Overproduction of Thermus sp. Strain T2 β-Galactosidase in Escherichia coli and Preparation by Using Tailor-Made Metal Chelate Supports

A novel thermostable chimeric β-galactosidase was constructed by fusing a poly-His tag to the N-terminal region of the β-galactosidase from Thermus sp. strain T2 to facilitate its overexpression in Escherichia coli and its purification by immobilized metal-ion affinity chromatography (IMAC). The poly-His tag fusion did not affect the activation, kinetic parameters, and stability of the β-galactosidase. Copper-iminodiacetic acid (Cu-IDA) supports enabled the most rapid adsorption of the His-tagged enzyme, favoring multisubunit interactions, but caused deleterious effects on the enzyme stability. To improve the enzyme purification a selective one-point adsorption was achieved by designing tailor-made low-activated Co-IDA or Ni-IDA supports. The new enzyme was not only useful for industrial purposes but also has become an excellent model to study the purification of large multimeric proteins via selective adsorption on tailor-made IMAC supports.     

Purification, immobilization and stabilization of a highly enantioselective alcohol dehydrogenase from Thermus thermophilus HB27 cloned in E. coli

This paper shows the purification and immobilization of a very interesting thermophilic alcohol dehydrogenase from Thermus thermophilus HB27 cloned in Escherichia coli. The purification was based on a first thermal treatment of the crude extract, that leaves the target enzyme in the supernatant, followed by the adsorption of most contaminant proteins in a IMAC column (the target protein did not adsorb on these columns due to the poorness of His residues). Final purification factor was around a 9-fold factor (no other protein bands were detected in SDS-PAGE gels) with an overall yield around 80%. Covalent immobilization of the enzyme on very different supports only permitted to improve the enzyme stability by a 5–10-fold factor, very similarly to the results obtained by the adsorption of the enzyme on polyethyleneimine coated supports. This enzyme adsorbed by ionic exchange maintained the activity unaltered during immobilization which was a very rapid process, and was more stable than the covalent preparations in the presence of organic solvents, and the enzyme was quite strongly adsorbed on the support. Therefore, it was proposed as a good option to prepare industrial biocatalysts of the enzyme. This preparation was utilized in the asymmetric reduction of acetophenone to produce (S)-(−)-1-phenylethanol, with an enantiomeric excess of more than 99%.     

Removal of poly-histidine fusion tags from recombinant proteins purified by expanded bed adsorption

Enzymatic methods have been used to cleave the C- or N-terminus polyhistidine tags from histidine tagged proteins following expanded bed purification using immobilized metal affinity chromatography (IMAC). This study assesses the use of Factor Xa and a genetically engineered exopeptidase dipeptidyl aminopeptidase-1 (DAPase-1) for the removal of C-terminus and N-terminus polyhistidine tags, respectively. Model proteins consisting of maltose binding protein (MBP) having a C- or N-terminal polyhistidine tag were used. Digestion of the hexahistidine tag of MBP-His(6) by Factor Xa and HT15-MBP by DAPase-1 was successful. The time taken to complete the conversion of MBP-His(6) to MBP was 16 h, as judged by SDS-PAGE and Western blots against anti-His antibody. When the detagged protein was purified using subtractive IMAC, the yield was moderate at 71% although the overall recovery was high at 95%. Likewise, a yield of 79% and a recovery of 97% was obtained when digestion was performed with using "on-column" tag digestion. On-column tag digestion involves cleavage of histidine tag from polyhistidine tagged proteins that are still bound to the IMAC column. Digestion of an N-terminal polyhistidine tag from HT15-MBP (1 mg/mL) by the DAPase-I system was superior to the results obtained with Factor Xa with a higher yield and recovery of 99% and 95%, respectively. The digestion by DAPase-I system was faster and was complete at 5 h as opposed to 16 h for Factor Xa. The detagged MBP proteins were isolated from the digestion mixtures using a simple subtractive IMAC column procedure with the detagged protein appearing in the flowthrough and washing fractions while residual dipeptides and DAPase-I (which was engineered to exhibit a poly-His tail) were adsorbed to the column. FPLC analysis using a MonoS cation exchanger was performed to understand and monitor the progress and time course of DAPase-I digestion of HT15-MBP to MBP. Optimization of process variables such as temperature, protein concentration, and enzyme activity was developed for the DAPase-I digesting system on HT15-MBP to MBP. In short, this study proved that the use of either Factor Xa or DAPase-I for the digestion of polyhistidine tags is simple and efficient and can be carried out under mild reaction conditions.     

