双水相电泳分离蛋白质的研究

近几年来,随着生物技术的迅速发展,制备型电泳技术的研究得到了重视。然而由于技术上的原因,大规模的制备型电泳技术的研究还未能取得突破。阻碍电泳放大的一个主要问题是由于电加热作用而导致的热对流对电泳分离的破坏。为解决这一问题,人们提出了许多方法。例如,在太空的微重力环境下进行电泳,应力稳定自由流动电泳,循环等电聚焦和区带电泳,色谱电泳和等电膜等电聚焦等。这些方法在电泳放大上都取得了一定的进展,但各有其局限性。最近,Clark提出利用双水相的液液界面阻止热对流的设想,为开发大规模的制备型电泳技术开辟了一条新途径、Raghava Rao等在两种双水相体系上施加电场后成倍地缩短了分相时间。Levine和Bier采用U型管电泳装置研究了双水相体系中血红蛋白的电泳迁移率,观测到界面有阻滞作用。Clark在柱型电泳装置中进行了一组双水相萃取肌红蛋白的简单实验。在10mA的恒电流下电泳40min之后,肌红蛋白的分配系数为7.5,而当电场反向后,分配系数变为0.04,界面阻力并不显著,两者结论并不一致。     

Targeted purification development enabled by computational biophysical modeling

Chromatographic and non‐chromatographic purification of biopharmaceuticals depend on the interactions between protein molecules and a solid–liquid interface. These interactions are dominated by the protein–surface properties, which are a function of protein sequence, structure, and dynamics. In addition, protein–surface properties are critical for in vivo recognition and activation, thus, purification strategies should strive to preserve structural integrity and retain desired pharmacological efficacy. Other factors such as surface diffusion, pore diffusion, and film mass transfer can impact chromatographic separation and resin design. The key factors that impact non‐chromatographic separations (e.g., solubility, ligand affinity, charges and hydrophobic clusters, and molecular dynamics) are readily amenable to computational modeling and can enhance the understanding of protein chromatographic. Previously published studies have used computational methods such as quantitative structure–activity relationship (QSAR) or quantitative structure–property relationship (QSPR) to identify and rank order affinity ligands based on their potential to effectively bind and separate a desired biopharmaceutical from host cell protein (HCP) and other impurities. The challenge in the application of such an approach is to discern key yet subtle differences in ligands and proteins that influence biologics purification. Using a relatively small molecular weight protein (insulin), this research overcame limitations of previous modeling efforts by utilizing atomic level detail for the modeling of protein–ligand interactions, effectively leveraging and extending previous research on drug target discovery. These principles were applied to the purification of different commercially available insulin variants. The ability of these computational models to correlate directionally with empirical observation is demonstrated for several insulin systems over a range of purification challenges including resolution of subtle product variants (amino acid misincorporations). Broader application of this methodology in bioprocess development may enhance and speed the development of a robust purification platform. © 2014 American Institute of Chemical Engineers Biotechnol. Prog., 31:154–164, 2015     

Synthesis and performance of 3D-megaporous structures for enzyme immobilization and protein capture

The preparation of megaporous bodies, with potential applications in biotechnology, was attempted by following several strategies. As a first step, naive and robust scaffolds were produced by polymerization of selected monomers in the presence of a highly soluble cross‐linker agent. Ion‐exchange function was incorporated by particle embedding, direct chemical synthesis, or radiation‐induced grafting. The total ionic capacity of such systems was 1.5 mmol H⁺/g, 1.4 mmol H⁺/g, and 17 mmol H⁺/g, respectively. These values were in agreement with the ability to bind model proteins: observed dynamic binding capacity at 50% breakthrough was ?7.2 mg bovine serum albumin/g, ?7.4 hen egg‐white lysozyme (HEWL) mg/g, and ?108 HEWL mg/g. In the later case, total (static) binding capacity reached 220 mg/g. It was observed that the structure and size of the megapores remained unaffected by the grafting procedure which, however, allowed for the highest protein binding capacity. Lysozyme supported on grafted body showed extensive clarification activity against a Micrococcus lysodekticus suspension in the flow‐through mode, i.e., 90% destruction of suspended microbial cells was obtained with a residence time ≈ 18 min. Both protein capture and biocatalysis applications are conceivable with the 3D‐megaporous materials described in this work. © 2011 American Institute of Chemical Engineers Biotechnol. Prog., 2011     

Extraction of DNA from soil using nanoparticles by magnetic bioseparation

Aims: To develop a simple, rapid and inexpensive soil DNA extraction protocol. Methods and Results: The protocol relies on the use of superparamagnetic silica‐magnetite nanoparticles for the isolation and purification of DNA from soil samples. DNA suitable for use in molecular biology applications was obtained from a number of soil samples. Conclusions: The DNA extracted using the tested method successfully permitted the PCR amplification of a fragment of the bacterial 16S rDNA gene. The extracted DNA could also be restriction endonuclease digested. Significance and Impact of the Study: The protocol reported here is simple and permits rapid isolation of PCR‐ready soil DNA. The method requires only small quantities of soil sample, is scalable and suitable for automation.     

