疏水膜色谱法对生物大分子的快速纯化

首次采用自制的分别级合了辛基、丁基、苯基及聚乙二醇-4000的4种常用疏水基团的纤维素疏水膜色谱柱,以键合了辛基、苯基的SepharoseCL－4B凝胶柱为对照,考察了疏水膜色谱柱对牛血清白蛋白（BSA）的动态吸附容量及流速对吸附容量的影响。疏水膜色谱柱对蛋白及酶具有较好的疏水吸附及纯化作用,但吸附容量比相应的琼脂糖凝胶柱低得多。增大流速及降低蛋白溶液质量浓度对疏水膜色谱柱的吸附容量影响较小,这些性能使膜色谱柱非常适合于大体积低质量浓度蛋白溶液（如基团工程培养液）的分离纯化。     

Hydrophobic interaction chromatography for the purification of a mycobacterial heat shock protein of relative molecular mass 60,000.

A recombinant mycobacterial heat shock protein of relative molecular mass 60,000 was purified by hydrophobic interaction chromatography. Chromatographic media with ligands of medium hydrophobicity, such as phenyl-Sepharose, bound too strongly to be used for the purification of this heat shock protein. Butyl-Sepharose, with weak hydrophobicity, allowed binding and elution with decreasing concentrations of ammonium sulphate, but only alkyl-Superose allowed the separation of two similar proteins from the Escherichia coli clone expressing the recombinant heat shock protein (relative molecular mass 60,000) of Mycobacterium bovis BCG. The binding parameters of recombinant human heat shock proteins of relative molecular mass 60,000 and 70,000 indicate that phenyl-Sepharose also binds too strongly for the separation of these two heat shock proteins.     

Affinity elution from a phosphonic acid-Sepharose derivative in the purification of human liver alkaline phosphatase

The compound p-aminobenzylphosphonic acid has been coupled via an azo linkage to tyraminyl-Sepharose 4B. This derivative at pH 6.0 bound most of the protein and all of the alkaline phosphatase in a crude preparation from human liver. The phosphatase was selectively eluted with the substrate 2-naphthylphosphate and a purification of 400-fold obtained. This step, when incorporated into a procedure for the purification of human liver alkaline phosphatase, yielded essentially pure enzyme.     

Characterization of bacterial L-(-)-tyrosine decarboxylase by isoelectric focusing and gel chromatography.

The purification of L-(-)-tyrosine apodecarboxylase (TAD) (E.C. 4.1.1.25), obtained from extracts of cells of Streptococcus faecalis, has been investigated by means of preparative isoelectric focusing, molecular sieve chromatography and hydrophobic interaction chromatography. Isoelectric focusing demonstrated two separate fractions possessing enzyme activity that had pI values of 4.5 and ca. 3.2. In the chromatographic methods, however, the activity was obtained in a single peak. It was found that hydrophobic interaction chromatography on phenyl-Sepharose was particularly suitable for purification purposes. The enzyme is very firmly bound to octyl-Sepharose CL-4B but retains most of its activity even in the bound state.     

GlcNAcstatin: a picomolar, selective O-GlcNAcase inhibitor that modulates intracellular O-glcNAcylation levels

Many phosphorylation signal transduction pathways in the eukaryotic cell are modulated by posttranslational modification of specific serines/threonines with N-acetylglucosamine (O-GlcNAc). Levels of O-GlcNAc on key proteins regulate biological processes as diverse as the cell cycle, insulin signaling, and protein degradation. The two enzymes involved in this dynamic and abundant modification are the O-GlcNAc transferase and O-GlcNAcase. Structural data have recently revealed that the O-GlcNAcase possesses an active site with significant structural similarity to that of the human lysosomal hexosaminidases HexA/HexB. PUGNAc, an O-GlcNAcase inhibitor widely used to raise levels of O-GlcNAc in human cell lines, also inhibits these hexosaminidases. Here, we have exploited recent structural information of an O-GlcNAcase-PUGNAc complex to design and synthesize a glucoimidazole-based inhibitor, GlcNAcstatin, which is a 5 pM competitive inhibitor of enzymes of the O-GlcNAcase family, shows 100000-fold selectivity over HexA/B, and binds to the O-GlcNAcase active site by mimicking the transition state as revealed by X-ray crystallography. This compound is able to raise O-GlcNAc levels in human HEK 293 and SH-SY5Y neuroblastoma cell lines and thus provides a novel, potent tool for the study of the role of O-GlcNAc in intracellular signal transduction pathways.     

Isolation of cytochrome P-450 components from marmoset liver microsomes by high-performance liquid chromatography.

