Targeted expression,purification, and cleavage of fusion proteins from inclusion bodies in Escherichia coli

Today, proteins are typically overexpressed using solubility-enhancing fusion tags that allow for affinity chromatographic purification and subsequent removal by site-specific protease cleavage. In this review, we present an alternative approach to protein production using fusion partners specifically designed to accumulate in insoluble inclusion bodies. The strategy is appropriate for the mass production of short peptides, intrinsically disordered proteins, and proteins that can be efficiently refolded in vitro.     

Secretion and affinity purification of glutathione S-transferase fusion proteins from yeast

Summary Sequences encoding GST-fusion proteins were cloned into the Saccharomyces cerevisiae secretion vector, pYEX-S1, to direct secretion into the culture medium. GST and metallothionein fused to GST were secreted successfully and the fusion proteins purified. With several other GST-fusion proteins however, the proteins were retained inside the cell, indicating limitations to the types of proteins that can be secreted from yeast.     

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.     

Single-process expression and purification of multiple recombinant proteins through cocultivation and affinity purification

Multiple recombinant proteins can be expressed simultaneously by inoculating multiple seed cultures into a single growth medium and inducing protein expression at a single time point. Up to three recombinant proteins can be individually purified from such a mixed culture (cocultivation) through the use of a combination of a multihistidine and a modified intein as affinity tags and the Ni sepharose and chitin as affinity matrices. This method may facilitate the study of protein complexes by rapidly obtaining multiple protein components in a single process and may potentially increase the efficiency of recombinant protein production at research and industrial scales.     

Purification of GFP fusion proteins with high purity and yield by monoclonal antibody-coupled affinity column chromatography

GFP has often been used as a marker of gene expression, protein localization in living and fixed tissues as well as for protein targeting in intact cells and organisms. Monitoring foreign protein expression via GFP fusion is also very appealing for bioprocess applications. Many cells, including bacterial, fungal, plant, insect and mammalian cells, can express recombinant GFP (rGFP) efficiently. Several methods and procedures have been developed to purify the rGFP or recombinant proteins fused with GFP tag. However, most current GFP purification methods are limited by poor yields and low purity. In the current study, we developed an improved purification method, utilizing a FMU-GFP.5 monoclonal antibody (mAb) to GFP together with a mAb-coupled affinity chromatography column. The method resulted in a sample that was highly pure (more than 97% homogeneity) and had a sample yield of about 90%. Moreover, the GFP epitope permitted the isolation of almost all the active recombinant target proteins fused with GFP, directly and easily, from the crude cellular sources. Our data suggests this method is more efficient than any currently available method for purification of GFP protein.     

Two-step metal affinity purification of double-tagged (NusA-His6) fusion proteins

The present purification protocol applies to target proteins that are fused to a double tag, such as NusA-His6, through a linker that includes a protease-recognition sequence. It involves two steps of immobilized metal ion affinity chromatography (IMAC). NusA stabilizes the passenger protein during translation, whereas the His-tag enables affinity purification of the fusion. The eluate resulting from the first IMAC is buffer-exchanged to remove the imidazole and to achieve optimal conditions for the enzymatic cleavage performed by a His-tagged recombinant protease. The digested sample is loaded directly for a second IMAC step and the target protein is selectively recovered in the flow-through. The resin binds residual non-digested fusion protein, double-tagged moiety, protease and any contaminant that bound the affinity resin and was eluted from the first IMAC. The purity of the target protein usually makes a further purification step unnecessary for most of the lab applications. It takes less than 5 hours to purify the protein from a 5 g pellet.     

Partial purification of guinea pig MIF by affinity column chromatography using macrophages.

