重组质粒pVAX1-PENK大规模制备研究

目的：建立质粒pVAX1-PENK的大规模制备2--艺。方法：对大肠杆菌工程菌DH5α-pVAX1-PENK进行补料发酵,利用自行发明的连续碱裂解过程对菌体进行裂解,经超滤浓缩后,用Sepharnse 6 Fast Flow层析柱分离DNA与RNA,再经Plasmidselect Xtra层析柱分离超螺旋质粒DNA与开环或线性质粒DNA,最后经Source 15Q层析柱精制质粒DNA。结果：发酵获得质粒pVAX1-PENK的产率为182mg／L,经碱裂解及层析分离后,最终制备的质粒DNA超螺旋比例大于98％,总回收率为60.5％,纯度（D260nm／D280nm）为1.8～2.0。结论：建立的质粒DNA生产工艺可以制备大量高纯度的质粒DNA,并避免了使用动物源性的酶及有毒试剂。     

Preparative peptide purification by cation-exchange and reversed-phase perfusion chromatography.

Cation exchange was compared to reversed-phase chromatography for the preparative purification of a 28-residue peptide (vasoactive intestinal polypeptide) on the 100-mg scale. Optimized high-speed, high-resolution methods were developed for both chromatographic modes on POROS Perfusion Chromatography flow-through particle chromatography columns. While both methods appeared to provide similar purity, the cation exchange column had approximately ten times the loading capacity per unit column volume as the reversed-phase column. Five-minute methods for desalting the cation exchange-purified peptide and analysis of fractions were developed using small reversed-phase columns. The cation-exchange method was scaled up to process 95 mg of crude peptide in a 12-min run.     

Plasmid DNA purification using a multimodal chromatography resin

Multimodal chromatography is widely used for isolation of proteins because it often results in improved selectivity compared to conventional separation resins. The binding potential and chromatographic behavior of plasmid DNA have here been examined on a Capto Adhere resin. Capto Adhere is a recent multimodal chromatography material allowing molecular recognition between the ligand and target molecule, which is based on combined ionic and aromatic interactions. Capto Adhere proved to offer a very strong binding of nucleic acids. This property could be used to isolate plasmid DNA from a crude Escherichia coli extract. Using a stepwise NaCl gradient, pure plasmid DNA could be obtained without protein and endotoxin contaminations. The RNA fraction bound most strongly to the resin and could be eluted only at very high salt concentrations (2.0 M NaCl). The chromatographic separation behavior was very robust between pH values 6 and 9, and the dynamic binding capacity was estimated to 60 µg/ml resin. Copyright © 2014 John Wiley & Sons, Ltd.     

Concentration and purification of enteroviruses by membrane chromatography.

A simple procedure for the concentration and partial purification of enteroviruses from tissue culture harvests is described. After removal of acid-precipitating components with a cationic detergent, the detergent and most membrane-coating components were removed by treatment with a cationic-exchange resin. The resin effluent was then acidified, and the virus was adsorbed to epoxy-fiberglass membranes. Virus was then eluted with pH 11.5 glycine-NaOH buffer. Since this eluate contains no orgcentrated simply by acidifying the eluate and passing it through a smaller membrane than that used for the first concentration. As high as 500-fold concentrations can be achieved, with a high efficiency of recovery.     

Concentration and purification of enteroviruses by membrane chromatography.

A simple procedure for the concentration and partial purification of enteroviruses from tissue culture harvests is described. After removal of acid-precipitating components with a cationic detergent, the detergent and most membrane-coating components were removed by treatment with a cationic-exchange resin. The resin effluent was then acidified, and the virus was adsorbed to epoxy-fiberglass membranes. Virus was then eluted with pH 11.5 glycine-NaOH buffer. Since this eluate contains no orgcentrated simply by acidifying the eluate and passing it through a smaller membrane than that used for the first concentration. As high as 500-fold concentrations can be achieved, with a high efficiency of recovery.     

