High-throughput protein purification under denaturating conditions by the use of cation exchange chromatography

A high-throughput protein purification strategy using the polycationic Z(basic) tag has been developed. In order for the strategy to be useful both for soluble and less soluble proteins, a denaturating agent, urea, was used in all purification steps. First, four target proteins were genetically fused to the purification tag, Z(basic). These protein constructs were purified by cation exchange chromatography and eluted using a salt gradient. From the data achieved, a purification strategy was planned including stepwise elution to enable parallel protein purification using a laboratory robot. A protocol that includes all steps, equilibration of the chromatography resin, load of sample, wash, and elution, all without any manual handling steps, was handled by the laboratory robot. The program allows automated purification giving milligram amounts of pure recombinant protein of up to 60 cell lysates. In this study 22 different protein constructs, with different characteristics regarding pI and solubility, were successfully purified by the laboratory robot. The data show that Z(basic) can be used as a general purification tag also under denaturating conditions. Moreover, the strategy enables purification of proteins with different pI and solubility using ion exchange chromatography (IEXC). The procedure is highly reproducible and allows for high protein yield and purity and is therefore a good complement to the commonly used His(6)-tag.     

Single-step recovery and solid-phase refolding of inclusion body proteins using a polycationic purification tag

A strategy for purification of inclusion body-forming proteins is described, in which the positively charged domain Z(basic) is used as a fusion partner for capture of denatured proteins on a cation exchange column. It is shown that the purification tag is selective under denaturing conditions. Furthermore, the new strategy for purification of proteins from inclusion bodies is compared with the commonly used method for purification of His(6)-tagged inclusion body proteins. Finally, the simple and effective means of target protein capture provided by the Z(basic) tag is further successfully explored for solid-phase refolding. This procedure has the inherited advantage of combining purification and refolding in one step and offers the advantage of eluting the concentrated product in a suitable buffer.     

金黄色葡萄球菌蛋白A (SpA) Z结构域串联体的克隆、表达和筛选

筛选一种高效重组金黄色葡萄球菌蛋白A(SpA)用于制备抗体纯化亲和介质。首先通过基因操作获得金黄色葡萄球菌蛋白A(SpA)的Z结构域单体、二串体、三串体、四串体和五串体基因,将目的基因分别克隆至pET-22b表达载体并转化至大肠杆菌BL21(DE3)感受态细胞,获得不同串联个数的Z结构域基因工程菌,经诱导表达和Ni2+亲和层析纯化得到Z结构域单体和二-五串体蛋白。纯化后的目的蛋白偶联至琼脂糖凝胶作为亲和层析介质,对人免疫球蛋白G(IgG)进行分离纯化。分析比较Z结构域串联体蛋白产量及其偶联的亲和介质对抗体吸附载量的差异。结果表明,构建的Z结构域单体、二串体、三串体、四串体和五串体基因工程菌能有效表达目的蛋白,制备的凝胶亲和介质可特异性吸附人IgG。增加Z结构域串联数,重组蛋白产量和单位摩尔数多聚体蛋白吸附载量获得提高,其中,重组四串体蛋白产量大(160 mg/10 g湿菌体),对抗体的吸附载量高(34.4 mg人IgG/mL胶),更适合作为配基用于亲和层析介质的制备。     

Enzymatic cleavage of fusion proteins using immobilised protease 3C

A strategy for efficient cleavage of fusion proteins using an immobilised protease has been developed. Protease 3C from coxsackie virus was recombinantly produced in Escherichia coli and covalently immobilised onto a solid support. Thereafter, Z(basic) tagged fusion proteins, with a specific cleavage sequence between the domains, were flown through the proteolytic column and circulated until complete cleavage. Subsequently, the processed protein solution was applied on a cation exchanger. Thereby, removal of the released, positively charged fusion tag, Z(basic), was done by adsorption to the matrix while the target proteins were recovered in the flow through. Interestingly, the columns were shown to be reusable without any measurable decrease in activity. Moreover, after storage in 4 degrees C for two months the activity was almost unaffected.     

