Recovery of active N-acetyl-D-glucosamine 2-epimerase from inclusion bodies by solubilization with non-denaturing buffers

Overexpression of recombinant N-acetyl-d-glucosamine 2-epimerase, one of the key enzymes for the synthesis of N-acetylneuraminic acid, in E. coli led to the formation of protein inclusion bodies. In this study we report the recovery of active epimerase from inclusion bodies by direct solubilization with Tris buffer. At pH 7.0, 25% of the inclusion bodies were solubilized with Tris buffer. The specific activity of the solubilized proteins, 2.08 ± 0.02 U/mg, was similar to that of the native protein, 2.13 ± 0.01 U/mg. The result of circular dichroism spectroscopy analysis indicated that the structure of the solubilized epimerase obtained with pH 7.0 Tris buffer was similar to that of the native epimerase purified from the clarified cell lysate. As expected, the extent of deviation in CD spectra increased with buffer pH. The total enzyme activity recovered by solubilization from inclusion bodies, 170.41 ± 10.06 U/l, was more than 2.5 times higher than that from the clarified cell lysate, 67.32 ± 5.53 U/l. The results reported in this study confirm the hypothesis that the aggregation of proteins into inclusion bodies is reversible and suggest that direct solubilization with non-denaturing buffers is a promising approach for the recovery of active proteins from inclusion bodies, especially for aggregation-prone multisubunit proteins.     

Three-step purification of lipopolysaccharide-free, polyhistidine-tagged recombinant antigens of Mycobacterium tuberculosis

Previous work has shown that the study of host immune responses against Mycobacterium tuberculosis, the causative agent of tuberculosis, requires the availability of multiple mycobacterial antigens. Since purification of protein from M. tuberculosis cells is extremely cumbersome, we developed a protocol for purifying milligram amounts of ten recombinant antigens of M. tuberculosis from E. coli cells. Purified proteins were immunologically active and free of contaminants that confound interpretation of cell-based immunological assays. The method utilizes a three-step purification protocol consisting of immobilized metal-chelate affinity chromatography, size exclusion chromatography and anion-exchange chromatography. The first two chromatographic steps yielded recombinant protein free of protein contaminants, while the third step (anion-exchange chromatography) efficiently removed E. coli lipopolysaccharide, a potent polyclonal activator of lymphoid cells. The recombinant proteins were immunologically indistinguishable from their native (i.e., purified from M. tuberculosis) counterparts. Thus the method provides a way to utilize recombinant proteins for immunological analyses that require highly purified antigens.     

Improved method for expression and isolation of the Mycoplasma hominis arginine deiminase from the recombinant strain of Escherichia coli

Arginine deiminase is a promising anticancer drug active against melanoma, hepatocarcinoma and other tumors. Recombinant strains of Escherichia coli that express arginine deiminase from pathogenic bacteria Mycoplasma have been developed. However, production costs of heterologous arginine deiminase are high due to use of an expensive inducer and extraction buffer, as well as using diluted culture for enzyme induction. We report on a new advanced protocol for Mycoplasma hominis arginine deiminase expression, extraction and renaturation. The main improvements include manipulation with dense suspensions of E. coli, use of lactose instead of isopropyl β-d-1-thiogalactopyranoside as an inducer and a cheaper but not less efficient buffer for solubilization of arginine deiminase inclusion bodies. In addition, supplementation of the storage culture medium with glucose and substrate (arginine) significantly stabilized the recombinant arginine deiminase producer. Homogenous preparations of recombinant arginine deiminase were obtained using anion-exchange and hydrophobic chromatography. The purified enzyme retained a specific activity of 30–34 U/mg for 12 months when stored at 4 °C in 20 mM sodium phosphate buffer pH 7.2 containing 1 M NaCl.     

Affinity purification and characterization of recombinant human galectin-1

Galectin-1, a polypeptidic factor that can have major effects on cell growth and apoptosis, was overexpressed in E. coli. This protein was purified to homogeneity by affinity chromatography on lactose coupled to divinylsulfone-activated agarose. The recombinant galectin-1 (rGAL1) was compared with the homologous protein purified from human brain tissue using two-dimensional electrophoresis on immobilized pH gradient (IPG-DALT). rGAL1 had a major isoelectric point of 5.4 (major pI of tissular galectin-1, 5.1) and its subunit molecular mass was 14 500. Addition of rGAL1 to Jurkat T-lymphoblastoid cells induced cell death in a concentration-dependent manner.     