Isolation, purification and quantification of BRCA1 protein from tumour cells by affinity perfusion chromatography

A new procedure for the isolation, purification and quantification of the product of the oncosuppressor gene brca1 in breast tissues, was carried out. It involves internal cell protein [³⁵S]methionine labelling followed by two perfusion chromatographies. The first one is heparin affinity chromatography, to purify all of the cell DNA-binding proteins. A subsequent specific immunoprecipitation of BRCA1 protein was performed with an antibody raised against BRCA1. The immune complex was isolated using the second chromatographic step, Protein A affinity chromatography. The amount of BRCA1 expressed by cells was expressed as a ratio, in percent, calculated as follows: 100× amount of labelled DNA-binding proteins (dpm) that bound specifically to the anti-BRCA1 polyclonal antibodies (K-18)/amount of whole labelled DNA-binding protein (dpm) purified on a heparin column. Applications to MCF7 and T-47D human breast tumour cell lines, which were treated or not using 2 mM sodium butyrate demonstrated an increase in BRCA1 protein expression.     

Improved purification of recombinant adenoviral vector by metal affinity membrane chromatography

The increasing importance of adenoviral vectors for gene therapy clinical trials necessitates the development of processes suitable for large-scale and commercial production of adenovirus. Here, we evaluated a novel purification process combining an anion-exchange chromatography and an immobilized metal affinity membrane chromatography for the purification of recombinant adenovirus. Adenovirus was initially purified from clarified infectious lysate by anion-exchange chromatography using Q Sepharose XL resin and further polished using a Sartobind IDA membrane unit charged with Zn²⁺ ions as affinity ligands. The metal affinity membrane chromatography efficiently removed residual host cell impurities that co-eluted with adenovirus during the previous anion-exchange chromatography step. The metal affinity membrane chromatography also separated defective adenovirus particles from the infectious adenovirus fraction. Furthermore, the metal affinity membrane chromatography showed an improved yield, when compared with a conventional bead-based metal affinity chromatography. The purity and specific activity of the adenovirus prepared using this two-step chromatography was comparable to those of adenovirus produced by the conventional CsCl density centrifugation. Therefore, our data provide an improved method for the purification of adenoviral vectors for clinical applications.     

Immobilized artificial membrane chromatography: rapid purification of functional membrane proteins

A solid-phase membrane mimetic system, denoted as immobilized artificial membranes (IAM), has been developed and utilized as a novel high-performance liquid chromatography (HPLC) matrix for the first step in the rapid purification of functional membrane proteins. IAM phases consist of monolayers of amphiphilic membrane lipid molecules covalently bonded to a rigid silica particle. These monolayers of lipids have proved remarkably effective for the chromatography of biomolecules. Several cytochrome P450 isozymes, an extremely important family of hydrophobic membrane proteins with a labile heme catalytic center, have been partially purified in functional conformations from rat liver, kidney, and adrenal microsomes on IAM supports. Functionality of purified P450 and P450 reductase has been demonstrated by optical difference spectroscopy, by carbon monoxide binding, and by reconstitution of enzymatic activity in vitro. Other membrane proteins, including rat liver plasma membrane NADH oxidase and ferricyanide oxidoreductase have also been partially purified by IAM HPLC. The methods for purification of these proteins are described.     

Advective hydrogel membrane chromatography for monoclonal antibody purification in bioprocessing