Toward pyrosequencing on surface-attached genetic material by use of DNA-binding luciferase fusion proteins

Mutation detection and single-nucleotide polymorphism genotyping require screening of large samples of materials and therefore the importance of high-throughput DNA analysis techniques is significant. Pyrosequencing is a four-enzyme bioluminometric DNA sequencing technology based on the sequencing-by-synthesis principle. Currently, the technique is limited to simultaneous analysis of 96 or 384 samples. Earlier, attempts to increase the sample capacity were made using micromachined filter chamber arrays where parallel analyses of nanoliter samples could be monitored in real time. We have developed a strategy for specific immobilization of the light-producing enzyme luciferase to the DNA template within a reaction chamber. By this approach, luciferase is genetically fused to a DNA-binding protein (Klenow polymerase or Escherichia coli single-stranded DNA-binding (SSB) protein) and to a purification handle (Z(basic)). The proteins are produced in E. coli and purified using cation and anion exchange chromatography with removal of Z(basic). The produced proteins have been analyzed using an assay for complete primer extension of DNA templates immobilized on magnetic beads detected by pyrosequencing chemistry. Results from these experiments show that the proteins bind selectively to the immobilized DNA and that their enzymatic domains were active. Z(basic)-SSB-luciferase produced the highest signal in this assay and was further exploited as enzymatic reagent for DNA sequencing.     

Expression and purification of human urodilatin by small ubiquitin-related modifier fusion in Escherichia coli

To prevent in vivo degradation, small peptides are usually expressed in fusion proteins from which target peptides can be released by proteolytic or chemical reagents. In this report, small ubiquitin-related modifier (SUMO) linked with a hexa-histidine tag was used as a fusion partner for the production of recombinant human urodilatin, a hormone for the treatment of acute decompensated heart failure. The fusion protein, which was overexpressed mainly as inclusion bodies in Escherichia coli, constituted about 25% of the total cell proteins. After purification by Ni-sepharose affinity chromatography and renaturation in refolding buffer, the fusion protein was cleaved with SUMO protease 1. Urodilatin was separated from the fusion partner by the subtractive chromatography using Ni-sepharose once again, and then further purified with reverse-phase high performance liquid chromatography. In vitro activity assay demonstrated that the recombinant urodilatin had a potent vasodilatory effect on rabbit aortic strips with an EC₅₀ of 1.77 ± 0.53 μg/ml, which was similar to that of the synthetic urodilatin standard. The expression strategy presented in this study allows convenient high yield and easy purification of small recombinant peptides with native sequences. Z. Sun and Z. Xia contribute equally to the work.     

Is there a rational method to purify proteins? From expert systems to proteomics

The purification of recombinant proteins for therapeutic or analytical applications requires the use of several chromatographic steps in order to achieve a high level of purity. A range of techniques is available such as anion and cation exchange chromatography, which can be carried out at different pHs, and hence used at different steps, hydrophobic interaction chromatography, gel filtration and affinity chromatography. Evidently when confronted with a complex mixture of partially unknown proteins or a clarified cell extract there are many different routes one can take in order to choose the minimum and most efficient number of purification steps to achieve a desired level of purity (e.g. 98, 99.5 or 99.9%). In this review we will show how an initial "proteomic" characterization of the complex initial mixture of target protein and protein contaminants can be used to select the most efficient chromatographic separation steps in order to achieve a maximum level of purity with a minimum number of steps. The chosen methodology was implemented in a computer based expert system. The first algorithm developed was used to select the most efficient purification method to separate a protein from its contaminants based on the physicochemical properties of the protein product and the protein contaminants. The second algorithm developed was used to predict the number and concentration of contaminants after each separation as well as protein product purity. The successful application of the expert system approach, based on an initial proteomic characterization, to the practical cases of protein mixtures and clarified fermentation supernatant is presented and discussed. The purification strategy proposed was experimentally tested and validated with a mixture of four proteins and the experimental validation was also carried out with an "unknown" supernatant of Bacillus subtilis producing a recombinant beta-1,3-glucanase. The system was robust to errors <10% which is the range that can be found in the experimental determination of the properties in the database of product and contaminants. On the other hand, the system was sensitive both to larger variations (>20%) in the properties of the contaminant database and the protein product and to variations in one protein property (e.g. hydrophobicity).     

