Protein body-inducing fusions for high-level production and purification of recombinant proteins in plants

For the past two decades, therapeutic and industrially important proteins have been expressed in plants with varying levels of success. The two major challenges hindering the economical production of plant-made recombinant proteins include inadequate accumulation levels and the lack of efficient purification methods. To address these limitations, several fusion protein strategies have been recently developed to significantly enhance the production yield of plant-made recombinant proteins, while simultaneously assisting in their subsequent purification. Elastin-like polypeptides are thermally responsive biopolymers composed of a repeating pentapeptide 'VPGXG' sequence that are valuable for the purification of recombinant proteins. Hydrophobins are small fungal proteins capable of altering the hydrophobicity of their respective fusion partner, thus enabling efficient purification by surfactant-based aqueous two-phase systems. Zera, a domain of the maize seed storage protein γ-zein, can induce the formation of protein storage bodies, thus facilitating the recovery of fused proteins using density-based separation methods. These three novel protein fusion systems have also been shown to enhance the accumulation of a range of different recombinant proteins, while concurrently inducing the formation of protein bodies. The packing of these fusion proteins into protein bodies may exclude the recombinant protein from normal physiological turnover. Furthermore, these systems allow for quick, simple and inexpensive nonchromatographic purification of the recombinant protein, which can be scaled up to industrial levels of protein production. This review will focus on the similarities and differences of these artificial storage organelles, their biogenesis and their implication for the production of recombinant proteins in plants and their subsequent purification.     

Gene synthesis, expression in Escherichia coli and purification of immunoreactive human insulin-like growth factors I and II. Application of a modified HPLC separation technique for hydrophobic proteins

We have expressed synthetic genes encoding human insulin-like growth factors I and II in large quantities in Escherichia coli as fusion proteins with the 300 N-terminal amino acids of the E. coli trpE gene product. The resulting hybrid proteins were purified from the insoluble fraction of crude bacterial lysates using a rapid HPLC separation procedure employing a C8 reversed-phase column and a gradient of 2-propanol in formic acid. With the procedure we obtained in volatile solvents highly purified fusion proteins that were used for further biochemical and immunological procedures. Here we describe biochemical characteristics of the bacterially expressed fusion proteins and demonstrate that these proteins share substantial antigenic properties with the native polypeptides allowing the establishment of highly specific monoclonal antibodies.     

Screening methods to determine biophysical properties of proteins in structural genomics

We have developed and tested a simple and efficient protein purification method for biophysical screening of proteins and protein fragments by nuclear magnetic resonance (NMR) and optical methods, such as circular dichroism spectroscopy. The method constitutes an extension of previously described protocols for gene expression and protein solubility screening [M. Hammarstr?m et al., (2002), Protein Science 11, 313]. Using the present purification scheme it is possible to take several target proteins, produced as fusion proteins, from cell pellet to NMR spectrum and obtain a judgment on the suitability for further structural or biophysical studies in less than 1 day. The method is independent of individual protein properties as long as the target protein can be produced in soluble form with a fusion partner. Identical procedures for cell culturing, lysis, affinity chromatography, protease cleavage, and NMR sample preparation then initially require only optimization for different fusion partner and protease combinations. The purification method can be automated, scaled up or down, and extended to a traditional purification scheme. We have tested the method on several small human proteins produced in Escherichia coli and find that the method allows for detection of structured proteins and unfolded or molten globule-like proteins.     

Linkers for improved cleavage of fusion proteins with an engineered alpha-lytic protease.

