Production of human serum albumin by sugar starvation induced promoter and rice cell culture

Human serum albumin (HSA) is the most widely used clinical serum protein. Currently, commercial HSA can only be obtained from human plasma, due to lack of commercially feasible recombinant protein expression systems. In this study, inducible expression and secretion of HSA by transformed rice suspension cell culture was established. Mature form of HSA was expressed under the control of the sucrose starvation-inducible rice α Amy3 promoter, and secretion of HSA into the culture medium was achieved by using the α Amy3 signal sequence. High concentrations of HSA were secreted into culture medium in a short time (2–4 days) by sucrose depletion after cell concentrations had reached a peak density in culture medium containing sucrose. The recombinant HSA had the same electrophoretic mobility as commercial HSA and was stable and free from apparent proteolysis in the culture medium. In a flask scale culture with repeated sucrose provision-depletion cycles, HSA was stably produced with yields up to 11.5% of total medium proteins or 15 mg/L per cycle after each sucrose provision-depletion cycle. A bubble column type bioreactor was designed for production of HSA. In the bioreactor scale culture, HSA was produced with yields up to 76.4 mg/L 4 days after sucrose depletion. HSA was purified from the culture medium to high purity by a simple purification scheme. Enrichment of HSA in culture medium simplifies downstream purification, minimizes protease degradation, and may reduce production cost. The combination of a DNA construct containing the α Amy3 promoter and signal sequence, and the use of a rice suspension cell culture can provide an effective system for the production of recombinant pharmaceutical proteins.     

Large-scale transient transfection of serum-free suspension-growing HEK293 EBNA1 cells: peptone additives improve cell growth and transfection efficiency

Large-scale transient transfection of mammalian cells is a recent and powerful technology for the fast production of milligram amounts of recombinant proteins (r-proteins). As many r-proteins used for therapeutic and structural studies are naturally secreted or engineered to be secreted, a cost-effective serum-free culture medium that allows their efficient expression and purification is required. In an attempt to design such a serum-free medium, the effect of nine protein hydrolysates on cell proliferation, transfection efficiency, and volumetric productivity was evaluated using green fluorescent protein (GFP) and human placental secreted alkaline phosphate (SEAP) as reporter genes. The suspension growing, serum-free adapted HEK293SF-3F6 cell line was stably transfected with an EBNA1-expression vector to increase protein expression when using EBV oriP bearing plasmids. Compared to our standard serum-free medium, concomitant addition of the gelatin peptone N3 and removal of BSA slightly enhanced transfection efficiency and significantly increased volumetric productivity fourfold. Using the optimized medium formulation, transfection efficiencies between 40-60% were routinely obtained and SEAP production reached 18 mg/L(-1). To date, we have successfully produced and purified over fifteen r-proteins from 1-14-L bioreactors using this serum-free system. As examples, we describe the scale-up of two secreted his-tagged r-proteins Tie-2 and Neuropilin-1 extracellular domains (ED) in bioreactors. Each protein was successfully purified to >95% purity following a single immobilized metal affinity chromatography (IMAC) step. In contrast, purification of Tie-2 and Neuropilin-1 produced in serum-containing medium was much less efficient. Thus, the use of our new serum-free EBNA1 cell line with peptone-enriched serum-free medium significantly improves protein expression compared to peptone-less medium, and significantly increases their purification efficiency compared to serum-containing medium. This eliminates labor-intensive and expensive chromatographic steps, and allows for the simple, reliable, and extremely fast production of milligram amounts of r-proteins within 5 days posttransfection.     

Expression and purification of sea raven type II antifreeze protein from Drosophila melanogaster S2 cells

We present a system for the expression and purification of recombinant sea raven type II antifreeze protein, a cysteine-rich, C-type lectin-like globular protein that has proved to be a difficult target for recombinant expression and purification. The cDNAs encoding the pro- and mature forms of the sea raven protein were cloned into a modified pMT Drosophila expression vector. These constructs produced N-terminally His(6)-tagged pro- and mature forms of the type II antifreeze protein under the control of a metallothionein promoter when transfected into Drosophila melanogaster S2 cells. Upon induction of stable cell lines the two proteins were expressed at high levels and secreted into the medium. The proteins were then purified from the cell medium in a simple and rapid protocol using immobilized metal affinity chromatography and specific protease cleavage by tobacco etch virus protease. The proteins demonstrated antifreeze activity indistinguishable from that of wild-type sea raven antifreeze protein purified from serum as illustrated by ice affinity purification, ice crystal morphology, and their ability to inhibit ice crystal growth. This expression and purification system gave yields of 95 mg/L of fully active mature sea raven type II AFP and 9.6 mg/L of the proprotein. This surpasses all previous attempts to express this protein in Escherichia coli, baculovirus-infected fall armyworm cells and Pichia pastoris and will provide sufficient protein for structural analysis.     