First we have confirmed the previous observation that the macrophage migration inhibitory factor (MIF) was adsorbed on normal peritoneal macrophages when they were incubated at 4 C for 60 min. It was found that macrophages fixed with 2% glutaraldehyde gave more reproducible results than viable cells in terms of "adsorption" of guinea pig MIF. The adsorption was achieved more completely at 37 C than at 4 C, indicating that this reaction is a temperature-dependent phenomenon. Using these glutaraldehyde-fixed macrophages, a kind of cell-affinity column was successfully developed. The guinea pig MIF preparation lost its activity when it was passed through this affinity column, and MIF adsorbed on the column was recovered by elution with 0.1 M (L)-fucose of 0.1 M (D)-glucose. Such MIF active eluate was found to be at least 30--40 fold more pure than the original MIF preparation which had been previously fractionated according to its molecular weight. Therefore, this type of macrophage-affinity column may be useful for the purification of MIF.     

Vectors for expression of proteins with single or combinatorial fluorescent protein and tandem affinity purification tags in Dictyostelium

The human tumour suppressor P53 is a key protein involved in tumour suppression. P53 acts as a "guardian of genome" by regulating many target genes involved in cell cycle regulation, DNA repair and apoptosis. We report the P53 expression by the methylotrophic yeast Pichia pastoris using the methanol inducible AOX1 promoter. We have produced the rP53 in intracellular form as well as secreted using the Saccharomyces cerevisiae alpha-mating factor prepro-leader sequence in two genetic contexts of Pichia, Mut(s) and Mut(+). The intracellular P53 was successfully produced by Mut(s) (KM71) as well as Mut(+) (X33) strains, however, the secreted form was mainly observed in the Mut(s) strain, despite a higher number of p53 copies integrated in the Mut(+) strain. Interestingly, in Mut(s) phenotype, the medium pH influences markedly the rP53 production since it was higher at pH 7 than 6.     

The use of recombinant fusion proteases in the affinity purification of recombinant proteins

In the affinity purification of recombinant fusion proteins, the rate-limiting step is usually the efficient proteolytic cleavage and removal of the affinity tail and the protease from the purified recombinant protein. We have developed a rapid, convenient, and efficient method of affinity purification that can overcome this limitation. In one example of the method, the protease 3C from a picornavirus (3Cpro), which cleaves specific sequences containing a minimum of 6-7 amino acids, has been expressed as a fusion with glutathione S-transferase. The resultant recombinant "fusion protease" cleaves fusion proteins bearing (from the amino-terminus) the same affinity tail as the fusion protease, a 3Cpro cleavage recognition site, and the recombinant protein of interest. The recombinant protein is purified in a single chromatographic step, which removes both the affinity tail and the fusion protease. The advantages over existing methods include much improved specificity of proteolytic cleavage, complete removal of the protease and the affinity tail in one step, and the option of adding any desired amount of fusion protease to ensure efficient cleavage. The potential flexibility of the method is shown by the use of various affinity tails and alternative fusion proteases.     

Cellulose affinity purification of fusion proteins tagged with fungal family 1 cellulose-binding domain

N- or C-terminal fusions of red-fluorescent protein (RFP) with various fungal cellulose-binding domains (CBDs) belonging to carbohydrate binding module (CBM) family 1 were expressed in a Pichia pastoris expression system, and the resulting fusion proteins were used to examine the feasibility of large-scale affinity purification of CBD-tagged proteins on cellulose columns. We found that RFP fused with CBD from Trichoderma reesei CBHI (CBD(Tr)(CBHI)) was expressed at up to 1.2g/l in the culture filtrate, which could be directly injected into the cellulose column. The fusion protein was tightly adsorbed on the cellulose column in the presence of a sufficient amount of ammonium sulfate and was efficiently eluted with pure water. Bovine serum albumin (BSA) was not captured under these conditions, whereas both BSA and the fusion protein were adsorbed on a phenyl column, indicating that the cellulose column can be used for the purification of not only hydrophilic proteins but also for hydrophobic proteins. Recovery of various fusion proteins exceeded 80%. Our results indicate that protein purification by expression of a target protein as a fusion with a fungal family 1 CBD tag in a yeast expression system, followed by affinity purification on a cellulose column, is simple, effective and easily scalable.     