Addition of an N-terminal fusion partner can greatly aid the expression and purification of a recombinant protein in Escherichia coli. We investigated two genetically engineered proteases designed to remove the fusion partner after the protein of interest has been expressed. Recombinant human insulin-like growth factor-II (hIGF-II) has been produced from E. coli-derived fusion proteins using a novel enzymatic cleavage system that uses a mutant of alpha-lytic protease. Initially, two potential fusion protein linkers were designed, Pro-Ala-Pro-His (PAPH) and Pro-Ala-Pro-Met (PAPM), and were tested as substrates in the form of synthetic dodecapeptides. Using mass spectrometry and reverse-phase HPLC, the position of cleavage was confirmed and the kinetics of synthetic peptide cleavage were examined. Use of the linkers in hIGF-II fusion proteins produced in E. coli was then evaluated. The fusion proteins constructed consist of the first 11 amino acids of porcine growth hormone linked N-terminally to hIGF-II by six amino acids that include the dipeptide Val-Asn followed by a variable tetrapeptide protease cleavage motif. Mass spectrometry and N-terminal sequencing confirmed that proteolytic cleavage of the fusion proteins had occurred at the predicted sites. Using the fusion proteins as substrates, the cleavage of the rationally designed motifs by the alpha-lytic protease mutant was compared. The fusion protein containing the motif PAPM had a k(cat)/K(M) ratio indicating a 1.6-fold preference over the PAPH fusion protein for cleavage by this enzyme. Furthermore, when hIGF-II fusion proteins containing the designed cleavable linkers were processed with the engineered alpha-lytic protease, they gave greatly improved yields of native hIGF-II compared to an analogous fusion protein cleaved by H64A subtilisin. Comparison of the peptide and protein cleavage studies shows that the efficient proteolysis of the cleavage motifs is an inherent property of the designed sequences and is not determined by secondary or tertiary structure in the fusion proteins.     

Large-scale preparation and biological activity of recombinant human parathyroid hormone

Human parathyroid hormone (hPTH) has been bacterially expressed in bioreactors as cro-β-galactosidase-hPTH fusion protein. We have developed a large-scale purification scheme that exploits the pH-dependent differential solubility of hPTH and a two-step Chromatographie procedure. We demonstrate that in a number of assay systems, the recombinant material obtained by this procedure is biologically active.     

Comparative evaluation of two purification methods of anti-CD19-c-myc-His6-Cys scFv

Different chromatographic methods have been used to purify bacterially expressed single chain antibodies in soluble or insoluble form. Here, we compared two methods for purification of anti-CD19-c-myc-His6-Cys scFv expressed in Escherichia coli as soluble protein. The protein-L-agarose purification method is a one step purification method that yielded significant amounts of pure protein compared to the two-step Ni-NTA-agarose plus Resource 15S purification method. However, the protein-L purification method exhibited an additional lower molecular weight protein contaminant. Based on results from in vitro gel digestion, mass spectrometry and database search results, we confirmed that the lower molecular weight protein contaminant, which could not be purified by Ni-NTA-agarose and 15S column method, is a degraded product of the full length scFv construct.     

Expression and secretion of glycosylated heparin biosynthetic enzymes using Komagataella pastoris

Heparin, an anticoagulant drug, is biosynthesized in selected animal cells. The heparin biosynthetic enzymes mainly consist of sulfotransferases and all are integral transmembrane glycoproteins. These enzymes are generally produced in engineered Escherichia coli as without their transmembrane domains as non-glycosylated fusion proteins. In this study, we used the yeast, Komagataella pastoris, to prepare four sulfotransferases involved in heparin biosynthesis as glycoproteins. While the yields of these yeast-expressed enzymes were considerably lower than E. coli-expressed enzymes, these enzymes were secreted into the fermentation media simplifying their purification and were endotoxin free. The activities of these sulfotransferases, expressed as glycoproteins in yeast, were compared to the bacterially expressed proteins. The yeast-expressed sulfotransferase glycoproteins showed improved kinetic properties than the bacterially expressed proteins.

     

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.     