Expression and purification of hexahistidine-tagged human glutathione S-transferase P1-1 in Escherichia coli

The bacterial expression and purification of human pi class glutathione S-transferase (hGST P1-1) as a hexahistidine-tagged polypeptide was performed. The expression plasmid for hGST P1-1 was constructed by ligation of the cDNA which codes for the protein into the expression vector pET-15b. The expressed protein was purified by either glutathione or metal (Co(2+)) affinity column chromatography, which produced the pure and fully active enzyme in one step with a yield of more than 30 mg/liter culture. The activity of the purified protein was 130 units mg(-1) from the GSH affinity column and 112 units mg(-1) from the Co(2+) affinity column chromatography. The purity of the protein was assessed by electrospray ionization mass spectrometry and size-exclusion chromatography. It showed that the real molecular weight of the hexahistidine-tagged hGST P1-1 polypeptide chain agreed with the calculated value and that the purified protein eluted as an apparent homodimer on the gel filtration column. Our expression system allows the expression and purification of active hexahistidine-tagged hGST P1-1 in high yield with no need of removal of the hexahistidine tag and gives pure protein in one purification step allowing further study of this enzyme.     

Small-scale, semi-automated purification of eukaryotic proteins for structure determination

A simple approach that allows cost-effective automated purification of recombinant proteins in levels sufficient for functional characterization or structural studies is described. Studies with four human stem cell proteins, an engineered version of green fluorescent protein, and other proteins are included. The method combines an expression vector (pVP62K) that provides in vivo cleavage of an initial fusion protein, a factorial designed auto-induction medium that improves the performance of small-scale production, and rapid, automated metal affinity purification of His8-tagged proteins. For initial small-scale production screening, single colony transformants were grown overnight in 0.4 ml of auto-induction medium, produced proteins were purified using the Promega Maxwell 16, and purification results were analyzed by Caliper LC90 capillary electrophoresis. The yield of purified [U-15N]-His8-Tcl-1 was 7.5 microg/ml of culture medium, of purified [U-15N]-His8-GFP was 68 microg/ml, and of purified selenomethione-labeled AIA-GFP (His8 removed by treatment with TEV protease) was 172 microg/ml. The yield information obtained from a successful automated purification from 0.4 ml was used to inform the decision to scale-up for a second meso-scale (10-50 ml) cell growth and automated purification. 1H-15N NMR HSQC spectra of His8-Tcl-1 and of His8-GFP prepared from 50 ml cultures showed excellent chemical shift dispersion, consistent with well folded states in solution suitable for structure determination. Moreover, AIA-GFP obtained by proteolytic removal of the His8 tag was subjected to crystallization screening, and yielded crystals under several conditions. Single crystals were subsequently produced and optimized by the hanging drop method. The structure was solved by molecular replacement at a resolution of 1.7 A. This approach provides an efficient way to carry out several key target screening steps that are essential for successful operation of proteomics pipelines with eukaryotic proteins: examination of total expression, determination of proteolysis of fusion tags, quantification of the yield of purified protein, and suitability for structure determination.     

重组黄杆菌肝素酶Ⅲ的纯化、表征及培养条件对酶生产的影响

肝素酶Ⅲ是一种特异性地裂解乙酰肝素的酶,在大肠杆菌中表达时容易形成包涵体.为实现肝素酶Ⅲ的可溶性表达,利用谷胱甘肽-S-转移酶(GST)与肝素酶Ⅲ融合性能,通过构建相应的表达质粒pGEX-heparinaseⅢ,在大肠杆菌中实现了肝素酶Ⅲ的可溶性表达.粗酶通过一步亲和纯化其纯度可达95%以上.通过对LB培养基摇瓶培养Escherichia coli BL21的诱导时机,诱导剂用量、诱导时间等培养条件的优化,确定了该可溶性肝素酶Ⅲ融合蛋白的最适生产条件.通过对纯酶的最适反应温度、pH、Ca~(2+)浓度等一系列性质研究,确定了该酶的最适反应条件.     

