, it can be concluded that the EPSPS protein in the GM soybean showed no significant allergenicity in the Sprague Dawley rats.     

Micellar Electrokinetic Capillary Chromatography of Proteins

Separations of model proteins obtained under denaturing conditions in the presence of micellar concentrations of ionic surfactants displayed high resolution and efficiency using either bare silica or C18-derivatized silica capillaries. Superior migration time reproducibility was achieved through the use of the C18-derivatized capillaries (run-to-run migration time % RSD = 0.2), relative to that obtained in bare silica capillaries (run-to-run migration time % RSD = 2.2), in the absence of buffer replenishment. The effects of surfactant concentration and pH upon the separation of a mixture of five model proteins of varying ionic and hydrophobic character were investigated, and the application of this technique to the analysis of a recombinant DNA-derived protein in fermentation broth was demonstrated.     

Recombinant enterokinase light chain with affinity tag: expression from Saccharomyces cerevisiae and its utilities in fusion protein technology.

Enterokinase and recombinant enterokinase light chain (rEK(L)) have been used widely to cleave fusion proteins with the target sequence of (Asp)(4)-Lys. In this work, we show that their utility as a site-specific cleavage agent is compromised by sporadic cleavage at other sites, albeit at low levels. Further degradation of the fusion protein in cleavage reaction is due to an intrinsic broad specificity of the enzyme rather than to the presence of contaminating proteases. To offer facilitated purification from fermentation broth and efficient removal of rEK(L) after cleavage reaction, thus minimizing unwanted cleavage of target protein, histidine affinity tag was introduced into rEK(L). Utilizing the secretion enhancer peptide derived from the human interleukin 1 beta, the recombinant EK(L) was expressed in Saccharomyces cerevisiae and efficiently secreted into culture medium. The C-terminal His-tagged EK(L) was purified in a single-step procedure on nickel affinity chromatography. It retained full enzymatic activity similar to that of EK(L), whereas the N-terminal His-tagged EK(L) was neither efficiently purified nor had any enzymatic activity. After cleavage reaction of fusion protein, the C-terminal His-tagged EK(L) was efficiently removed from the reaction mixture by a single passage through nickel-NTA spin column. The simple affinity tag renders rEK(L) extremely useful for purification, post-cleavage removal, recovery, and recycling and will broaden the utility and the versatility of the enterokinase for the production of recombinant proteins.     

溶氧反馈分批补料高密度培养人骨形成蛋白-2工程菌

对表达人骨形成蛋白－2成熟肽的基因工程大肠杆菌E.coli DH5α/pDH-B2m在500mL摇瓶中进行了培养条件的摸索实验,并在此基础上扩大至NBS Bioflo IV20L发酵罐,利用溶氧反馈－分批补料培养技术：在培养过程中保持适当的溶解氧（40％）,以溶氧值在线反馈控制搅拌速度及流加补料培养基,使细菌保持适当的比生长率,成功地进行了工程菌的高密度培养,最终菌体密度达OD600＝57,每升干菌量22.8g,目的蛋白的表达量占细菌总蛋白的30％,人骨形成蛋白－2成熟肽的理论产率达到3.59g/L。     

Reduction of acetate accumulation in Escherichia coli cultures for increased recombinant protein production