A fast protein liquid chromatographic (FPLC) system with pre-packed and laboratory-packed columns was used for the analytical and preparative isolation of marmoset monkey cytochrome P-450 (P450) and NADPH-P450-reductase. Chromatographic separations also allowed the recovery of cytochrome b5, NADH-b5-reductase and epoxide hydratase. Cholate-solubilized liver microsomes from phenobarbital-induced marmosets were crudely purified on 8-aminooctyl-Sepharose or 6-aminohexyl-Sepharose and then fractionated into several isoenzyme groups using hydroxyapatite. Further purification on Mono S or CM-Sepharose and finally on phenyl-Superose, phenyl-Sepharose or octyl-Sepharose yielded a P450 fraction which was apparently homogeneous as judged by sodium dodecyl sulphate-polyacrylamide gel electrophoresis in the automated Phast system using silver staining. Removal of excess of non-ionic detergent was effected by hydroxyapatite columns, and this was compared with other methods. For the isolation of P450 isoenzymes from untreated marmosets, Mono Q columns were employed and yielded at least two highly purified forms. NADPH-P450-reductase was recovered from the 8-aminooctyl-Sepharose column or crudely fractionated on DEAE-Sepharose Fast Flow. Subsequent purification via 2',5'-ADP-Sepharose and Superose 12 chromatography resulted in a homogeneous preparation.     

Purification of rabbit skeletal muscle troponin C

Troponin C binds to phenyl-Sepharose in the presence of Ca2+ and can be eluted with EDTA. This property was used as an essential step in the purification of this protein from rabbit skeletal muscle. Troponin C was extracted with 6M urea from extensively washed ground muscle. The protein was bound to and eluted from DEAE-Sephadex, fractionated by size on Sephadex G75, and in a final step purified from UV-absorbing non-protein impurities on phenyl-Sepharose. The total yield of electrophoretically pure protein was 60 mg per 100 g of muscle, which is considerably higher than that previously obtained.     

Studies on the chromatographic fractionation of Trichoderma reesei cellulases by hydrophobic interaction

This work reports new studies on cellulases fractionation by hydrophobic interaction chromatography. The purification procedure for the Trichoderma reesei cellulase complex consists of gel permeation chromatography on Sephadex G-25M followed by an ultrafiltration step. The concentrated enzyme solution was then fractionated on Sepharose CL-6B modified by covalent immobilization of 1,4-butanediol diglycidyl ether. The influence of the mobile phase composition on the chromatographic behaviour of the T. reesei cellulase complex was investigated. By using 13% (w/v) ammonium sulphate in eluent buffer, a selective separation of beta-glucosidase with a two-fold increase in specific activity and a recovery of 60% cellobiase activity were obtained. Other commercial hydrophobic supports (octyl- and phenyl-Sepharose) were also tested and compared under the same conditions.     

Effect of Different Purification Techniques on the Characteristics of Heteropolysaccharide-Protein Biopolymer from Durian (<em>Durio zibethinus</em>) Seed

Natural biopolymers from plant sources contain many impurities (e.g., fat, protein, fiber, natural pigment and endogenous enzymes), therefore, an efficient purification process is recommended to minimize these impurities and consequently improve the functional properties of the biopolymer. The main objective of the present study was to investigate the effect of different purification techniques on the yield, protein content, solubility, water- and oil-holding capacity of a heteropolysaccharide-protein biopolymer obtained from durian seed. Four different purification methods using different chemicals and solvents (i.e., A (isopropanol and ethanol), B (isopropanol and acetone), C (saturated barium hydroxide), and D (Fehling solution)] to liberate the purified biopolymer from its crude form were compared. In most cases, the purification process significantly (p < 0.05) improved the physicochemical properties of heteropolysaccharide-protein biopolymer from durian fruit seed. The present work showed that the precipitation using isopropanol and acetone (Method B) resulted in the highest purification yield among all the tested purification techniques. The precipitation using saturated barium hydroxide (Method C) led to induce the highest solubility and relatively high capacity of water absorption. The current study reveals that the precipitation using Fehling solution (Method D) most efficiently eliminates the protein fraction, thus providing more pure biopolymer suitable for biological applications.     