Paper-PEG-based membranes for hydrophobic interaction chromatography: purification of monoclonal antibody

This article discusses the preparation of novel Paper-PEG interpenetrating polymer network-based membranes as inexpensive alternative to currently available adsorptive membranes. The Paper-PEG membranes were developed for carrying out hydrophobic interaction membrane chromatography (HIMC). PEG is normally very hydrophilic but can undergo phase separation and become hydrophobic in the presence of high antichaotropic salt concentrations. Two variants of the Paper-PEG membranes, Paper-PEG 1 and Paper-PEG 2 were prepared by grafting different amounts of the polymer on filter paper and these were tested for their hydraulic properties and antibody binding capacity. The better of the two membranes (Paper-PEG 1) was then used for purifying the monoclonal antibody hIgG1-CD4 from simulated mammalian cell culture supernatant. The processing conditions required for purification were systematically optimized. The dynamic antibody binding capacity of the Paper-PEG 1 membrane was about 9 mg/mL of bed volume. A single step membrane chromatographic process using Paper-PEG 1 membrane gave high monoclonal antibody purity and recovery. The hydraulic permeability of the paper-based membrane was high and was maintained even after many runs, indicating that membrane fouling was negligible and the membrane was largely incompressible.     

Purification of equine IgG using membrane based enhanced hybrid bioseparation technique: a potential method for manufacturing hyperimmune antibody

Hyperimmune equine IgG is widely used as antivenom and anti-rabies agents. This article discusses a membrane based enhanced hybrid bioseparation technique for efficient and scalable purification of equine immunoglobulin G (IgG) from horse serum. This technique is an improved version of a standard hybrid bioseparation technique developed within our group earlier for fractionation of human plasma proteins (Ghosh. 2004. J Membr Sci 237: 109-117). In the presence of a high antichaotropic salt concentration, equine IgG is selectively and reversibly captured within a stirred cell membrane module from horse serum, partly due to precipitation and microfiltration, and partly due to hydrophobic interaction based membrane adsorption, while the impurities are washed out from the device. The reversibly sequestered IgG is then released by lowering the salt concentration which favor both dissolution of the precipitated IgG and desorption of the membrane bound IgG. The enhanced hybrid bioseparation technique improves the IgG recovery from the membrane module by switching from a stirring to non-stirring mode during the IgG release phase. It also reduces membrane fouling by an appropriate pH switch. The effects of operating conditions on equine IgG capture were first systematically studied. The enhanced hybrid bioseparation technique was followed by an ultrafiltration step to remove ammonium sulfate and low molecular weight impurities. The equine IgG purity obtained under optimized conditions was 88% and its recovery was over 90%, both being significantly higher than corresponding values obtained using currently used purification techniques.     

铁蛋白介导的地衣多糖酶胞内自发聚集及其高效制备

酶分离纯化、固定化及催化性能提升一直是生物催化领域的研究热点和前沿,也是众多研究者致力解决的难点.研究和开发新型的纯化、固定化及提升催化性能的方法,降低纯化及储存等设备的要求及生产成本,对酶大规模应用具有重要意义.文中将铁蛋白(ferritin)与目标酶(地衣多糖酶)基因融合,经高效表达后,在细胞内 自发形成无载体固定...     

Carbon nanotube clusters as universal bacterial adsorbents and magnetic separation agents

The magnetic susceptibility and high bacterial affinity of carbon nanotube (CNT) clusters highlight their great potential as a magnetic bio‐separation agent. This article reports the CNT clusters' capability as “universal” bacterial adsorbents and magnetic separation agents by designing and testing a multiwalled carbon nanotube (MWNT) cluster‐based process for bacterial capturing and separation. The reaction system consisted of large clusters of MWNTs for bacterial capture and an external magnet for bio‐separation. The designed system was tested and optimized using Escherichia coli as a model bacterium, and further generalized by testing the process with other representative strains of both gram‐positive and gram‐negative bacteria. For all strains tested, bacterial adsorption to MWNT clusters occurred spontaneously, and the estimated MWNT clusters' adsorption capacities were nearly the same regardless of the types of strains. The bacteria‐bound MWNT clusters also responded almost instantaneously to the magnetic field by a rare‐earth magnet (0.68 Tesla), and completely separated from the bulk aqueous phase and retained in the system. The results clearly demonstrate their excellent potential as highly effective “universal” bacterial adsorbents for the spontaneous adsorption of any types of bacteria to the clusters and as paramagnetic complexes for the rapid and highly effective magnetic separations. © 2009 American Institute of Chemical Engineers Biotechnol. Prog., 2010     

Purification of histidine-tagged single-chain Fv-antibody fragments by metal chelate affinity precipitation using thermoresponsive copolymers

Metal chelate affinity precipitation (MCAP) has been successfully developed as a simple purification process for proteins that have affinity for metal ions. The present lack of widespread applications for this technique as compared to immobilized metal affinity chromatography (IMAC) may be related to the scarcity of well-characterized metal affinity macroligands (AML) and their applications to the number of different purification systems. In the present work we describe a detailed study of a new purification system using metal-loaded thermoresponsive copolymers as AML. The copolymers of vinylimidazole (VI) with N-isopropylacrylamide (NIPAM) were synthesized by radical polymerization with imidazole contents of 15 and 24 mol%. When loaded with Cu(II) and Ni(II) ions the copolymers selectively precipitated extracellularly expressed histidine-tagged single-chain Fv-antibody fragments (His(6)-scFv fragments) from the fermentation broth free from E. coli cells. Precipitation was induced by salt at mild temperatures and the bound antibody fragments were recovered by dissolving the protein-polymer complex in EDTA buffer and subsequent reprecipitation of the polymer. His(6)-scFv fragments were purified with yields of 91 and 80% and purification folds of 16 and 21 when Cu(II) and Ni(II) copolymers were used, respectively. The protein precipitation capacity of the Ni(II) copolymer showed a dependence on the VI concentration in the copolymer. The SDS-PAGE pattern showed significant purification of the antibody fragments.