Negative chromatography on agarose-TREN as a technique for purification of protein spiked in soybean seeds extract

Alkyl amines and polyamines have been used as ligands for protein purification by mixed-mode chromatography. The adsorption of proteins onto these ligands seems to be governed by multiple effects such as electrostatic, hydrophobic, and affinity interactions. In this work we investigated the adsorption of proteins extracted from soybean onto the adsorbent agarose-Tris(2-aminoethyl)amine (TREN). The effects of flow rate, buffer system, and extract concentration on the capture of proteins extracted from soybean were evaluated. Experiments using Mes at pH 6.5 as adsorption buffer allowed the adsorption of almost the totality of native soybean protein with a dynamic adsorption capacity of 13.50 mg mL^?1 adsorbent. Experiments with human IgG (pI in the range of 5.8–9.0) and human serum albumin (HSA, pI of 4.9) spiked into these extracts lead to the conclusion that electrostatic forces play a major role in the interaction between protein and agarose-TREN. Based on this work, negative chromatography with agarose-TREN should be considered as a method for purification of basic recombinant protein produced in transgenic soybean seeds.     

Purification of recombinant α-amylase with immuno-affinity chromatography using monoclonal antibody

A monoclonal antibody against recombinant thermostable α-amylase produced by Escherichia coli was isolated from serum-free medium and immobilized on Sepharose 4B. The adsorption equilibrium between α-amylase and the immobilized immuno-adsorbent showed a Langmuir type isotherm. The breakthrough curve calculated numerically using the averaged volumetric coefficient coincided well with the experimental data. More than 90% of the activity of bound α-amylase could be recovered by eluting with glycine-HCl buffer (pH 2.5). The elution profile at pH 2.5 became sharper with increasing temperature. By using an immuno-affinity column, the recombinant α-amylase produced by E. coli could be purified homogeneously from crude extract enzyme solution with two-step elution.     

Recombinant antigen production for assays of intradermoreaction for diagnosis and surveillance of tuberculosis

The goal of the present work was to develop reagents with potential for tuberculosis diagnosis. Genetic sequences of Mycobacterium tuberculosis secretion antigens were amplified by PCR, cloned into the Gateway^® system, and expressed in Escherichia coli. The recombinant M. tuberculosis proteins were purified by metal affinity chromatography and preparative gel SDS-PAGE electrophoresis followed by electroelution and removal of endotoxins using Triton X-114. In total, seven recombinant proteins were obtained (ESAT-6, CFP10, TB10.3, TB10.4, MTSP11, MPT70, and MPT83). Delayed hypersensitivity reactions (DHR) was evaluated in Cavia porcellus and compared to the response using a standard purified protein derivative (PPD). All seven recombinant proteins produced a positive induration reaction in an intradermal test in guinea pigs previously sensitized with M. tuberculosis. When applied together, at a concentration of each recombinant protein 0.04 mg/mL, the intradermoreaction in C. porcellus was significantly higher than that obtained by standard PPD (p-value = 0.00386).     

High-level production and purification of biologically active proteins from bacterial and mammalian cells using the tandem pGFLEX expression system

Because of the complexities involved in the regulation of gene expression in Escherichia coli and mammalian cells, it is considered general practice to use different vectors for heterologous expression of recombinant proteins in these host systems. However, we have developed and report a shuttle vector system, pGFLEX, that provides high-level expression of recombinant glutathione S-transferase (GST) fusion proteins in E. coli and mammalian cells. pGFLEX contains the cytomegaloma virus (CMV) immediate-early promoter in tandem with the E. coli lacZpo system. The sequences involved in gene expression have been appropriately modified to enable high-level production of fusion proteins in either cell type. The pGFLEX expression system allows production of target proteins fused to either the N or C terminus of the GST π protein and provides rapid purification of target proteins as either GST fusions or native proteins after cleavage with thrombin. The utility of this vector in identifying and purifying a component of a multi-protein complex is demonstrated with cyclin A. The pGFLEX expression system provides a singular and widely applicable tool for laboratory or industrial production of biologically active recombinant proteins in E. coli and mammalian cells.     