N-糖酰胺酶F在大肠杆菌中的高效表达及其脱糖基化作用研究

从脑膜炎脓杆菌（Flavobacterium meningosepticum）基因组中通过PCR扩增了N-糖酰胺酶F（PNGase F）基因,经酶切后与表达载体pET28a连接,获得的重组质粒转入大肠杆菌BL21(DE3)。重组大肠杆菌经诱导表达和纯化提取后,获取大量高纯度N-糖酰胺酶F,其纯度达90%以上。试验证明,经纯化的重组N-糖酰胺酶F可以切除核糖核酸酶B、转铁蛋白和人IgG等糖蛋白上的N-糖链,具有脱糖基化作用。     

蛇毒锯鳞蝰素融合蛋白的发酵与纯化

研究大肠杆菌表达重组蛇毒锯鳞蝰素(Echistatin,Ecs)融合蛋白的发酵和纯化工艺。将Ecs基因插入表达载体pTXB1,转化E.coliBL21(DE3)构建工程菌。对工程菌进行补料分批培养并诱导表达,研究培养基、培养和诱导时间对工程菌生长和目的蛋白表达的影响,几丁质亲和层析纯化Ecs融合蛋白,经DTT裂解后,检测Ecs活性。发酵后菌体湿重可达75g/L,融合蛋白表达量约占总蛋白的35%,重组质粒在BL21宿主菌中传代稳定。亲和层析纯化后,得到Ecs单体,得率为28mg/L发酵液。生物学活性分析显示,重组Ecs能有效抑制血小板的聚集,其活性与天然Ecs相似。优化了Ecs融合基因工程菌的发酵和纯化条件,为规模化生产奠定基础。     

High-level expression of biologically active human prolactin from recombinant baculovirus in insect cells

We examined the feasibility of high-level production of recombinant human prolactin, a multifunctional protein hormone, in insect cells using a baculovirus expression system. The human prolactin cDNA with and without the secretory signal sequence was cloned into pFastBac1 baculovirus vector under the control of polyhedrin promoter. Prolactin was produced upon infection of either Sf9 or High-Five cells with the recombinant baculovirus containing the human prolactin cDNA. The production of recombinant prolactin varied from 20 to 40 mg/L of monolayer culture, depending on the cell types. The prolactin polypeptide with its own secretory signal was secreted into the medium. N-terminal amino acid sequence analysis of the recombinant polypeptide purified from the culture medium indicated that the protein was processed similar to human pituitary prolactin. Carbohydrate analysis of the purified protein indicated that a fraction of the recombinant prolactin made in insect cells appeared to be glycosylated. Also, both secreted and nonsecreted forms of the recombinant prolactin in insect cells were biologically equivalent to the native human prolactin (pituitary derived) in the Nb2 lymphoma cell proliferation assay.     

Secretory production system of bionanocapsules using a stably transfected insect cell line

Bionanocapsules (BNCs) are hollow nanoscale particles composed of L protein of the hepatitis B virus surface antigen that represent specific affinity for human hepatocytes. BNCs can transfer genes and drugs into human hepatocytes efficiently and specifically. BNC can be expressed in yeast cells. In this study, we developed a new L particle production system using a stably transfected insect cell line. For this purpose, we established a host–vector system using the Trichoplusia ni insect cell line. L particles were efficiently secreted by the overexpression of the L protein, which was fused to the secretion signal peptide. The concentration of L particles was reached approximately 1.7 μg/ml in 5 days during cultivation in a serum-free medium without antibiotic selective pressure. The production of L particles was maintained for at least 75 days. The secretory production of L particles facilitated their easy purification by chromatography. Furthermore, it was demonstrated that purified L particles can transfect only human hepatocytes. Therefore, an insect cell expression system is an attractive tool for the production of BNC.     

Recombinant expression, isotope labeling, refolding, and purification of an antimicrobial peptide, piscidin

An antimicrobial peptide, piscidin, was overexpressed as a fused form with the ubiquitin molecule in Escherichia coli, and the fusion protein was purified using immobilized metal affinity chromatography (IMAC). The peptide was released from its fusion partner by using yeast ubiquitin hydrolase (YUH), and subsequently purified by reverse phase chromatography. The expression and purification process of piscidin encountered several problems such as the lysis of the bacterial cell upon induction of the peptide production, the unwanted cleavage of the fusion protein inside the bacterial cell, and high tendency to aggregate in the aqueous environment. Such problems were alleviated by employing ubiquitin as a fusion partner for piscidin, growing the cells at a lower temperature, and changing the order of the purification steps. The yields of the fusion protein and the peptide were around 15 and 1.5 mg per liter of LB or minimal medium, respectively. The recombinant expression and purification of piscidin will enable its structural and dynamic studies using multidimensional NMR spectroscopy.     