A dual protease approach for expression and affinity purification of recombinant proteins

We describe a new method for affinity purification of recombinant proteins using a dual protease protocol. Escherichia coli maltose binding protein (MBP) is employed as an N-terminal tag to increase the yield and solubility of its fusion partners. The MBP moiety is then removed by rhinovirus 3C protease, prior to purification, to yield an N-terminally His₆-tagged protein. Proteins that are only temporarily rendered soluble by fusing them to MBP are readily identified at this stage because they will precipitate after the MBP tag is removed by 3C protease. The remaining soluble His₆-tagged protein, if any, is subsequently purified by immobilized metal affinity chromatography (IMAC). Finally, the N-terminal His₆ tag is removed by His₆-tagged tobacco etch virus (TEV) protease to yield the native recombinant protein, and the His₆-tagged contaminants are removed by adsorption during a second round of IMAC, leaving only the untagged recombinant protein in the column effluent. The generic strategy described here saves time and effort by removing insoluble aggregates at an early stage in the process while also reducing the tendency of MBP to “stick” to its fusion partners during affinity purification.     

An affinity column for the purification of prenyltransferases

Farnesyl pyrophosphate synthetase (EC 2.5.1.1) from chicken liver, pig liver, and yeast has been purified to homogeneity in a single chromatographic step by affinity chromatography. The affinity ligand, geranylmethylphosphonophosphate, is linked to Affi-Gel 10 through the phosphonophosphate moiety. The affinity gel is stable chemically and the internal phosphonophosphate linkage is not hydrolyzed by nonspecific phosphatases. A single column has been used repeatedly for over a year with no degradation in its performance. A typical purification only requires 2 days and gives a 500- to 600-fold purification of enzyme from a crude ammonium sulfate precipitate.     

Intracellular Targets of Paullones. Identification following affinity purification on immobilized inhibitor

Numerous inhibitors of cyclin-dependent kinases and glycogen synthase kinase-3 (GSK-3) are being developed in view of their potential applications against cancers and neurodegenerative disorders. Among these, paullones constitute a family of potent and apparently selective cyclin-dependent kinase and GSK-3 inhibitors. However, their actual intracellular targets remain to be identified. To address this issue we have immobilized a paullone, gwennpaullone, on an agarose matrix. Extracts from various cell types and tissues were screened for proteins interacting with this matrix. This approach validated GSK-3alpha and GSK-3beta as major intracellular paullone targets and also mitochondrial, but not cytoplasmic, malate dehydrogenase (MDH). Mitochondrial MDH was indeed inhibited by micromolar concentrations of paullones. Mitochondrial MDH was the major paullone-binding protein in the parasitic protozoon Leishmania mexicana, and paullones inhibited growth of the parasite. This simple batchwise affinity chromatography approach constitutes a straightforward method for the identification of intracellular targets of this particular class of novel anti-mitotic compounds. It has revealed an unexpected target, mitochondrial MDH, the inhibition of which may participate in the pharmacological effects of paullones.     

Removal of cleavage slow points from affinity tags used in the IMAC purification of recombinant proteins

The complete enzymatic removal of affinity tags from tagged recombinant proteins is often required but can be challenging when slow points for cleavage exist. This study documents a general approach to remove N‐terminal tags from recombinant proteins specifically designed to be efficiently captured by IMAC resins. In particular, site‐directed mutagenesis procedures have been used to modify the amino acid sequence of metal binding tags useful in IMAC purifications of recombinant proteins with the objective to increase cleavage efficiency with the exopeptidase, dipeptidyl aminopeptidase 1. These tags were specifically developed for application with borderline metal ions, such as Ni²⁺ or Cu²⁺ ions, chelated to the immobilized ligands, 1,4,7‐triazacyclononane (tacn) and its analogs. Due to the ability to control cleavage site structure and accessibility via site directed mutagenesis methods, these procedures offer considerable scope to obtain recombinant proteins with authentic native N‐termini, thus avoiding any impact on structural stability, humoral and cellular immune responses, or other biological functions. Collectively, these IMAC‐based methods provide a practical alternative to other procedures for the purification of recombinant proteins with tag removal. Overall, this approach is essentially operating as an integrated down‐stream purification capability.     