Cloning,expression and characterization of an organic solvent tolerant lipase from Pseudomonas fluorescens JCM5963

A novel lipase gene from an organic solvent degradable strain Pseudomonas fluorescens JCM5963 was cloned, sequenced, and overexpressed as an N-terminus His-tag fusion protein in E. coli. The alignment of amino acid sequences revealed that the protein contained a lipase motif and shared a medium or high similarity with lipases from other Pseudomonas strains. It could be defined as a member of subfamily I.1 lipase. Most of the recombinant proteins expressed as enzymatically active aggregates soluble in 20 mM Tris–HCl buffer (pH 8.0) containing sodium deoxycholate are remarkably different from most subfamily I.1 and I.2 members of Pseudomonas lipases expressed as inactive inclusion body formerly described in E. coli. The recombinant lipase (rPFL) was purified to homogeneity by Ni-NTA affinity chromatography and Sephacryl S-200 gel filtration chromatography. The purified lipase was stable in broad ranges of temperatures and pH values, with the optimal temperature and pH value being 55 °C and 9.0, respectively. Its activity was found to increase in the presence of metal ions such as Ca²⁺, Sn²⁺ and some non-ionic surfactants. In addition, rPFL was activated by and remained stable in a series of water-miscible organic solvents solutions and highly tolerant to some water-immiscible organic solvents. These features render this novel lipase attraction for biotechnological applications in the field of organic synthesis and detergent additives.     

Refolding process of cysteine-rich proteins:Chitinase as a model

Background:

Recombinant proteins overexpressed in E. coli are usually deposited in inclusion bodies. Cysteines in the protein contribute to this process. Inter- and intra- molecular disulfide bonds in chitinase, a cysteine-rich protein, cause aggregation when the recombinant protein is overexpressed in E. coli. Hence, aggregated proteins should be solubilized and allowed to refold to obtain native- or correctly- folded recombinant proteins.

Methods:

Dilution method that allows refolding of recombinant proteins, especially at high protein concentrations, is to slowly add the soluble protein to refolding buffer. For this purpose: first, the inclusion bodies containing insoluble proteins were purified; second, the aggregated proteins were solubilized; finally, the soluble proteins were refolded using glutathione redox system, guanidinium chloride, dithiothreitol, sucrose, and glycerol, simultaneously.

Results:

After protein solubilization and refolding, SDS-PAGE showed a 32 kDa band that was recognized by an anti-chitin antibody on western blots.

Conclusions:

By this method, cysteine-rich proteins from E. coli inclusion bodies can be solubilized and correctly folded into active proteins.Key Words: Chitinase, Cysteine-rich proteins, Protein refolding, Protein solubilization     

Production of prone-to-aggregate proteins

Expression of recombinant proteins in Escherichia coli (E. coli) remains the most popular and cost-effective method for producing proteins in basic research and for pharmaceutical applications. Despite accumulating experience and methodologies developed over the years, production of recombinant proteins prone to aggregate in E. coli-based systems poses a major challenge in most research applications. The challenge of manufacturing these proteins for pharmaceutical applications is even greater. This review will discuss effective methods to reduce and even prevent the formation of aggregates in the course of recombinant protein production. We will focus on important steps along the production path, which include cloning, expression, purification, concentration, and storage.     

Purification and properties of the antizymes of Escherichia coli to ornithine decarboxylase

The purification of the antizymes to ornithine decarboxylase of Escherichia coli to homogeneity is detailed. An acidic component, pI 3.8, and two basic histone-like proteins, pI above 9.5, are described. The two latter proteins constitute approximately 90% of the total antizyme activity.     

Assay and purification of a solubilized membrane receptor that binds the lysosomal enzyme α-l-iduronidase

A receptor that binds the lysosomal enzyme α-l-iduronidase via phosphorylated mannose residues on the enzyme has been solubilized from Swarm rat chondrosarcoma membranes using a pH 9.5 buffer containing 0.1% Triton X-100. Detergent-solubilized receptor in crude and purified preparations was measured by assay of bound α-l-iduronidase after adsorbing the receptor-enzyme complex onto insoluble phospholipid vesicles (liposomes). Binding of α-l-iduronidase to the liposomes required receptor and was completely inhibited by mannose 6-phosphate but not glucose 6-phosphate, indicating that the receptor maintained specificity following solubilization. Receptors from rat chondrosarcoma and human diploid fibroblasts were purified to apparent homogeneity using a phosphomannan-Sepharose affinity column. Both had identical molecular weights in polyacrylamide gels containing sodium dodecyl sulfate (M_r = 215,000). Amino acid analysis and two-dimensional gel electrophoresis was carried out on the purified rat chondrosarcoma receptor. Two forms of the receptor with different pI's were observed (pI 5.5 and 6.2). One form (pI 5.5) was made more basic (pI 5.8) by treatment with neuraminidase.     