High-level expression of recombinant Fc chimeric proteins in suspension cultures of stably transfected J558L cells

Recombinant Fc chimeric proteins are useful tools for studying protein function, including the analysis of molecular interactions by techniques such as expression cloning. Here we describe a method we have used to express the IgLON family proteins, CEPU1 and OBCAM, as recombinant Fc chimeric proteins in stably transfected mouse J558L myeloma cells. The use of this cell line provided the opportunity to maximize protein production, as it secretes antibodies in large quantities and can be grown to high density in small volumes of culture medium. Isolation of recombinant OBCAMFc from the adherent COS7 cell line suggested a minimum level of expression of 0.07 mg OBCAMFc/100 mL culture medium, while the J558L cell line expressed OBCAMFc at approximately 11.4 mg/100 mL culture medium. Purification of IgLON-Fc expressed by J558L cells was simpler than purification from COS7 cells because of the lower volume of culture medium generated. Furthermore, contamination of J558L expressed IgLONFc with bovine IgG from the culture medium was negligible. The method presented, which utilizes a commercially available small-scale bioreactor, provides the nonspecialist protein expression laboratory with the means to produce recombinant proteins quickly and easily in milligram quantities.     

Optimum conditions for production and purification of human papillomavirus type 16 L1 protein from Saccharomyces cerevisiae

Several prophylactic human papillomavirus (HPV) vaccines have been developed based on virus-like particles (VLPs) made from viral L1 proteins. A substantial number of VLPs is necessary for biochemical characterization and diagnostic test development. To establish the optimum conditions for production and purification of HPV L1 in the yeast expression system we varied the amount and nature of the carbon source and evaluated HPV 16 L1 recovery by three purification methods. Maximally threefold more HPV 16 L1 was produced with a 4% carbon source than with a 2% carbon source. In addition, the productivity of HPV 16 L1 varied by 25% depending on the combination of glucose and galactose in the 4% carbon source. We introduced an ammonium sulfate precipitation step in place of the ultracentrifugation using a sucrose cushion routinely used for HPV L1 purification, and optimized the purification by cation-exchange chromatography. Overall L1 protein recovery using the ammonium sulfate precipitation method was 30%, the highest recovery achieved so far. The purified HPV 16 L1 protein successfully self-assembled into VLPs. Purification by ammonium sulfate precipitation was maximally 15 times greater than ultracentrifugation on a sucrose cushion. We anticipate that our procedures for production and purification will reduce the cost, time and labor involved in obtaining sufficient yields of VLPs.     

Single-Step Purification and Biological Activity of Human Nerve Growth Factor Produced from Insect Cells

Human nerve growth factor (NGF) was cloned and engineered for expression in a baculovirus-infected Spodoptera frugiperda (SF-9) insect cell system. Culture supernatants contained 2-3 mg/L of recombinant human NGF. The human NGF produced by this system was purified to apparent homogeneity with a single-step affinity chromatography procedure using a high-affinity monoclonal antibody originally raised against murine NGF. The purification procedure yielded 1-2 mg of pure, human NGF per liter of culture supernatant; i.e., approximately 60% recovery of the human NGF originally released into the culture medium. Although the gene transfected into the SF-9 cells coded for pro-NGF, the NGF recovered after purification was greater than 95% fully processed, mature protein. The KD for the affinity of the pure, recombinant human NGF for NGF receptor in PC12 membranes is 0.20 +/- 0.05 nM. Activation of neurite outgrowth in PC12 cells occurs with ED50 values of 85 +/- 20 pM and 9.6 +/- 1.5 pM for a 3-day primary response and a 1-day secondary response, respectively. The pure, recombinant human NGF also stimulates a significant increase in dopamine content of PC12 cells with an ED50 of 5.8 +/- 2.7 pM. These binding and biological activation properties are consistent with values observed using murine NGF purified from submaxillary glands.     

