The purification of IgY from chicken egg yolk by preparative electrophoresis

Chicken IgY has been purified from egg yolk by preparative electrophoresis on the Gradiflow, a system which has been employed for the purification of a wide range of proteins with high recovery and biological activity. Protein purification on the Gradiflow utilises electrophoresis with selected combinations of porous membranes and buffers. The purification of IgY was achieved by initial PEG lipid precipitation, then a single step Gradiflow run by a strategy based on the relatively high pI range of IgY compared to other egg yolk proteins. The IgY yields obtained from the delipidised supernatant are consistently greater than 80% by immunoassay. The purity of the IgY fraction compared favourably with IgY prepared using three commercial products.     

大肠杆菌表达重组人生长激素的纯化

目的 :获得具有生物学活性的重组人生长激素 (rhGH)。方法 :PBV -GH/DH5α菌体经超声破菌、反复洗涤后获得包涵体。将包涵体变性、复性 ,用硫酸铵盐析 ,离子交换层析和凝胶层析进行纯化。产物经SDS -PAGE、HPLC、N末端 15个氨基酸序列检测验证。结果 :终产物rhGH纯度达 98.2 % ,比活性大于 3.0IU/mg。分子量为 2 2kDa ,N末端氨基酸序列与DNA序列推导的氨基酸序列完全一致。结论 :从自构建的PBV -GH/DH5α工程菌中获得高纯度、高活性重组人生长激素。其纯化工艺为中试生产提供可靠依据。     

Novel method for purification of staphylococcal enterotoxin A

A novel single-step procedure for the purification of staphylococcal enterotoxin A (SEA), namely, dye ligand affinity chromatography with the triazine dye Red A, was developed. SEA purified by this method produced a single band when subjected to sodium dodecyl sulfate-polyacrylamide gel electrophoresis. The yield from 5 liters of culture supernatant was 0.113 g, corresponding to an overall yield of 55%. In some instances, purification of SEA from culture supernatants by dye ligand affinity chromatography produced two enterotoxin peaks that could be eluted from the column with 300 and 500 mM phosphate buffer (pH 6.8). Enterotoxin from these peaks produced a single band when subjected to sodium dodecyl sulfate-polyacrylamide gel electrophoresis, but multiple bands were observed on isoelectric focusing gels. This method of purification represents a significant improvement in time, yields, and purity of enterotoxin over previously published purification methods.     

Novel method for purification of staphylococcal enterotoxin A.

A novel single-step procedure for the purification of staphylococcal enterotoxin A (SEA), namely, dye ligand affinity chromatography with the triazine dye Red A, was developed. SEA purified by this method produced a single band when subjected to sodium dodecyl sulfate-polyacrylamide gel electrophoresis. The yield from 5 liters of culture supernatant was 0.113 g, corresponding to an overall yield of 55%. In some instances, purification of SEA from culture supernatants by dye ligand affinity chromatography produced two enterotoxin peaks that could be eluted from the column with 300 and 500 mM phosphate buffer (pH 6.8). Enterotoxin from these peaks produced a single band when subjected to sodium dodecyl sulfate-polyacrylamide gel electrophoresis, but multiple bands were observed on isoelectric focusing gels. This method of purification represents a significant improvement in time, yields, and purity of enterotoxin over previously published purification methods.     

Optimisation of aqueous two-phase extraction of human antibodies

The purification of human antibodies in an aqueous two-phase system (ATPS) composed of polyethylene glycol (PEG) 6000 and phosphate was optimised by surface response methodology. A central composite design was used to evaluate the influence of phosphate, PEG and NaCl concentration and of the pH on the purity and extraction yield of IgG from a simulated serum medium. The conditions that maximise the partition of IgG into the upper phase were determined to be high concentrations of NaCl and PEG, low concentrations of phosphate and low pH values. An ATPS composed of 12% PEG, 10% phosphate, 15% NaCl at pH 6 was further used to purify human monoclonal antibodies from a Chinese Hamster Ovary (CHO) concentrated cell culture supernatant with a recovery yield of 88% in the upper PEG-rich phase and a purification factor of 4.3. This ATPS was also successfully used to purify antibodies from a hybridoma cell culture supernatant with a recovery yield of 90% and a purification factor of 4.1.     

Purification of recombinant chimeric B72.3 Fab' and F(ab')2 using streptococcal protein G.