Strategies for the purification and on-column cleavage of glutathione-S-transferase fusion target proteins

In this report, we describe a flexible, efficient and rapid protein purification strategy for the isolation and cleavage of glutathione-S-transferase (GST) fusion proteins. The purification and on-column cleavage strategy was developed to work for the purification of difficult proteins and for target proteins where efficient fusion-tag cleavage is essential for downstream processes, such as structural and functional studies. To test and demonstrate the flexibility of this method, seven diverse unrelated target proteins were assayed. A purification technique is described that can be applied to a wide range of both soluble and membrane inserted recombinant target proteins of differing function, structure and chemical nature. This strategy is performed in a single chromatographic step applying an on-column cleavage method, yielding "native" proteins in the 200 microg to 40 mg/l scale of 95-98% purity.     

S-Zephyr, a new high performance ion exchange chromatography column matrix.

S-Zephyr, a new column material for high performance cation exchange chromatography of proteins, is compared with Mono-S. The comparison is based on a retentivity study, a model separation of an artificial protein mixture, a sample load capacity experiment and the development of the separation performance at a column overload situation. S-Zephyr is found to be a good matrix for cation exchange chromatography, for analytical separations as well as for small and large scale protein purification applications.     

Towards higher-throughput membrane protein production for structural genomics initiatives

Integral membrane proteins present unparalleled challenges for structural genomics programs. Samples from this class of proteins are not only difficult to produce in quantities sufficient for analysis by X-ray diffraction or NMR, but their hydrophobic properties add extra dimension to their purification and subsequent crystallization. New systems that seek to tackle the production problems are in development. In our laboratory, one such strategy exploits the unique physiology of the Rhodobacter species of photosynthetic bacteria where we have designed an overexpression system that coordinates the heterologous production of targeted hydrophobic proteins with nascent, unfilled membranes that can be used to harbor them. In this study, we describe the means by which purification of recombinant membrane proteins produced in such a fashion can be purified efficiently from Rhodobacter membranes using relatively higher-throughput, semi-automated methods. These protocols utilize a state-of-the-art FPLC system for affinity chromatography, followed by gel filtration or ion exchange chromatography to enhance purity for crystallization attempts. The Rhodobacter expression system coupled with the semi-automation of purification steps represents an advance towards the development of a strategy for obtaining structures for membrane proteins at a more rapid pace.     

A multipurpose fusion tag derived from an unstructured and hyperacidic region of the amyloid precursor protein

Expression and purification of aggregation‐prone and disulfide‐containing proteins in Escherichia coli remains as a major hurdle for structural and functional analyses of high‐value target proteins. Here, we present a novel gene‐fusion strategy that greatly simplifies purification and refolding procedure at very low cost using a unique hyperacidic module derived from the human amyloid precursor protein. Fusion with this polypeptide (dubbed FATT for Flag‐Acidic‐Target Tag) results in near‐complete soluble expression of variety of extracellular proteins, which can be directly refolded in the crude bacterial lysate and purified in one‐step by anion exchange chromatography. Application of this system enabled preparation of functionally active extracellular enzymes and antibody fragments without the need for condition optimization.     

Fractionation of two protein kinases from avian myeloblastosis virus and characterization of the protein kinase activity preferring basic phosphoacceptor proteins.