The culture of Escherichia coli for the commercial production of recombinant proteins has increased significantly in recent years. The production of acetate as a byproduct retards cell growth, inhibits protein formation, and diverts carbon from biomass to protein product. Our approach to reducing acetate accumulation was to disable the phosphoenolpyruvate:sugar phosphotransferase system (PEP-PTS) by deleting the ptsHI operon in the wild-type E. coli strain GJT001. The mutation caused a severe reduction in growth rate and glucose uptake rate in glucose-supplemented M9 minimal medium, which confirmed the mutation, and eliminated acetate accumulation. The mutant strain (TC110) apparently metabolized glucose by a non-PTS mechanism that we are currently investigating, followed by phosphorylation by glucokinase. In complex medium such as 2xLB broth with 2% glucose, TC110 was able to grow quickly and still retained the phenotype of significantly reduced acetate accumulation (9.1+/-6.6 vs. 90.4+/-1.6mM in GJT001, P<0.05). The reduced acetate accumulation resulted in a significant improvement in final OD (23.5+/-0.7 in TC110 vs. 8.0+/-0.1 in GJT001, P<0.05). We tested the strains for the production of model recombinant proteins such as green fluorescent protein (GFP) and beta-galactosidase. TC110 had a 385-fold improvement in final volumetric productivity of GFP over GJT001 in shake flasks with 2xLB broth with 2% glucose. The distribution of GFP fluorescence in the cell population, as determined by flow cytometry, was much broader in GJT001 (coefficient of variation=466+/-35%) than in TC110 (coefficient of variation=55+/-1%). In corn steep liquor medium with 2% glucose, we observed a 28.5-fold improvement in final volumetric production of GFP in TC110 over GJT001. TC110 had a 7.5-fold improvement in final volumetric productivity of beta-galactosidase over GJT001 in 2xLB broth with 2% glucose medium. When tested in a batch bioreactor cultures with 2xLB broth with 2% glucose medium, the volumetric production of GFP by TC110 was 25-fold higher than that of GJT001. In summary, the ptsHI mutant of GJT001 resulted in reduced acetate accumulation, which led to significant improvements in recombinant protein production in batch bioreactors.     

Growth-associated synthesis of recombinant human glucagon and human growth hormone in high-cell-density cultures of Escherichia coli

Synthesis of two recombinant proteins (human glucagon and human growth hormone) was investigated in fed-batch cultures at high cell concentrations of recombinant Escherichia coli. The glucose-limited growth was achieved without accumulation of metabolic by-products and hence the cellular environment is presumed invariable during growth and recombinant protein synthesis. Via exponential feeding in the two-phase fed-batch operation, the specific cell growth rate was successfully controlled at the desired rates and the fed-batch mode employed is considered appropriate for examining the correlation between the specific growth rate and the efficiency of recombinant product formation in the recombinant E. coli strains. The two recombinant proteins were expressed as fusion proteins and the concentration in the culture broth was increased to 15 g fusion growth hormone l⁻¹ and 7 g fusion glucagon l⁻¹. The fusion growth hormone was initially expressed as soluble protein but seemed to be gradually aggregated into inclusion bodies as the expression level increased, whereas the synthesized fusion glucagon existed as a cytoplasmic soluble protein during the whole induction period. The stressful conditions of cultivation employed (i.e. high-cell-density cultivation at low growth rate) may induce the increased production of various host-derived chaperones and thereby enhance the folding efficiency of synthesized heterologous proteins. The synthesis of the recombinant fusion proteins was strongly growth-dependent and more efficient at a higher specific growth rate. The mechanism linking specific growth rate with recombinant protein productivity is likely to be related to the change in cellular ribosomal content. Received: 27 May 1997 / Received last revision: 31 October 1997 / Accepted: 21 November 1997     

Effect of cycle time on fungal morphology, broth rheology, and recombinant enzyme productivity during pulsed addition of limiting carbon source

For many years, high broth viscosity has remained a key challenge in large-scale filamentous fungal fermentations. In previous studies, we showed that broth viscosity could be reduced by pulsed addition of limiting carbon during fed-batch fermentation. The objective in this study was to determine how changing the frequency of pulsed substrate addition affects fungal morphology, broth rheology, and recombinant enzyme productivity. To accomplish this, a series of duplicate fed-batch fermentations were performed in 20-L fermentors with a recombinant glucoamylase producing strain of Aspergillus oryzae. The total cycle time for substrate pulsing was varied over a wide range (30-2,700 s), with substrate added only during the first 30% of each cycle. As a control, a fermentation was conducted with continuous substrate feeding, and in all fermentations the same total amount of substrate was added. Results show that the total biomass concentration remained relatively unaltered, while a substantial decrease in the mean projected area of fungal elements (i.e., average size) was observed with increasing cycle time. This led to reduced broth viscosity and increased oxygen uptake rate. However, high values of cycle time (i.e., 900-2,700 s) showed a significant increase in fungal conidia formation and significantly reduced recombinant enzyme productivity, suggesting that the fungi channeled substrate to storage compounds rather than to recombinant protein. In addition to explaining the effect of cycle time on fermentation performance, these results may aid in explaining the discrepancies observed on scale-up to larger fermentors.     