Streptococcal protein G has been used extensively for the purification of antibodies using the interaction of the Fc region with protein G. Many antibodies also interact with protein G through a low-affinity binding site for the Fab region. The exploitation of this low-affinity interaction for the purification of Fab' fragments is described here. Chimeric mouse-human B72.3 Fab' and F(ab')2 fragments were expressed by CHO cells and purified from CHO cell supernatant using protein G-Sepharose. Since chimeric B72.3 Fab' bound weakly to the protein G-Sepharose it could be separated from F(ab')2 and eluted with a pH 7 wash whereas B72.3 F(ab')2 required elution at pH 2. Both Fab' and F(ab')2 were recovered with full immunoreactivity and could be further purified using gel-filtration chromatography to greater than 99% purity. This method allows the simple purification of directly expressed Fab' or F(ab')2 fragments from CHO cell supernatant.     

Optimization of Escherichia coli cultivation methods for high yield neuropeptide Y receptor type 2 production

The recombinant expression of human G protein-coupled receptors usually yields low production levels using commonly available cultivation protocols. Here, we describe the development of a high yield production protocol for the human neuropeptide Y receptor type 2 (Y2R), which provides the determination of expression levels in a time, media composition, and process parameter dependent manner. Protein was produced by Escherichia coli in a defined medium composition suitable for isotopic labeling required for investigations by nuclear magnetic resonance spectroscopy. The Y2 receptor was fused to a C-terminal 8x histidine tag by means of the pET vector system for easy one-step purification via affinity chromatography, yielding a purity of 95-99% for every condition tested, which was determined by SDS-PAGE and Western blot analysis. The Y2 receptor was expressed as inclusion body aggregates in complex media and minimal media, using different carbon sources. We investigated the influences of media composition, temperature, pH, and set specific growth rate on cell behavior, biomass wet weight specific and culture volume specific amounts of the target protein, which had been identified by inclusion body preparation, solubilization, followed by purification and spectrometric determination of the protein concentration. The developed process control strategy led to very high reproducibility of cell growth and protein concentrations with a maximum yield of 800 μg purified Y2 receptor per gram wet biomass when glycerol was used as carbon source in the mineral salt medium composition (at 38 °C, pH 7.0, and a set specific growth rate of 0.14 g/(gh)). The maximum biomass specific amount of purified Y2 receptor enabled the production of 35 mg Y2R per liter culture medium at an optical density (600 nm) of 25.     

Expression of truncated tobacco osmotin in Escherichia coli: purification and antifungal activity

PURPOSE OF WORK: Tobacco osmotin is a functional homolog of mammalian adiponectin, and has antifungal activity. This work was undertaken to produce recombinant osmotin that has previously been unsuccessful because of its toxicity. Expression of recombinant tobacco osmotin (rOSM) in Escherichia coli inclusion bodies has been achieved. The optimal pH for rOSM expression in ZYM 505 medium is 7.0 at OD(650) of 1.5 of culture growth. The rOSM from the inclusion body was extracted with 8 M urea, and purified using CM-cellulose and cobalt-agarose bead affinity chromatography to a high purity. Approximately 80% of the rOSM remained bound to CM-cellulose and Cobalt-agarose beads after initial elution. The yield of purified rOSM was between 40 and 50 mg from 2 l of culture. Repeated elution of protein from CM-cellulose and Co-agarose increased the yield of rOSM to 200 mg from 2 l culture. The purified rOSM showed variable antifungal activities against two pathogenic yeast strains; Cryptococcus neoformans, Candida albicans, and non-pathogenic strains; Saccharomyces cerevisiae and Pichia methanolica.     

Capture of human monoclonal antibodies from a clarified cell culture supernatant by phenyl boronate chromatography

In this work, we investigated the feasibility of using phenyl boronate (PB) chromatography for the direct capture of monoclonal antibodies from a CHO cell supernatant. Preliminary results, using pure protein solutions have shown that PB media can bind to human antibodies, not only at strong alkaline conditions but also at acidic pH values. In fact, antibodies have been found to bind in the pH range 5.5-8.5. On the other hand, insulin and human serum albumin did not bind at alkaline pH but at lower pH, which reflects the importance of non-specific interactions with the matrix. Different binding and eluting buffers were evaluated for the capture of immunoglobulin G (IgG) from a CHO cell supernatant and the most promising results were obtained using 20 mM 4-(2-hydroxyethyl)-1-piperazineethanesulfonic acid at pH 8.5 as binding buffer and 1.5 M Tris-HCl as eluting buffer. Using a step elution, all IgG was recovered in the elution pool with a maximum purification factor of 56. A gradient elution allowed a further increase of the final purity, yet achieving a slightly lower yield. IgG recovery was around 85% and the purification factor was 76. The highest purity was obtained when the pH of the cell supernatant feed was previously adjusted to 8.5. Starting from an initial protein purity of 1.1% and high-performance liquid chromatography (HPLC) purity of 2.2%, after PB adsorption, a final protein purity of 85% and a HPLC purity of 88% was achieved.     