Simple purification ofEscherichia coli-derived recombinant human interleukin-2 expressed with N-terminus fusion of glucagon

Simple procedures have been devised for purifying recombinant human interleukin-2 (hIL-2), which was expressed inEscherichia coli using sequences of glucagon molecules and enterokinase cleavage site as an N-terminus fusion partner. The insoluble aggregates of recombinant fusion protein produced inE. coli cytoplasm were easily dissolved by simple alkaline pH shift (8→12→8). Following enterokinase cleavage, the recombinant hIL-2 was finally purified by one-step reversed-phase HPLC with high purity. The ease and high efficiency of this simple purification process seem to mainly result from the role of used glucagon fusion partner, which could be applied to the production of other therapeutically important proteins.     

High level expression and purification of recombinant flounder growth hormone in E. coli

Recombinant flounder growth hormone was overproduced in E. coli by using codon optimized synthetic gene and optimized expression conditions for high level production. The gene was cloned into PET-28a expression vector and transformed into E. coli BL21 (DE3). Induction at lower temperature, lower IPTG concentrations and richer growth media during expression resulted in increased expression level. The protein expression profile was analyzed by SDS-PAGE, the authenticity was confirmed by western blotting and the concentration was determined by Bradford assay. In addition, several attempts were made to produce soluble product and all resulted in insoluble product. The overexpressed protein was efficiently purified from inclusion bodies by moderate speed centrifugation after cell lysis. Among the solubilization buffers examined, buffer with 1% N-lauroylsarcosine in the presence of reducing agent DTT at alkaline pH resulted in efficient solubilization and recovery. The denaturant was removed by filtration and dialysis. The amount of the growth hormone recovered was significantly higher than previous reports that expressed native growth hormone genes in E. coli. The methodology adapted in this study, can be used to produce flounder growth hormone at large scale level so that it can be used in aquaculture. This approach may also apply to other proteins if high level expression and efficient purification is sought in E. coli.     

A simple method for the purification of over-expressed extracellular sucrase of Zymomonas mobilis from a recombinant Escherichia coli

The over-expressed extracellular sucrase (SacC) of Zymomonas mobilisfrom a recombinant Escherichia coli (pZSP62) carrying the sacC gene was purified partially by repeated cycles of freezing and thawing. This method separated the highly expressed recombinant protein from the bulk of endogenous E. coli proteins. The enzyme was further purified 14 fold with a 55% yield from the cellular extract of E. coli by hydroxyapatite chromatography. The purified enzyme had a Mr of 46 kDa by SDS-PAGE. Its km value for sucrose was 86 mM and was optimal at pH 5.0 and at 36°C.     

Production of recombinant Chikungunya virus envelope 2 protein in Escherichia coli

Chikungunya, a mosquito-borne viral disease caused by Chikungunya virus (CHIKV), has drawn substantial attention after its reemergence causing massive outbreaks in tropical regions of Asia and Africa. The recombinant envelope 2 (rE2) protein of CHIKV is a potential diagnostic as well as vaccine candidate. Development of cost-effective cultivation media and appropriate culture conditions are generally favorable for large-scale production of recombinant proteins in Escherichia coli. The effects of medium composition and cultivation conditions on the production of recombinant Chikungunya virus E2 (rCHIKV E2) protein were investigated in shake flask culture as well as batch cultivation of Escherichia coli. Further, the fed-batch process was also carried out for high cell density cultivation of E. coli expressing rE2 protein. Expression of rCHIKV E2 protein in E. coli was induced with 1 mM isopropyl-beta-thiogalactoside (IPTG) at ~23 g dry cell weight (DCW) per liter of culture and yielded an insoluble protein aggregating to form inclusion bodies. The final DCW after fed-batch cultivation was ~35 g/l. The inclusion bodies were isolated, solubilized in 8 M urea and purified through affinity chromatography to give a final product yield of ~190 mg/l. The reactivity of purified E2 protein was confirmed by Western blotting and enzyme-linked immunosorbent assay. These results show that rE2 protein of CHIKV may be used as a diagnostic reagent or for further prophylactic studies. This approach of producing rE2 protein in E. coli with high yield may also offer a promising method for production of other viral recombinant proteins.     