Oligonucleotide trapping method for purification of transcription factors

Initial purification of two serotypic variants of recombinant botulinum neurotoxin toxin heavy chain fragment [rBoNT(Hc)], produced intracellularly in the yeast Pichia pastoris, using hydrophobic charge induction chromatography (HCIC) is reported. HCIC employs a matrix containing a weakly ionizable ligand that binds proteins through hydrophobic interactions at neutral pH and elutes the proteins by charge repulsion at acidic pH. HCIC optimization led to different purification conditions for each of the proteins even though they have 58% sequence similarity. The HCIC resin has a higher affinity for the fragment of serotype A than that of serotype B. The 10% dynamic breakthrough capacity for the serotype A fragment is >12.5 mg per ml of resin and is approximately 3.5 mg or the serotype B fragment per ml of resin. Stable elution conditions are also different for the two serotypes. The serotype A fragment is unstable when citrate is used to elute the product. However the serotype B fragment is stable when eluted with citrate buffer, and it is further purified by a overnight precipitation caused by the citrate buffer. This paper reports the development strategy, dynamic capacity breakthrough curves, resin and separation reproducibility, and preliminary scale-up data. The summation of the data demonstrates that HCIC is a scaleable process step for biopharmaceutical production of rBoNT(Hc) proteins.     

Selective elution of soluble rat liver glutathione transferases from a glutathione-Sepharose affinity column

Glutathione transferases (GST) are dimeric enzymes that take part in many detoxification processes. A previous report described the use of a glutathione-Sepharose affinity matrix for the purification of human liver GST. The method involved the use of 5 mM glutathione in a high pH buffer, and the yields were nearly 100%. This method and adapted techniques have now been applied to rat liver GST. Selective GST elution can be obtained in several different ways: by stepwise change of the pH and/or glutathione concentration, and by linear gradient elution. Gel electrophoresis showed, however, that none of the fractions contained pure GST isoenzymes. Also, less than 50% of the total rat liver GST was eluted with 5 mM glutathione, in contrast to the results with human liver GST. A glutathione concentration of 30 mM is necessary for quantitative desorption of rat liver GST from a glutathione-Sepharose column.     

Drugs Targeting the A3 Adenosine Receptor: Human Clinical Study Data

The A3 adenosine receptor (A3AR) is overexpressed in pathological human cells. Piclidenoson and namodenoson are A3AR agonists with high affinity and selectivity to A3AR. Both induce apoptosis of cancer and inflammatory cells via a molecular mechanism entailing deregulation of the Wnt and the NF-κB signaling pathways. Our company conducted phase I studies showing the safety of these 2 molecules. In the phase II studies in psoriasis patients, piclidenoson was safe and demonstrated efficacy manifested in significant improvements in skin lesions. Namodenoson is currently being developed to treat liver cancer, where prolonged overall survival was observed in patients with advanced liver disease and a Child–Pugh B score of 7. A pivotal phase III study in this patient population has been approved by the FDA and the EMA and is currently underway. Namodenoson is also being developed to treat non-alcoholic steatohepatitis (NASH). A Phase IIa study has been successfully concluded and showed that namodenoson has anti-inflammatory, anti-fibrosis, and anti-steatosis effects. A phase IIb study in NASH is currently enrolling patients. In conclusion, A3AR agonists are promising drug candidates in advanced stages of clinical development and demonstrate safety and efficacy in their targeted indications.     

Structural and functional characterization of calelectrins from bovine liver.

Two Ca2(+)-dependent membrane-binding proteins with apparent molecular weights of 70000 (calelectrin70) and 32000 (calelectrin32) were isolated from bovine liver using phenyl-Sepharose affinity chromatography followed by diethylaminoethyl (DEAE)-cellulose and Ultrogel AcA44 chromatographies. Limited proteolysis and immunological analyses indicated that calelectrin32 was not a digested product from calelectrin70. Both calelectrins bound to phosphatidylserine and to calmodulin in a Ca2(+)-dependent manner. Circular dichroism studies showed that the apparent alpha-helical contents of calelectrin70 and calelectrin32 were 25 and 40%, respectively and they underwent Ca2(+)-dependent conformational changes. When the calelectrins were incubated with a brain microtubule preparation, they were phosphorylated by endogenous kinase(s) and phosphorylation occurred on serine residues. Moreover, calelectrin70 showed an inhibitory action on endogenous kinase activity in the presence of Ca2+.     

Integrated process for the purification of antibodies combining aqueous two-phase extraction, hydrophobic interaction chromatography and size-exclusion chromatography

We have evaluated a process incorporating aqueous two-phase extraction, hydrophobic interaction chromatography (HIC) and size-exclusion chromatography (SEC) for the purification of human immunoglobulin G (IgG) from a Chinese hamster ovary (CHO) cell supernatant. These unit operations were chosen not only for allowing the removal of target impurities but also for facilitating the integration of different process units without the need for any conditioning step. Extraction in aqueous two-phase systems (ATPSs), composed of polyethylene glycol (PEG) and sodium citrate, allowed the concentration of the antibodies in the citrate-rich phase and the removal of the most hydrophobic compounds in the PEG-rich phase. An ATPS composed of 10% (w/w) PEG 3350 and 12% (w/w) citrate, at pH 6, allowed the recovery of IgG with a 97% yield, 41% HPLC purity and 72% protein purity. This bottom phase was then directly loaded on a phenyl-Sepharose HIC column. This intermediate purification step allowed the capture of the antibodies using a citrate mobile phase with 99% of the antibody recovered in the elution fractions, with 86% HPLC purity and 91% protein purity. Finally, SEC allowed the final polishing by removing IgG aggregates. HIC-eluted fractions were directly injected in a Superose 6 size-exclusion column affording a 100% pure IgG solution with 90% yield.     