On-column refolding purification and characterization of recombinant human interferon-lambda1 produced in Escherichia coli

Interferon-lambda1 (IFN-lambda1) is a member of the recently discovered type III IFNs (IFN-lambda), which possesses antiviral, antitumor, and immunomodulatory activities. In this study, the recombinant human IFN-lambda1 containing a hexahistidine tag was expressed in Escherichia coli. IFN-lambda1 was overexpressed under the control of T7 promoter and most of the protein existed in the form of inclusion bodies. The expressed insoluble protein was solubilized with urea, purified and refolded by one-step immobilized metal-ion affinity chromatography using Ni(2+)-nitrilotriacetic acid agarose. The purified IFN-lambda1 appeared as a single band on SDS-PAGE and the purity was more than 95%. The yield was 86 mg IFN-lambda1 from 1L of bacterial culture. Western blotting and N-terminal sequencing confirmed the identity of the purified protein. The purified IFN-lambda1 exhibited specific antiviral activity as demonstrated by a cytopathic effect reduction assay. Thus, this on-column refolding method provides an efficient way to obtain an active IFN-lambda1 with high yield and high purity.     

Verticase： a Fibrinolytic Enzyme Produced by Verticillium sp, Tj33, an Endophyte of Trachelospermum jasminoides

Plant endophytes are among the most important resources of biologically active metabolites. Twenty-three endophyte strains residing in Trachelospermum jasminoides were cultivated in vitro with the cultures assayed for the fibrinolytic substance production. As a result, the culture of VerticUlium sp. Tj33 was shown to be the most active. A fibrinolytic enzyme designated as verticase was subsequently purified from the supernatant of Verticillium sp. culture broth by a combination of DEAE-52, Sephadex G-75 and hydrophobic column chromatographies. Verticase, with its molecular mass of 31 kDa and pl of 8.5, was demonstrated to be homogeneous by sodium dodecyl suIfate-polyacrylamide gel electrophoresis and isoelectric focusing electrophoresis. Verticase is an enzyme that hydrolyzes fibrin directly without activation of plaminogen. It was stable in a broad pH range from 4 through to 11 with the optimal reaction pH value and temperature shown to be around 9-10 and 50-60℃, respectively. The fibrinolytic activity of verticase was severely inhibited by phenylmethylsulfony fluoride, indicating that verticase was a serine protease.     

Single step recombinant human growth hormone (rhGH) purification from milk by peptide affinity chromatography

Recombinant human growth hormone (rhGH) is used for the treatment of several pathologies, most of them related to growth. Although different expression systems can be used for its production, the milk from transgenic cows is one of the most interesting due to the high rhGH level achieved (5 g/L). We have designed and synthesized short peptides (9 or 10 amino acid long) using Fmoc chemistry and studied their ability to purify rhGH from milk once immobilized on an agarose support. Using spiked milk with the hormone as a sample, rhGH was purified with 88% yield and 92% purity in a single step with a fold purification of 4.5. © 2018 American Institute of Chemical Engineers Biotechnol. Prog., 34:999–1005, 2018     

人鼠嵌合单克隆抗体c30.6的纯化

采用介体电泳技术对CHO细胞培养液中的人鼠嵌合单克隆抗体c30.6进行纯化,第一步在pH8.6条件下进行,抗体带正电荷而培养液中的大部分杂质带负电荷,抗体和杂质的在电场作用下向两电极运动,结果被分离在分离膜的两侧,SDS－PAGE显示抗体纯度达95％,且剩余杂质的分子量均小于抗体的分子量。第二步是在pH6.0条件下进行,此时抗体和杂质都带正电荷,它们在电场作用下向同一方向运动,但分离膜只允许分子量较小的杂质通过,抗体得以进一步纯化,抗体的回收率为80％,而且生物活性未受影响。     

生淀粉酶生产菌株Paenibacillus sp.的筛选和酶的纯化及酶学性质

分离得到1株产生淀粉酶的菌株,通过扩增和测定16S rDNA序列并进行比对,发现是Paenibacillus属的细菌。液体摇瓶发酵结束后,其产生的生淀粉酶比酶活达108.5U/mL。通过饱和(NH4)2SO4沉淀、Sephacryl S-300层析的方法对其所产的生淀粉酶进行分离纯化,得到纯化的酶蛋白比酶活为5112.04U/mg,纯化倍数为14.1,相对分子质量约为1.0×105。该酶以木薯生淀粉为底物时,最适pH5.6,最适温度50℃。金属离子Ca2+、Mg2+对该酶具有激活作用,Zn2+、Cu2+、Fe2+、Ni2+、Mn2+、Co2+和EDTA2-对该酶均具有抑制作用。     