High-density transient gene expression in suspension-adapted 293 EBNA1 cells

Large-scale transient gene expression (TGE) in mammalian cells is an attractive method to rapidly produce recombinant proteins for pre-clinical studies, with some processes reported to reach 100 L. However, the yield remains low, hardly over 20 mg protein/L, mainly because the current TGEs have been performed at low cell density (approximately 5 x 10(5) cells/mL). In this study, the strategy to improve TGE focuses on facilitating transfection at high cell density. A high-density perfusion culture of 293 EBNA1 cells was established in 2-L bioreactor using Freestyle 293 expression medium (Invitrogen, Singapore) to grow the cells for transfection. Transfection was then carried out at 1 x 10(7) cells/mL using polyethylenimine (PEI) as DNA carrier, at the optimized conditions of 6 microg DNA/10(7) cells and 1:3 DNA to PEI mass ratio. During the post-transfection phase, 80.8 mg/L of the model protein, EPO was obtained at day 5.5 post-transfection (130 mg total EPO production) using a fed-batch culture mode. In comparison, perfusion cultures using an enriched SFM II medium resulted in a longer post-transfection production phase (8 days), and 227 mg of EPO was produced in 10.7 L medium, showing that high-density TGE enables the production of several hundreds of milligrams of protein in a 2 L bioreactor. In addition, a protocol for economical plasmid preparation based on anion exchange was also established to satisfy TGE's demand in terms of quality and quantity. To the best of our knowledge, this is the first report of transient transfections at a high cell density of up to 1 x 10(7) cells/mL.     

An efficient heat-inducible Bacillus subtilis bacteriophage 105 expression and secretion system for the production of the Streptomyces clavuligerus beta-lactamase inhibitory protein (BLIP)

The Streptomyces clavuligerus beta-lactamase inhibitory protein (BLIP) has been shown to be a potent inhibitor of class A beta-lactamases including the Escherichia coli TEM-1 beta-lactamase (Ki = 0.6 nM). A heat-inducible BLIP expression system was constructed based on a derivative of Bacillus subtilis phage phi105. The recombinant BLIP produced by this system was secreted to the culture medium, purified to homogeneity, and fully active. We have shown that the signal peptide of BLIP functions well in B. subtilis to secrete BLIP out of the cells, which facilitates purification. The absence of a His-tag also avoids the activity and structure of BLIP being altered. An unprecedented high yield of recoverable protein in culture supernatant (3.6mg of >95% pure BLIP/l culture) was achieved by a simple purification protocol. We have developed an efficient production process in which the culture time before heat-induction was 3-4h and the culture supernatant could be collected 5h after induction. This total time of 8-9h is considered to be very short compared to that of the native S. clavuligerus culturing (60-70h). We achieved a very efficient BLIP production rate of 0.8-0.9mg/l/h. Heterologous gene expression was tightly controlled and no production of BLIP was observed before heat-induction, suggesting that cell density can be further increased to improve enzyme yield.     

球孢白僵菌丝氨酸蛋白酶基因CDEP-1在毕赤酵母中的表达

我们从球孢白僵菌中克隆了丝氨酸蛋白酶Pr1类基因CDEP-1。为明确CDEP-1的功能、评价其在害虫生物防治中的潜力,需要大量制备具有生物活性的CDEP-1编码蛋白。由于大肠杆菌系统表达真核基因存在产物复性困难的问题,本文利用毕赤酵母系统来表达CDEP-1。结果表明,CDEP-1可在毕赤酵母中高效的分泌表达,而且产物活性高,甲醇诱导48h后上清液中的酶活即可达到38,266U/L。诱导表达的上清液经浓缩后进行凝胶过滤层析,得到了CDEP-1的初纯品,蛋白质含量为50mg/L。将纯化的蛋白酶CDEP-1免疫家兔,制备了CDEP-1的抗血清。Westernblotting分析表明,制备的抗血清可特异性地检测CDEP-1。     

Expression and characterization of human glycosylated interleukin-1 receptor antagonist in Pichia pastoris

Interleukin-1 receptor antagonist is an inhibitor of the pro-inflammatory action of interleukin-1. The gene encoding for interleukin-1 receptor antagonist (IL-1ra) was cloned into a Pichia pastoris expression vector pPICzalphaA (Invitrogen, USA) and transformed into P. pastoris strain SMD1168H. Multi-copy selection of the gene produced a high expressing strain of IL-1ra that produced 17mg/L of total secreted purified protein. The IL-1ra produced in P. pastoris was a mixture of glycosylated and non-glycosylated IL-1ra where 70% of the total protein was glycosylated. SP-Sepharose purification allowed for separation of the two expressed forms of IL-1ra, which permits biochemical investigation of glycosylated and non-glycosylated IL-1ra using one expression system. Mass spectrometric analysis revealed the expression of the full-length protein and that the glycosylated IL-1ra contained high mannose glycoforms that ranged from Man(9)GlcNAc(2) to Man(14)GlcNAc(2).