Intein-mediated protein ligation: harnessing nature's escape artists

Inteins are naturally occurring proteins that are involved in the precise cleavage and formation of peptide bonds in a process known as protein splicing. Genetic engineering has allowed the controllable cleavage of peptide bonds at either the N- or C-terminus of the intein. Inteins displaying controllable cleavage have been used in the isolation of bacterially expressed proteins possessing either a C-terminal thioester or an N-terminal cysteine. The specific placement of these reactive groups has allowed either protein-protein or protein-peptide condensation through a native peptide bond. This review describes the methods used to specifically generate these reactive groups on bacterially expressed proteins and some applications of this technique, known as intein-mediated protein ligation. Furthermore, a versatile two intein (TWIN) system will be described which enables the circularization and polymerization of bacterially expressed proteins or peptides.     

Expression and purification of histidine-tagged proteins from the gram-positive Streptococcus gordonii SPEX system

Streptococcus gordonii (S. gordonii) has been used as a gram-positive bacterial expression vector for secreted or surface-anchored recombinant proteins. Fusion of the gram-positive bacterial N-terminal signal sequence to the target protein is all that is required for efficient export. This system is termed SPEX for Surface Protein EXpression and has been used to express proteins for a variety of uses. In this study, the SPEX system has been further developed by the construction of vectors that express polyhistidine-tagged fusion proteins. SPEX vectors were constructed with an N-terminal or C-terminal histidine tag. The C-repeat region (CRR) from Streptococcus pyogenes M6 protein and the Staphylococcus aureus nuclease A (NucA) enzyme were tested for expression. The fusion proteins were purified using metal affinity chromatography (MAC). Results show that the fusion proteins were expressed and secreted from S. gordonii with the His tag at either the N- or C-terminal position and could be purified using MAC. The M6 fusions retained immunoreactivity after expression and purification as determined by immunoblots and ELISA analyses. In addition, NucA fusions retained functional activity after MAC purification. The M6-His and NucA-His fusions were purified approximately 15- and 10-fold respectively with approximately 30% recovery of protein using MAC. This study shows that the polyhistidine tag in either the N- or C-terminal position is a viable way to purify secreted heterologous proteins from the supernatant of recombinant S. gordonii cultures. This study further illustrates the value of the SPEX system for secreted expression and purification of proteins.     

Recombinant human insulin. VIII. Isolation of fusion protein--S-sulfonate, biotechnological precursor of human insulin, from the biomass of transformed Escherichia coli cells

Various methods have been investigated for the isolation and purification of fusion proteins of precursors of human insulin in the form of S-sulfonates, from the biomass of transformed Escherichia coli cells. Fusion proteins were prepared with different sizes and structures of the leader peptide and the poly-His position (inserted for purification by metal chelate affinity chromatography). The fusion proteins contained an IgG-binding B domain of protein A from Staphylococcus aureus at the N-terminus and an Arg residue between the leader peptide of the molecule and the proinsulin sequence, for trypsin cleavage of the leader peptide. Six residues of Cys in proinsulin allow the chemical modification of the protein as a (Cys-S-SO(-)(3))(6) derivative (S-sulfonate), which increases its polyelectrolytic properties and improves the efficiency of its isolation. Various methods of oxidative sulfitolysis were compared with catalysis by sodium tetrathionate or cystine and Cu2+ or Ni2+ ions. An optimum scheme for the isolation and purification of S-sulfonated fusion proteins was developed by the combination of metal-chelating affinity and ion-exchange chromatography. Highly purified (95%) S-sulfonated fusion protein was recovered which was 85% of the fusion protein contained in the biomass of E. coli cells. Folding of fusion protein S-sulfonate occurred with high yield (up to 90-95%). We found that the fusion protein-S-sulfonate has proinsulin-like secondary structure.This structure causes highly efficient fusion protein folding.     