Purification of labelled antibodies by hydrophobic interaction chromatography

In order to improve the sensitivity of immunometric assays, a chromatographic technique was developed that virtually eliminates components causing non-specific background. Labelled antibodies were applied to a phenyl-Sepharose column in physiological buffer. When labelled anitbodies were purified by this technique, the non-specific background of various time-resolved immunofluorometric assays was reduced 3- to 10-fold and was very close to the instrument background. The assay sensitivity was simultaneously increased by a factor of 2 to 16. This purification method might be used to improve the results of immunometric assays in general.     

Immobilized metal affinity composite membrane based on cellulose for separation of biopolymers

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猪肝中单胺氧化酶B的分离纯化

依据单胺氧化酶B(monoamine oxidase B, MAOB)的疏水特性,建立了一种从猪肝中分离纯化MAOB的新方法。用含有1% Triton X-100的膜蛋白裂解液制备粗酶,以饱和度为20%～50%的硫酸铵反抽提进行粗提,再利用自制的配基密度为75.7 μmol/mL的苯基疏水色谱及Sepharose Q High Performance离子交换色谱进一步分离纯化,得到纯化倍数为18.2、酶比活为135 U/mg的MAOB。十二烷基硫酸钠-聚丙烯酰胺凝胶电泳(SDS-PAGE)分析显示为相对分子质量约60 000的单一蛋白质带。采用高效液相色谱-电喷雾串联质谱对该酶进行鉴定,证实为MAOB。本研究所用分离纯化方法可以有效纯化MAOB, 为MAOB的深入研究提供技术支撑。     

Purification of soluble acetylcholinesterase from sheep liver by affinity chromatography

The purpose of this study was to develop a protocol for the purification of acetylcholinesterase (AChE, acetylcholine acetylhydrolase, E.C.3.1.1.7) enzyme and to extend a purification method for further enzyme characterization. A further aim was to study whether the edrophonium’s pharmacologic action is due primarily to the inhibition or inactivation of AChE at sites of cholinergic transmission. The purification of a soluble AChE from sheep liver using affinity chromatography on Concanavalin A–Sepharose 4B and edrophonium–Sepharose 6B is studied. The affinity matrix was synthesized by coupling an inhibitor edrophonium to epoxy-activated Sepharose at flow rate of 0.5 ml/min. AChE is a pivotal enzyme in the cholinergic nervous system. Its primary function is to catalyze hydrolysis of released acetylcholine (ACh) and thus maintain homeostasis of this neurotransmitter in the central and peripheral nervous systems. Hence, AChE is important in both pharmacological and toxicological mechanisms. It was purified 842-fold with a specific activity of 21 U/mg protein. Sodium dodecyl sulfate (SDS) electrophoresis resulted in a monomeric molecular weight of 67.04 kDa, while on gel chromatography using Sephacryl S-200 under nondenaturing conditions to be 201.5 kDa. Based on the molecular weight obtained by gel filtration, the purified AChE was assumed to be a tetrameric form.     

Evaluation of protein-A chromatography media

In process-scale antibody purification, protein-A affinity chromatography is commonly used as the initial purification step. In this paper, two different protein-A media were evaluated. These adsorbents have a porous glass backbone with different pore sizes: 700 A and 1000 A. Adsorption equilibrium data of human immunoglobulins on these media were measured via a batch technique and correlated using the Langmuir isotherm model. A larger static capacity was found for the smaller pore size material, which is probably a result of the larger specific surface area and associated higher ligand concentration. The protein uptake kinetics were also obtained via a stirred tank experiment using different initial protein concentrations. A surface layer model was used to represent the protein uptake by the media and to estimate values of a concentration-independent effective diffusivity within the particle. Experimental breakthrough curves were also obtained from packed beds operated under different conditions. Calculated breakthrough profiles were found to be in good agreement with the experimental results. Experimental breakthrough data were used to determine the dependence of the dynamic capacity of the media as a function of the fluid residence time. A larger dynamic capacity was also found for the smaller pore size media. The permeability of large scale packed beds was also reported and used in conjunction with the dynamic capacity to calculate the process production rate.