抗ErbB2嵌合抗体chA21大规模纯化工艺的建立及质量研究

自行研制的抗ErbB2嵌合抗体chA21具有抑制高表达ErbB2的乳腺癌细胞生长的作用。在前期小规模培养和纯化工作的基础上,以填充床生物反应器大规模培养CHO工程细胞株表达的上清为原料,采用亲和层析、凝胶过滤除盐、阳离子交换层析、分子筛等步骤,分离纯化嵌合抗体chA21,建立了大规模纯化工艺,并按照中国药典（2005年版第三部）对最终产品进行全面鉴定和质量控制。该工艺能有效解决抗体纯化过程形成的多聚体问题,去除内毒素和DNA残留;可以确保每批纯化20~40L培养上清,每批收获嵌合抗体可达5g以上,蛋白总回收率大于50％,纯度可达98％。研究结果表明,该抗体纯化工艺得率高,质量控制方法稳定可靠,适用于大规模生产。     

Effect of acidotropic amines on the accumulation of newly synthesized membrane and luminal proteins in Chinese-hamster ovary (CHO) cell lysosomes.

Lysosomes were isolated by sequential gradient centrifugation [Madden, Wirt & Storrie (1987) Arch. Biochem. Biophys. 257, 27-38] from control or acidotropic-amine-treated Chinese-hamster ovary (CHO) cells. By marker-enzyme analysis, the preparation from chloroquine or NH4Cl-treated cells was about 25-fold enriched for lysosomes compared with the postnuclear supernatant and contained little or no marker activities for the plasma membrane, rough endoplasmic reticulum, Golgi apparatus, mitochondria, cytosol and peroxisomes. The yield of amine-treated lysosomes was about 60% relative to the postnuclear supernatant. Electron microscopy and cytochemistry demonstrated that the amine-treated preparation was highly purified. Cytochemical analyses after a short-term pulse of horseradish peroxidase revealed that endosomal contamination of the lysosomal preparation was less than 1%. Lysosomal polypeptides were biosynthetically labelled with [35S]methionine and identified by SDS/polyacrylamide-gel electrophoresis. As expected, the bulk accumulation of luminal proteins into lysosomes was decreased. The bulk accumulation of membrane proteins was increased by acidotropic amine treatment. There were also several qualitative differences in each lysosomal compartment, with new species observed and other species absent. These data suggest that a low pH is not necessary for the normal accumulation of the bulk of membrane proteins in lysosomes and that membrane trafficking from Golgi apparatus to lysosomes occurs at a high rate in acidotropic-amine-treated CHO cells.     

Prokaryotic overexpression of TEV–rhGH and characterization of its polyclonal antibody

Recombinant protein technology represents one of the best solutions to achieve rapid, efficient, and cost-effective protein expression and purification of therapeutic proteins. Growth hormone (GH) is an excellent example of these proteins used in the therapy of hormone deficiencies. In this work, a plasmid, pRSET–TEV–rhGH, has been constructed to overexpress recombinant human GH (rhGH) by cloning its gene downstream of an N-terminal 6 × His-tagged polypeptide (43 aa) in the T7 promoter-plasmid pRSET. This polypeptide was cleavable by means of the integrated recognition site for the tobaccos etch virus (TEV) protease, resulting in an rhGH protein at an exact length and sequence. After IPTG induction, this plasmid effectively expressed TEV–rhGH protein (27 kDa) in the cytoplasm of Escherichia coli, which accumulated in the form of inclusion bodies. The 6 × His-tagged protein, with a yield of ~ 150 mg/L of culture, was purified from the cell extract using metal affinity chromatography, as shown after SDS-PAGE blue staining, and was confirmed by immunoblotting using specific commercial monoclonal antibodies. In order to detect TEV–rhGH, in ELISA and immunoblotting, specific polyclonal antibody, with high titer (~ 10^− 5 fold dilution), was produced in a rabbit and purified using affinity chromatography. Preliminary tests have proved that TEV–rhGH protein and its specific purified IgG antibody could provide valuable tools for rhGH productive and diagnostic purposes.     