C-terminal and n-terminal fusions of aequorin with small peptides in immunoassay development

Aequorin fusion proteins have been used extensively in intracellular Ca2+ measurements and in the development of binding assays. Gene fusions to aequorin for production of fusion proteins have been so far limited to its N-terminus, as previous studies have indicated that aequorin loses its activity upon modification of its C-terminus. To further investigate this, two model peptides, an octapeptide (DTLDDDDL), and leu-enkephalin (TGGFL), an opioid peptide, were fused to the C-terminus of a cysteine-free mutant of aequorin through genetic engineering. The octapeptide was also fused to the N-terminus of the aequorin-leu-enkephalin fusion protein, which enables its affinity purification. Contrary to reports of earlier studies, we found that aequorin retains its bioluminescence activity after modification of the C-terminus. The half-life of light emission and the calibration curves obtained with the fusion proteins were comparable to those of the cysteine-free mutant of aequorin. Dose-response curves for the octapeptide were generated using two aequorin-octapeptide fusion proteins with the octapeptide fused to the N-terminus in one case, and to the C-terminus in the other. Similar detection limits for the octapeptide were obtained using both fusion proteins. The C-terminal fusion system has advantages in cases where antibodies recognize only the C-terminus of the peptide, as well as in cases where the functionality of the peptide lies in its C-terminus. The purification is also simplified as the affinity tag can be engineered at one terminus and the peptide of interest at the other.     

Fusion tails for the recovery and purification of recombinant proteins.

Several fusion tail systems have been developed to promote efficient recovery and purification of recombinant proteins from crude cell extracts or culture media. In these systems, a target protein is genetically engineered to contain a C- or N-terminal polypeptide tail, which provides the biochemical basis for specificity in recovery and purification. Tails with a variety of characteristics have been used: (1) entire enzymes with affinity for immobilized substrates or inhibitors; (2) peptide-binding proteins with affinity to immunoglobulin G or albumin; (3) carbohydrate-binding proteins or domains; (4) a biotin-binding domain for in vivo biotination promoting affinity of the fusion protein to avidin or streptavidin; (5) antigenic epitopes with affinity to immobilized monoclonal antibodies; (6) charged amino acids for use in charge-based recovery methods; (7) poly(His) residues for recovery by immobilized metal affinity chromatography; and (8) other poly(amino acid)s, with binding specificities based on properties of the amino acid side chain. Fusion tails are useful at the lab scale and have potential for enhancing recovery using economical recovery methods that are easily scaled up for industrial downstream processing. Fusion tails can be used to promote secretion of target proteins and can also provide useful assay tags based on enzymatic activity or antibody binding. Many fusion tails do not interfere with the biological activity of the target protein and in some cases have been shown to stabilize it. Nevertheless, for the purification of authentic proteins a site for specific cleavage is often included, allowing removal of the tail after recovery.     

Study of protein splicing and intein-mediated peptide bond cleavage under high-cell-density conditions

Protein splicing elements (inteins), capable of catalyzing controllable peptide bond cleavage reactions, have been used to separate recombinant proteins from affinity tags during affinity purification. Since the inteins eliminate the use of a protease in the recovery process, the intein-mediated purification system has the potential to significantly reduce recovery costs for the industrial production of recombinant proteins. Thus far, the intein system has only been examined and utilized for expression and purification of recombinant proteins at the laboratory scale for cells cultivated at low cell densities. In this study, protein splicing and in vitro cleavage of intein fusion proteins expressed in high-cell-density fed-batch fermentations of recombinant Escherichia coli were examined. Three model intein fusion constructs were used to examine the stability and splicing/cleavage activities of the fusion proteins produced under high-cell-density conditions. The data indicated that the intein fusion protein containing the wild-type intein catalyzed efficient in vivo protein splicing during high-cell-density cultivation. Also, the intein fusion proteins containing modified inteins catalyzed efficient thiol-induced in vitro cleavage reactions. The results of this study demonstrated the potential feasibility of using the intein-mediated protein purification system for industrial-scale production of recombinant proteins.     