Thermodynamics of single peptide bond cleavage in bovine pancreatic trypsin inhibitor (BPTI)

A major goal of this paper was to estimate a dynamic range of equilibrium constant for the opening of a single peptide bond in a model protein, bovine pancreatic trypsin inhibitor (BPTI). Ten mutants of BPTI containing a single Xaa-->Met substitution introduced in different parts of the molecule were expressed in Escherichia coli. The mutants were folded, purified to homogeneity, and cleaved with cyanogen bromide to respective cleaved forms. Conformation of the intact mutants was similar to the wildtype, as judged from their circular dichroism spectra. Substantial conformational changes were observed on the chemical cleavage of three single peptide bonds--Met46-Ser, Met49-Cys, and Met53-Thr--located within the C-terminal helix. Cleavage of those peptide bonds caused a significant destabilization of the molecule, with a drop of the denaturation temperature by 56.4 degrees C to 68 degrees C at pH 4.3. Opening of the remaining seven peptide bonds was related to a 10.8 degrees C to 39.4 degrees C decrease in T(den). Free energies of the opening of 10 single peptide bonds in native mutants (Delta G(op,N)) were estimated from the thermodynamic cycle that links denaturation and cleavage free energies. To calculate those values, we assumed that the free energy of opening of a single peptide bond in the denatured state (Delta G(op,D)) was equal to -2.7 kcal/mole, as reported previously. Calculated Delta G(op,N) values in BPTI were in the range from 0.2 to 10 kcal/mole, which was equivalent to a >1 million-fold difference in equilibrium constants. The values of Delta G(op,N) were the largest for peptide bonds located in the C-terminal helix and significantly lower for peptide bonds in the beta-structure or loop regions. It appears that opening constants for single peptide bonds in various proteins span across 33 orders of magnitude. Typical equilibrium values for a single peptide bond opening in a protein containing secondary structure elements fall into negligibly low values, from 10(-3) to 10(-8), and are efficient to ensure stability against proteolysis.     

Efficient and rapid purification of recombinant human alpha-galactosidase A by affinity column chromatography

The lysosomal enzyme alpha-galactosidase A (alpha-Gal A) metabolizes neutral glycosphingolipids that possess alpha-galactoside residues at the non-reducing terminus, and inherited defects in the activity of alpha-Gal A lead to Fabry disease. We describe here an efficient and rapid purification procedure for recombinant alpha-Gal A by sequential Concanavalin A (Con A)-Sepharose and immobilized thio-alpha-galactoside (thio-Gal) agarose column chromatography. Optimal elution conditions for both columns were obtained using overexpressed human alpha-Gal A. We recommend the use of a mixture of 0.9 M methyl alpha-mannoside and 0.9 M methyl alpha-glucoside in 0.1 M acetate buffer (pH 6.0) with 0.1 M NaCl for the maximum recovery of glycoproteins with multiple high-mannose type sugar chains from Con A column chromatography, and that the Con A column should not be reused for the purification of glycoproteins that are used for structural studies. Binding of the enzyme to the thio-Gal column requires acidic condition at pH 4.8. A galactose-containing buffer (25 mM citrate-phosphate buffer, pH 5.5, with 0.1 M galactose, and 0.1 M NaCl) was used to elute alpha-Gal A. This procedure is especially useful for the purification of mutant forms of alpha-Gal A, which are not stable under conventional purification techniques. A protocol that purifies an intracellular mutant alpha-Gal A (M279I) expressed in COS-7 cells within 6h at 62% overall yield is presented.