Strategies for the enrichment and identification of basic proteins in proteome projects

Two-dimensional gel electrophoresis (2-DE) is currently the method of choice for separating complex mixtures of proteins for visual comparison in proteome analysis. This technology, however, is biased against certain classes of proteins including low abundance and hydrophobic proteins. Proteins with extremely alkaline isoelectric points (pI) are often very poorly represented using 2-DE technology, even when complex mixtures are separated using commercially available pH 6-11 or pH 7-10 immobilized pH gradients. The genome of the human gut pathogen, Helicobacter pylori, is dominated by genes encoding basic proteins, and is therefore a useful model for examining methodology suitable for separating such proteins. H. pylori proteins were separated on pH 6-11 and novel pH 9-12 immobilized pH gradients and 65 protein spots were subjected to matrix-assisted laser desorption/ionization-time of flight mass spectrometry, leading to the identification of 49 unique proteins. No proteins were characterized with a theoretical pI of greater than 10.23. A second approach to examine extremely alkaline proteins (pI > 9.0) utilized a prefractionation isoelectric focusing. Proteins were separated into two fractions using Gradiflow technology, and the extremely basic fraction subjected to both sodium dodecyl sulphate-polyacrylamide gel electrophoresis and liquid chromatography (LC) - tandem mass spectrometry post-tryptic digest, allowing the identification of 17 and 13 proteins, respectively. Gradiflow separations were highly specific for proteins with pI > 9.0, however, a single LC separation only allowed the identification of peptides from highly abundant proteins. These methods and those encompassing multiple LC 'dimensions' may be a useful complement to 2-DE for 'near-to-total' proteome coverage in the alkaline pH range.     

Comparison of microbial and transient expression (tobacco plants and plant-cell packs) for the production and purification of the anticancer mistletoe lectin viscumin

Cancer is the leading cause of death in industrialized countries. Cancer therapy often involves monoclonal antibodies or small-molecule drugs, but carbohydrate-binding lectins such as mistletoe (Viscum album) viscumin offer a potential alternative treatment strategy. Viscumin is toxic in mammalian cells, ruling them out as an efficient production system, and it forms inclusion bodies in Escherichia coli such that purification requires complex and lengthy refolding steps. We therefore investigated the transient expression of viscumin in intact Nicotiana benthamiana plants and Nicotiana tabacum Bright Yellow 2 plant-cell packs (PCPs), comparing a full-length viscumin gene construct to separate constructs for the A and B chains. As determined by capillary electrophoresis the maximum yield of purified heterodimeric viscumin in N. benthamiana was ~7 mg/kg fresh biomass with the full-length construct. The yield was about 50% higher in PCPs but reduced 10-fold when coexpressing A and B chains as individual polypeptides. Using a single-step lactosyl-Sepharose affinity resin, we purified viscumin to ~54%. The absence of refolding steps resulted in estimated cost savings of more than 80% when transient expression in tobacco was compared with E. coli. Furthermore, the plant-derived product was ~3-fold more toxic than the bacterially produced counterpart. We conclude that plants offer a suitable alternative for the production of complex biopharmaceutical proteins that are toxic to mammalian cells and that form inclusion bodies in bacteria.     

Dendritic cell activating factor produced by mouse macrophage hybridoma

A mouse macrophage (M phi) hybridoma which produces a soluble factor responsible for the cooperation between M phi and spleen dendritic cells (DC) was constructed. The antigen-presenting activity and the stimulator cell activity in the allogeneic or syngeneic mixed leukocyte reaction of DC were significantly augmented when DC were incubated with the culture supernatant of the hybridoma treated with various stimulants including latex beads. The monokine present in the culture supernatant of the hybridoma, called dendritic cell-activating factor (DCAF), augmented the production of lymphocyte-activating factor by DC while Ia expression of DCAF-treated DC was not altered. DCAF had no effect on the antigen-presenting activity of peritoneal resident M phi or B cell blasts while the antigen-presenting activity of spleen M phi was enhanced, but the degree of the enhancement was much less than that of spleen DC. DCAF was found to have the following properties: its pI value is between pH 4 and 5; it is stable at pH 2 to 10; and it loses its activity on incubation at 75 C for 30 min. When the culture supernatant of the hybridoma stimulated with latex beads was subjected to gel filtration, the DCAF activity was detected in the 20 Kd to 25 Kd, 30 Kd to 40 Kd, and 50 Kd to 60 Kd molecular weight regions. The 30 Kd to 40 Kd fraction, which is the major peak fraction, was further purified by ion-exchange chromatography followed by gel-filtration chromatography. When each fraction was subjected to SDS-PAGE, a 30 Kd band corresponding to the DCAF activity was observed and DCAF was purified to about 90% purity.