Two protein kinase activities were fractionated from purified virions of avian myeloblastosis virus. Distinguishing characteristics of these two protein kinases included: (i) their binding properties during purification by ion-exchange chromatography; (ii) their estimated molecular weights; and (iii) their phosphoacceptor protein specificities. The protein kinase that bound to the anion exchanger DEAE-cellulose (pH 7.2) had an estimated molecular weight of 60,000 to 64,000 and preferred basic phosphoacceptor proteins. The protein kinase that bound to the cation exchanger phosphocellulose (pH 7.2) had an estimated molecular weight of 42,000 to 46,000 and preferred acidic phosphoacceptor proteins. The protein kinase preferring basic phosphoacceptor proteins was further purified and characterized. Optimal transfer of phosphate catalyzed by this enzyme required a divalent metal ion, a sulfhydryl-reducing agent, and ATP as phosphate donor. GTP was not an effective phosphate donor at concentrations comparable to ATP; and the cyclic nucleotides cyclic AMP and cyclic GMP neither stimulated nor inhibited protein phosphorylation by the protein kinase. The specificity of the protein kinase for basic phosphoacceptor proteins extended to proteins from avian myeloblastosis virus, in that the neutral to basic virion proteins p12, p19, and p27 served as phosphate acceptors. In addition, the protein kinase also appeared to phosphorylate itself. The role(s) of this virion-associated protein kinase is discussed.     

Routine manufacture of recombinant proteins using expanded bed adsorption chromatography

Two different recombinant human proteins were purified directly from Pichia pastoris whole cell fermentation broth, containing 30–44% biomass (wet weight percent), by strong cation exchange expanded bed adsorption chromatography. Expanded bed adsorption chromatography provided clarification, product purification and product concentration in a single unit operation at large scale (2000-l nominal fermentation volume). The efficiency of expanded bed adsorption chromatography resulted in a short process time, high process yield, and limited proteolytic degradation of the target proteins. The separations were operated using a 60-cm (d) column run at 14 l/min. For one protein, expanded bed adsorption chromatography resulted in an average product recovery of 113% (relative to fermentation supernatant) and a purity of 89% (n=10). For the other protein, the average product recovery was 99% (relative to fermentation supernatant) and the purity was 62.1 (n=10). Laboratory experiments showed that biomass reduced product dynamic binding capacity for protein 2.     

包涵体蛋白的分离和色谱法体外复性纯化研究进展

重组蛋白在大肠杆菌中表达多为无活性的包涵体形式,须经洗涤、溶解、复性后才能得到生物活性蛋白。综述了近年来包涵体蛋白分离纯化和复性技术研究进展,重点讨论了色谱法复性技术的应用,包括尺寸排阻色谱、亲和色谱、离子交换色谱、疏水相互作用色谱、固定化脂质体色谱、扩张床吸附色谱的进展情况。     

Comparison of strong cation exchange and SDS-PAGE fractionation for analysis of multiprotein complexes

Affinity purification of protein complexes followed by identification using liquid chromatography/mass spectrometry (LC-MS/MS) is a robust method to study the fundamental process of protein interaction. Although affinity isolation reduces the complexity of the sample, fractionation prior to LC-MS/MS analysis is still necessary to maximize protein coverage. In this study, we compared the protein coverage obtained via LC-MS/MS analysis of protein complexes prefractionated using two commonly employed methods, SDS-PAGE and strong cation exchange chromatography (SCX). The two complexes analyzed focused on the nuclear proteins Bmi-1 and GATA3 that were expressed within the cells at low and high levels, respectively. Prefractionation of the complexes at the peptide level using SCX consistently resulted in the identification of approximately 3-fold more proteins compared to separation at the protein level using SDS-PAGE. The increase in the number of identified proteins was especially pronounced for the Bmi-1 complex, where the target protein was expressed at a low level. The data show that prefractionation of affinity isolated protein complexes using SCX prior to LC-MS/MS analysis significantly increases the number of identified proteins and individual protein coverage, particularly for target proteins expressed at low levels.     