Direct chemical extraction of a recombinant viral coat protein from Escherichia coli at high cell density.

The release of protein and DNA from nonrecombinant E. coli JM101 and recombinant E. coli HMS174(DE3) expressing L1 (the major viral coat protein of human papillomavirus type 16) as an inclusion body was demonstrated at high cell density (OD(600) = 160). For the nonrecombinant strain, extraction efficiency decreased significantly as cell mass increased, with a high viscosity increase in the postextraction broth. A different dependence on cell concentration was observed for the recombinant strain, with total protein extraction efficiency exceeding 85% for both uninduced and induced cells. Almost complete release of the recombinant L1 protein was achieved at high cell concentration (OD(600) = 80 approximately 160) without the use of reducing agent. This greatly extends the concentration range for chemical extraction.     

丁醇合成途径关键酶基因在大肠杆菌中的克隆和表达

【目的】克隆丙酮丁醇梭状芽胞杆菌(Clostridium acetobutylicum)ATCC824丁醇合成途径关键酶基因,构建产丁醇的工程大肠杆菌。【方法】以C.acetobutylicum ATCC824基因组为模板,分别扩增丁醇合成途径关键酶基因thil,adhE2和BCS operon(crt-bcd-etfB-etfA-hbd)基因序列,构建BCS operon-adhE2-thil/pTrc99a/MG1655(pBAT)。重组菌E.coli pBAT采用0.1 mmol异丙基-β-硫代半乳糖苷(IPTG)诱导5 h,测定乙酰基转移酶(THL)、3-羟基丁酰辅酶A脱氢酶(HBD)、3-羟基丁酰辅酶A脱水酶(CRT)、丁酰辅酶A脱氢酶(BCD)、醛醇脱氢酶(BYDH/BDH)的酶活。并以该基因工程菌作为发酵菌种,采用好氧、厌氧和微好氧三种培养方式,检测丁醇产量。【结果】酶活测定结果显示:THL酶活达到0.160 U/mg protein,酶活力提高了近30倍;HBD酶活力提高了近5倍;CRT酶活达到1.53 U/mg protein,野生菌株无此酶活;BCD酶活力提高了32倍;BYDH/BDH酶活力无显著提高。3种发酵培养结果显示在微好氧和厌氧条件下,均有丁醇产生,且丁醇的最大产量约为84 mg/L。【结论】本实验通过构建产丁醇基因工程大肠杆菌,实现了丁醇关键酶基因在大肠杆菌中的活性表达以及发酵产丁醇,为发酵法生产丁醇开辟了一条新的途径。     

Efficient expression and purification of human interferon alpha2b in the methylotrophic yeast, Pichia pastoris

The human interferon alpha2b (hIFN-alpha2b) is the most widely used member of IFNalpha family, and it exerts many biological actions including broad-spectrum antiviral effects, inhibition of tumor cell proliferation and enhancement of immune functions. Herein, the cDNA coding for hIFN-alpha2b has been cloned into the secreting expression organism Pichia pastoris, and the high level expression of hIFN-alpha2b has been achieved. SDS-PAGE and Western blotting assays of culture broth from a methanol-induced expression strain demonstrated that recombinant hIFN-alpha2b, a 18.8 kDa protein, was secreted into the culture medium. The recombinant protein was purified to greater than 95% using Source Q ion exchange and Superdex 75 size-exclusion chromatography steps. Finally, 298 mg of the protein was obtained in high purity from 1l of the supernatant and its identity to hIFN-alpha2b was confirmed by NH(2)-terminal amino acid sequence analysis. The bioassay of the recombinant protein gave a specific activity of 1.9 x 10(9)IU/mg. Our results suggest that the P. pastoris expression system can be used to produce large quantities of fully functional hIFN-alpha2b for both research and industrial purpose.