Screening of suitable immobilized metal chelates for adsorption of monoclonal antibodies against mutant amidase from Pseudomonas aeruginosa

The chromatographic behaviour of monoclonal antibodies (MAbs) of IgM class against mutant (T103I) amidase from Pseudomonas aeruginosa was investigated. The effect of ligand concentration, the length of spacer arm and the nature of metal ion were investigated on immobilized metal ion affinity chromatography (IMAC). MAbs against mutant amidase adsorbed to Cu (II), Ni (II), Zn (II), Co (II) and Ca (II)-IDA agarose columns. The adsorption of MAbs onto immobilized metal chelates was pH dependent because an increase in the binding of MAbs was observed as the pH was raised from 6.0 to 8.0. The adsorption of MAbs to metal chelates was due to coordination of histidine residues which are available in the 3rd constant domain of heavy chain (CH3) of immunoglobulins since the presence of imidazole in the equilibration buffer abolished the adsorption of MAbs to the column packed with commercial IDA-Zn(II) agarose at pH 8.0. The combination of tailor-made stationary phases for IMAC and a correct choice of the adsorption conditions permitted to design a one-step purification procedure for MAbs of IgM class. Culture supernatants containing MAbs of IgM class against mutant amidase (T103I) were chromatographed by IMAC Co (II) column at pH 8.0. The results strongly suggest that one-step purification of MAbs of IgM class by IMAC is a cost-effective and process-compatible alternative to the other purification procedures.     

Recovery and purification of aprotinin from industrial insulin-processing effluent by immobilized chymotrypsin and negative IMAC chromatographies

Aprotinin, a bovine protease inhibitor currently also produced in recombinant bacteria, yeast, and corn, has valuable applications as a human therapeutic and in tissue culture. The objective of this work was to develop the basis of a large-scale aprotinin purification process centered on immobilized metal ion affinity chromatography (IMAC). This technique uses ligands—metal ions—of a lower cost and higher stability than those traditionally used in affinity chromatography. Since aprotinin does not interact with IMAC ligands, collection is from the nonretained fractions (negative chromatography). Stirred-tank batch IMAC adsorption experiments indicated that one-step aprotinin purification could not be successful. Immobilized chymotrypsin chromatography was then used as a prepurification step, yielding a suitable feed for IMAC (with purification factors as high as 476). IMAC column fed with these prepurified materials produced purified aprotinin in the nonretained fractions with purification factors as high as 952.     

Immobilized metal affinity chromatography of monoclonal immunoglobulin M against mutant amidase from Pseudomonas aeruginosa

The chromatographic behavior of monoclonal antibodies (MAbs) of immunoglobulin (Ig) M class against mutant (T103I) amidase from Pseudomonas aeruginosa was investigated on immobilized metal chelates. The effect of ligand concentration, the length of spacer arm, and the nature of metal ion were investigated in immobilized metal affinity chromatography (IMAC). The MAbs against mutant amidase adsorbed to Cu(II), Ni(II), Zn(II), Co(II), and Ca(II)-iminodiacetic acid (IDA) agarose columns. The increase in ligand concentration (epichlorohydrin: 30-60 and 1,4-butanediol-diglycidyl ether: 16-36) resulted in higher adsorption to IgM into immobilized metal chelates. The length of spacer arm was found to affect protein adsorption, as longer spacer arm (i.e., 1,4-butanediol-diglycidyl ether) increased protein adsorption of immobilized metal chelates. The adsorption of IgM onto immobilized metal chelates was pH dependent because an increase in the binding of IgM was observed as the pH varied from 6.0 to 8.0. The adsorption of IgM to immobilized metal chelates was the result of coordination of histidine residues to metal chelates that are available in the third constant domain of heavy chain (CH3) of immunoglobulins, as the presence of imidazole (5 mM) in the equilibration buffer abolished the adsorption of IgM to the column. The combination of tailor-made stationary phases for IMAC and a correct design of the adsorption parameters permitted to devise a one-step purification procedure for IgM. Culture supernatants containing IgM against mutant amidase (T103I) were purified either by IMAC on EPI-60-IDA-Co (II) column or by gel filtration chromatography on Sephacryl S-300HR. The specific content of IgM and final recovery of antibody activity exhibited similar values for both purification schemes. The purified preparations of IgM obtained by both schemes were apparently homogeneous on native polyacrylamide gel electrophoresis with a Mr of 851,000 Da. The results presented in this work strongly suggest that one-step purification of IgM by IMAC is a cost-effective and processcompatible alternative to other types of chromatography.     

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.     

Immobilized metal affinity chromatography of monoclonal immunoglobulin M against mutant amidase from Pseudomonas aeruginosa