Direct and simple detection of recombinant proteins from cell lysates using differential scanning fluorimetry

A simple, inexpensive, and universal method to quantify the recombinant proteins in Escherichia coli cell lysate using differential scanning fluorimetry (DSF) is reported. This method is based on the precise correlation between Δ(fluorescence intensity) determined by DSF and the amount of protein in solution. We first demonstrated the effectiveness of the DSF method using two commercially available enzymes, α-amylase and cellobiase, and then confirmed its utility with two recombinant proteins, amylosucrase and maltogenic amylase, expressed in E. coli. The Δ(fluorescence intensity) in DSF analysis accurately correlated with the concentration of the purified enzymes as well as the recombinant proteins in E. coli cell lysates. The main advantage of this method over other techniques such as Western blotting, enzyme-linked immunosorbent assay (ELISA), and green fluorescence protein (GFP) fusion proteins is that intact recombinant protein can be quantified without the requirement of additional chemicals or modifications of the recombinant protein. This DSF assay can be performed using widely available equipment such as a real-time polymerase chain reaction (RT–PCR) instrument, microplates or microtubes, and fluorescent dye. This simple but powerful method can be easily applied in a wide range of research areas that require quantification of expressed recombinant proteins.     

Engineered Escherichia coli capable of co-utilization of cellobiose and xylose

Natural ability to ferment the major sugars (glucose and xylose) of plant biomass is an advantageous feature of Escherichia coli in biofuel production. However, excess glucose completely inhibits xylose utilization in E. coli and decreases yield and productivity of fermentation due to sequential utilization of xylose after glucose. As an approach to overcome this drawback, E. coli MG1655 was engineered for simultaneous glucose (in the form of cellobiose) and xylose utilization by a combination of genetic and evolutionary engineering strategies. The recombinant E. coli was capable of utilizing approximately 6 g/L of cellobiose and 2 g/L of xylose in approximately 36 h, whereas wild-type E. coli was unable to utilize xylose completely in the presence of 6 g/L of glucose even after 75 hours. The engineered strain also co-utilized cellobiose with mannose or galactose; however, it was unable to metabolize cellobiose in the presence of arabinose and glucose. Successful cellobiose and xylose co-fermentation is a vital step for simultaneous saccharification and co-fermentation process and a promising step towards consolidated bioprocessing.     

Proteomic analysis of contaminants in recombinant membrane hemeproteins expressed in <Emphasis Type="Italic">E. coli</Emphasis> and isolated by metal affinity chromatography

Contaminating proteins have been identified by “shotgun” proteomic analysis in 14 recombinant preparations of human membrane heme- and flavoproteins expressed in Escherichia coli and purified by immobilized metal ion affinity chromatography. Immobilized metal ion affinity chromatography of ten proteins was performed on Ni²⁺-NTA-sepharose 6B, and the remaining four proteins were purified by ligand affinity chromatography on 2',5'-ADP-sepharose 4B. Proteomic analysis allowed to detect 50 protein impurities from E. coli. The most common contaminant was Elongation factor Tu2. It is characterized by a large dipole moment and a cluster arrangement of acidic amino acid residues that mediate the specific interaction with the sorbent. Peptidyl prolyl-cis-trans isomerase SlyD, glutamine-fructose-6-phosphate aminotransferase, and catalase HPII that contained repeating HxH, QxQ, and RxR fragments capable of specific interaction with the sorbent were identified among the protein contaminants as well. GroL/GroS chaperonins were probably copurified due to the formation of complexes with the target proteins. The Ni²⁺ cations leakage from the sorbent during lead to formation of free carboxyl groups that is the reason of cation exchanger properties of the sorbent. This was the putative reason for the copurification of basic proteins, such as the ribosomal proteins of E. coli and the widely occurring uncharacterized protein YqjD. The results of the analysis revealed variation in the contaminant composition related to the type of protein expressed. This is probably related to the reaction of E. coli cell proteome to the expression of a foreign protein. We concluded that the nature of the protein contaminants in a preparation of a recombinant protein purified by immobilized metal ion affinity chromatography on a certain sorbent could be predicted if information on the host cell proteome were available.