Construction of a modified vector for efficient purification of recombinant Mycobacterium tuberculosis proteins expressed in Escherichia coli

A major problem in assessing the vaccine and diagnostic potential of various proteins encoded by Mycobacterium tuberculosis genome is the inability to produce large quantities of these proteins, even when Escherichia coli or other heterologous systems are employed for recombinant protein production. To overcome these barriers, we have constructed a modified expression vector, using pGEX-4T-1 vector as the backbone. In addition to the features offered by the pGEX-4T vectors, the new vector allowed easy purification of recombinant proteins on the highly versatile Ni-NTA-agarose affinity matrix. The utility of the new vector was demonstrated by expressing and purifying, to near homogeneity, two M. tuberculosis proteins, i.e., Rv3872 (a member of the multi-gene PE subfamily) and Rv3873 (a member of the multi-gene PPE subfamily), which are encoded by the RD1 region of M. tuberculosis. The proteins encoded by rv3872 and rv3873 were expressed at high levels as fusion proteins with glutathione-S-transferase in E. coli. The recombinant Rv3872 and Rv3873 proteins were purified and isolated free of the fusion partner (GST) by affinity purification on glutathione-Sepharose and/or Ni-NTA-agarose affinity matrix and cleavage of the purified fusion proteins by thrombin protease. The recombinant Rv3872 protein was nearly homogeneous (more than 95% pure) while Rv3873 preparation was more than 90% pure. The recombinant Rv3872 and Rv3873 proteins were immunologically active and reacted with antibodies in sera from TB patients. Our results demonstrate the utility of the newly constructed expression vector with two affinity tags for efficient expression and purification of recombinant M. tuberculosis proteins expressed in E. coli, which could be used for further diagnostic and immunological studies.     

Partial purification of human parathyroid hormone 1-84 as a thioredoxin fusion form in recombinant Escherichia coli by thermoosmotic shock

A modified purification method, thermoosmotic shock (osmotic shock coupled with heat-treatment) for heat-stable proteins, was devised in the purification of Trx-hPTH (1-84) (human parathyroid hormone coupled with thioredoxin as a fusion partner) from E. coli. Thermoosmotic shock can integrate the functions of extraction and crude separation of fusion protein Trx-hPTH (1-84). To improve the purification efficiency, thermoosmotic shock conditions were optimized and achieved as follows: the optimized high osmotic solution containing 20mM Tris-HCl buffer (pH 8.0), 1mM EDTA, and 25% sucrose; the low osmotic solution containing 20mM Tris-HCl buffer (pH 8.0), 1mM EDTA, and the heat-treatment temperature of 100 degrees C for 10 min. Using this method, the purity of Trx-hPTH (1-84) was up to 73% and the yield was up to 72%, respectively. In addition, the two separation methods of both thermoosmotic shock and affinity chromatography have been compared, indicating that thermoosmotic shock is an economical and feasible way for the fusion protein separation. Besides, the thermoosmotic shock method may be used for the purification of some proteins of thermal stability without N-terminal His-tag.     

Dihydrofolate reductase as a new "affinity handle".

Dihydrofolate reductase (DHFR) has been demonstrated to be a versatile "affinity handle" for expression of recombinant proteins. The DHFR "handle" has advantages not only in terms of efficiency of expressing the fusion protein as a soluble form but also in stabilizing unstable polypeptides and facilitating purification of the expressed protein by means of methotrexate-bound affinity chromatography and by making use of the enzyme activity. Fifteen genes encoding different lengths of polypeptides of 5 to 44 amino acids were chemically synthesized and introduced into expression vectors, pTP70-1 or its derivatives. All the polypeptide genes were efficiently expressed in Escherichia coli cells as fusion proteins which show DHFR activity. The respective fusion proteins were highly purified from cell-free extracts by monitoring the DHFR activity at each purification step. The use of methotrexate-bound affinity chromatography was very effective. In order to cut out the polypeptides, the purified fusion proteins were treated with either BrCN or site-specific protease according to the spacer sequence. The objective polypeptide was purified by means of a reversed-phase high-pressure liquid chromatography (HPLC) system. Specific cleavage of the purified fusion protein actually yielded very few peptide fragments, so the assignment and isolation of the objective polypeptide were carried out without difficulty.     