Design of affinity tags for one-step protein purification from immobilized zinc columns

Affinity tags are often used to accomplish recombinant protein purification using immobilized metal affinity chromatography. Success of the tag depends on the chelated metal used and the elution profile of the host cell proteins. Zn(II)-iminodiacetic acid (Zn(II)-IDA) may prove to be superior to either immobilized copper or nickel as a result of its relatively low binding affinity for cellular proteins. For example, almost all Escherichia coli proteins elute from Zn(II)-IDA columns between pH 7.5 and 7.0 with very little cellular protein emerging at pH values lower than 7.0. Thus, a large portion of the Zn(II)-IDA elution profile may be free of contaminant proteins, which can be exploited for one-step purification of a target protein from raw cell extract. In this paper we have identified several fusion tags that can direct the elution of the target protein to the low background region of the Zn(II)-IDA elution profile. These tags allow targeting of proteins to different regions of the elution profile, facilitating purification under mild conditions.     

Metal-chelate affinity precipitation of proteins using responsive polymers

Affinity precipitation of proteins uses polymers capable of reversible soluble-insoluble transitions in response to small environmental changes (temperature, pH or solvent composition). Here we describe protocols for (i) the synthesis of responsive polymers with specific affinity to target proteins and (ii) the purification of proteins using these polymers. The purification is based on precipitation of the affinity complex between the protein and the polymer, which is induced by environmental changes. This separation strategy is simpler and more cost effective than conventional affinity column chromatography. Specifically, we describe the synthesis of thermoresponsive 1-vinylimidazole:N-isopropylacrylamide copolymers. The whole procedure takes 2-3 h when applied to purification of recombinant His-tag proteins or proteins with natural metal binding groups by means of metal chelate affinity precipitation. Optimization of the polymer composition and the type of chelating ions allows for target protein yields of 80% and higher.     

Identification and Monitoring of Host Cell Proteins by Mass Spectrometry Combined with High Performance Immunochemistry Testing

Biotherapeutics are often produced in non-human host cells like Escherichia coli, yeast, and various mammalian cell lines. A major focus of any therapeutic protein purification process is to reduce host cell proteins to an acceptable low level. In this study, various E. coli host cell proteins were identified at different purifications steps by HPLC fractionation, SDS-PAGE analysis, and tryptic peptide mapping combined with online liquid chromatography mass spectrometry (LC-MS). However, no host cell proteins could be verified by direct LC-MS analysis of final drug substance material. In contrast, the application of affinity enrichment chromatography prior to comprehensive LC-MS was adequate to identify several low abundant host cell proteins at the final drug substance level. Bacterial alkaline phosphatase (BAP) was identified as being the most abundant host cell protein at several purification steps. Thus, we firstly established two different assays for enzymatic and immunological BAP monitoring using the cobas® technology. By using this strategy we were able to demonstrate an almost complete removal of BAP enzymatic activity by the established therapeutic protein purification process. In summary, the impact of fermentation, purification, and formulation conditions on host cell protein removal and biological activity can be conducted by monitoring process-specific host cell proteins in a GMP-compatible and high-throughput (> 1000 samples/day) manner.     

Characterization of polycationic amino acids fusion systems for ion-exchange purification of cyclodextrin glycosyltransferase from recombinant Escherichia coli

Fusion proteins with charged polycationic amino acid tails were constructed for the purpose of simple ion-exchange purification with high purity. A number of positively charged lysine and arginine tails were fused to the C-terminus of cyclodextrin glycosyltransferase (CGTase) derived from Bacillus macerans and expressed in Escherichia coli. The ionic binding forces provided by the tails allowed the selective recovery of CGTase from recombinant E. coli cell extracts, while CGTase by itself could not bind to the cation exchanger at neutral pH. The type of amino acids used and the length of the tail directly affected the purification factors. Most intracellular proteins of E. coli adsorbed on the cation exchanger could be removed by washing with 400 mM NaCl solution at pH 7.4, suggesting that a fusion partner suitable for purification purpose should be provided with high binding strength and the maintenance of adsorption by washing with NaCl solution. Among the fusion CGTases constructed, the CGTK10ase containing 10 lysine residues provided sufficiently high binding strength to allow purification to its homogeneity through simple ion-exchange chromatography.