Protein A chromatography is widely employed for the capture and purification of monoclonal antibodies (mAbs). Because of the high cost of protein A resins, there is a significant economic driving force to seek new downstream processing strategies. Membrane chromatography has emerged as a promising alternative to conventional resin based column chromatography. However, to date, the application has been limited to mostly ion exchange flow through (FT) mode. Recently, significant advances in Natrix hydrogel membrane has resulted in increased dynamic binding capacities for proteins, which makes membrane chromatography much more attractive for bind/elute operations. The dominantly advective mass transport property of the hydrogel membrane has also enabled Natrix membrane to be run at faster volumetric flow rates with high dynamic binding capacities. In this work, the potential of using Natrix weak cation exchange membrane as a mAb capture step is assessed. A series of cycle studies was also performed in the pilot scale device (> 30 cycles) with good reproducibility in terms of yield and product purities, suggesting potential for improved manufacturing flexibility and productivity. In addition, anion exchange (AEX) hydrogel membranes were also evaluated with multiple mAb programs in FT mode. Significantly higher binding capacity for impurities (support mAb loads up to 10Kg/L) and 40X faster processing speed were observed compared with traditional AEX column chromatography. A proposed protein A free mAb purification process platform could meet the demand of a downstream purification process with high purity, yield, and throughput. © 2015 American Institute of Chemical Engineers Biotechnol. Prog., 31:974–982, 2015     

Evaluation of immobilized metal membrane affinity chromatography for purification of an immunoglobulin G1 monoclonal antibody

The large scale production of monoclonal antibodies (McAbs) has gaining increased relevance with the development of the hybridoma cell culture in bioreactors creating a need for specific efficient bioseparation techniques. Conventional fixed bead affinity adsorption commonly applied for McAbs purification has the drawback of low flow rates and colmatage. We developed and evaluated a immobilized metal affinity chromatographies (IMAC) affinity membrane for the purification of anti-TNP IgG(1) mouse McAbs. We immobilized metal ions on a poly(ethylene vinyl alcohol) hollow fiber membrane (Me(2+)-IDA-PEVA) and applied it for the purification of this McAbs from cell culture supernatant after precipitation with 50% saturation of ammonium sulphate. The purity of IgG(1) in the eluate fractions was high when eluted from Zn(2+) complex. The anti-TNP antibody could be eluted under conditions causing no loss of antigen binding capacity. The purification procedure can be considered as an alternative to the biospecific adsorbent commonly applied for mouse IgG(1) purification, the protein G-Sepharose.     

A high-throughput approach to developing and optimizing mixed-mode membrane chromatography for protein purification

Membrane chromatography has been established as a viable alternative to packed-bed column chromatography for the purification of therapeutic proteins. Purification via membrane chromatography offers key advantages, including higher productivity and reduced buffer usage. Unlike column chromatography purification, the utilization of high-throughput screening in order to reduce development times and material requirements has been a challenge for membrane chromatography. This research focused on the development of a new, high-throughput screening technique for use in screening membrane chromatography conditions for monoclonal antibody purification. The developed screen utilizes a 96-well plate format, thereby allowing for the screening of multiple different membrane conditions at once. For this study, four mixed-mode cation exchange membranes and one cation exchange membrane were evaluated on the plate. The screen is performed in a similar manner to that of a resin slurry plate screen, however, instead of a single loading step, the antibody feed was loaded in 50 mg/ml increments up to a maximum loading of 450 mg/ml. Performing a similar, incremental loading on a resin plate would be impractical, as mixing times are substantially longer due to pore diffusion limitations. However, due to the significantly faster rate of mass transfer for membranes relative to resin, mixing times could be reduced by up to a factor of sixty on the membrane plate. Additional optimization showed that higher hydrophobicity can potentially lead to slower kinetics and mixing times that may need to be adjusted accordingly. The end result is a screen that has been proven to provide results comparable to those obtained on larger-scale membrane purification runs while also enabling exploration of a much greater operating space and significantly reducing the feed materials required.     

The purification of human serum 1 -antitrypsin by affinity chromatography on concanavalin A

α₁-Antitrypsin (α₁-AT) has been isolated from human serum by a two-step procedure which involves chromatography on DEAE-Sephadex followed by affinity chromatography on insolubilized concanavalin A. This protein appeared to be homogeneous when examined by electrophoresis on cellulose acetate and double immunodiffusion; minor contaminants, however, were detected by gel electrophoresis and immunoelectrophoresis. This procedure is readily adaptable to the large-scale purification of α₁-AT and should facilitate further studies on the physicochemical and biological properties of α₁-AT and its genetic variants.