Cleavage and purification of intein fusion proteins using the Streptococcus gordonii spex system

A gram-positive bacterial expression vector using Streptococcus gordonii has been developed for expression and secretion, or surface anchoring of heterologous proteins. This system, termed Surface Protein Expression system or SPEX, has been used to express a variety of surface anchored and secreted proteins. In this study, the Mycobacterium xenopi (Mxe) GyrA intein and chitin binding domain from Bacillus circulans chitinase Al were used in conjunction with SPEX to express a fusion protein to facilitate secretion, cleavage, and purification. Streptococcus gordonii was transformed to express a secreted fusion protein consisting of a target protein with a C-terminal intein and chitin-binding domain. Two target proteins, the C-repeat region of the Streptococcus pyogenes M6 protein (M6) and the nuclease A (NucA) enzyme of Staphylococcus aureus, were expressed and tested for intein cleavage. The secreted fusion proteins were purified from culture medium by binding to chitin beads and subjected to reaction conditions to induce intein self-cleavage to release the target protein. The M6 and NucA fusion proteins were shown to bind chitin beads and elute under cleavage reaction conditions. In addition, NucA demonstrated enzyme activity both before and after intein cleavage.     

Photoaffinity labeling and biochemical characterization of binding proteins for pheromones,juvenile hormones,and peptides

Radiolabeled photoaffinity analogs can be used to purify and characterize proteins involved in pheromone perception, juvenile hormone (JH) action, and neuropeptide reception. Several photoaffinity analogs and purification strategies are described for each of these physiological targets. First, a diazoacetate photoaffinity label is used to selectively modify the pheromone binding protein of the gypsy moth, Lymantria dispar. Reverse-phase HPLC is then employed to fractionate the male antennal proteins. Second, a tandem procedure involving preparative isoelectric focusing (IEF) and ion-exchange (IEX) HPLC is employed for the purification of the Manduca sexta hemolymph juvenile hormone binding protein (JHBP), which has now been cloned and sequenced. A separate application of this strategy for the purification of the 29 kDa JH I/methoprene receptor proteins from epidermal nuclei of M. sexta larvae is outlined. A new photolabel, farnesyl diazoketone, has been employed for the characterization of crustacean hemolymph methyl farnesoate binding proteins. Third, the development of neuropeptide photoaffinity labels is described for two systems: (1) the red pigment concentrating hormone (RPCH) of shrimp and (2) the allatostatins isolated from the brain of the cockroach Diploptera punctata.     

Eukaryotic proteins expressed in Escherichia coli: an improved thrombin cleavage and purification procedure of fusion proteins with glutathione S-transferase

Several systems have been developed to allow for rapid and efficient purification of recombinant proteins expressed in bacteria. The expression of polypeptides in frame with glutathione S-transferase (GST) allows for purification of the fusion proteins from crude bacterial extracts under nondenaturing conditions by affinity chromatography on glutathione agarose (D. B. Smith and K. S. Johnson, 1988, Gene 67, 31-40). This vector expression system has also incorporated specific protease cleavage sites to facilitate proteolysis of the bacterial fusion proteins. In our hands, the cleavage of these fusion proteins at a thrombin cleavage site proceeded slowly. To facilitate the cleavage of fusion proteins, we have introduced a glycine-rich linker (glycine kinker) containing the sequence P.G.I.S.G.G.G.G.G located immediately following the thrombin cleavage site. This glycine kinker greatly increases the thrombin cleavage efficiency of several fusion proteins. The introduction of the glycine kinker into fusion proteins allows for the cleavage of the fusion proteins while they are attached to the affinity resin resulting in a single step purification of the recombinant protein. More than 2 mg of the highly purified protein was obtained from the equivalent of 100 ml of bacterial culture within a few hours when a protein tyrosine phosphatase was employed as a test protein. The vector, pGEX-KG, has also been modified to facilitate cloning of a variety of cDNAs in all reading frames and has been successfully used to express several eukaryotic proteins.