The chromatographic behavior of monoclonal antibodies (MAbs) of immunoglobulin (Ig) M class against mutant (T103I) amidase from Pseudomonas aeruginosa was investigated on immobilized metal chelates. The effect of ligand concentration, the length of spacer arm, and the nature of metal ion were investigated in immobilized metal affinity chromatography (IMAC). The MAbs against mutant amidase adsorbed to Cu(II), Ni(II), Zn(II), Co(II), and Ca(II)-iminodiacetic acid (IDA) agarose columns. The increase in ligand concentration (epichlorohydrin: 30–60 and 1,4-butanediol-diglycidyl ether: 16–36) resulted in higher adsorption to IgM into immobilized metal chelates. The length of spacer arm was found to affect protein adsorption, as longer spacer arm (i.e., 1,4-butanediol-diglycidyl ether) increased protein adsorption of immobilized metal chelates. The adsorption of IgM onto immobilized metal chelates was pH dependent because an increase in the binding of IgM was observed as the pH varied from 6.0 to 8.0. The adsorption of IgM to immobilized metal chelates was the result of coordination of histidine residues to metal chelates that are available in the third constant domain of heavy chain (CH3) of immunoglobulins, as the presence of imidazole (5 mM) in the equilibration buffer abolished the adsorption of IgM to the column. The combination of tailor-made stationary phases for IMAC and a correct design of the adsorption parameters permitted to devise a one-step purification procedure for IgM. Culture supernatants containing IgM against mutant amidase (T103I) were purified either by IMAC on EPI-60-IDA-Co (II) column or by gel filtration chromatography on Sephacryl S-300HR. The specific content of IgM and final recovery of antibody activity exhibited similar values for both purification schemes. The purified preparations of IgM obtained by both schemes were apparently homogeneous on native polyacrylamide gel electrophoresis with a M _r of 851,000 Da. The results presented in this work strongly suggest that one-step purification of IgM by IMAC is a cost-effective and process-compatible alternative to other types of chromatography.     

One-step purification,covalent immobilization,and additional stabilization of a thermophilic poly-His-tagged beta-galactosidase from Thermus sp. strain T2 by using novel heterofunctional chelate-epoxy Sepabeads

Using the poly-His-tagged-beta-galactosidase from Thermus sp. strain T2 overexpressed in Escherichia coli (MC1116) as a model enzyme, we have developed a strategy to purify and immobilize proteins in a single step, combining the excellent properties of epoxy groups for enzyme immobilization with the good performance of immobilized metal-chelate affinity chromatography for protein purification. The aforementioned enzyme could not be immobilized onto standard epoxy supports with good yields, and after purification and storage, it exhibited a strong trend to yield very large aggregates as shown by ultracentrifugation experiments. That preparation could not be immobilized in any support, very likely because the pores of the solid became clogged by the large aggregates. These novel epoxy-metal chelate heterofunctional supports contain a low concentration of Co(2+) chelated in IDA groups and a high density of epoxy groups. This enabled the selective adsorption of poly-His-tagged enzymes, and as this adsorption step is necessary for the covalent immobilization procedure, the selective covalent immobilization of the target enzyme could take place. This strategy allowed similar maximum loadings of the target enzyme using either pure or crude preparations of the enzyme. The enzyme derivative presented a very high activity at 70 degrees C (over 1000 IU in the hydrolysis of lactose) and very high stability and stabilization when compared to its soluble counterpart (activity remained unaltered after several days of incubation at 50 degrees C). In fact, this preparation was much more stable than when the same enzyme was immobilized onto standard epoxy Sepabeads.     

Production,IMAC purification,and molecular modeling of N-carbamoyl-D-amino acid amidohydrolase C-terminally fused with a six-his peptide

A six-His peptide was genetically engineered to the C-terminus of Agrobacterium radiobacter N-carbamoyl-D-amino acid amidohydrolase monomer to facilitate the protein purification with immobilized metal affinity chromatography (IMAC). The fusion enzyme, named as DCaseH, was overexpressed in Escherichia coli and one-step IMAC-purified. The production study showed that DCaseH was optimally produced at 15 degrees C for 25 h by the induction of 0.05 mM IPTG. Both Co(2+)-chelated TANOL gels and Ni(2+)-chelated nitriloacetic acid agarose gels efficiently purified DCaseH, with the former yielding purer enzyme than the latter. Highly pure DCaseH was obtained in the former purification with the addition of 5 mM imidazole in the washing buffer, and the specific enzyme activity was increased more than 11-fold. Denaturing IMAC purification successfully purified DCaseH from inclusion bodies that were mostly composed of the overexpressed DCaseH, while the attempt to refold the purified enzyme by either dialysis or solid-state refolding was not achieved. The purified native enzyme was optimally active at pH 6.5 and 50 degrees C, and the presence of 10% glycerol increased the activity. The molecular modeling of dimeric DCaseH indicated that the six-His tags were freely exposed to the protein surface, resulting in the selective and effective IMAC purification of DCaseH.     

An efficient two step purification and molecular characterization of beta-galactosidases from Aspergillus oryzae

Beta-galactosidases (beta-D-galactoside-galactohydrolases (EC 3.2.1.23), lactases) are important industrial enzymes used for the hydrolysis of lactose from milk and milk whey. These enzymes are produced by different organisms and purified by multi-step procedures. The multi-step purification schemes are cost and time ineffective which can also lead to poor yield, denaturation and loss of enzymatic activity. In our study, extracellular beta-galactosidase from mutant strain Aspergillus oryzaeH26-10-7 was purified by a two step procedure, Metal-ion Affinity Chromatography (IMAC) followed by size-exclusion separation. Purified enzyme was characterized by sodium dodecyl Sulphate polyacrylamide gel electrophoresis (SDS-PAGE) and zymographic analysis. This fungal beta-galactosidase was characterized as a protein corresponding to 113 kDa. Enzyme from mutant strain was found to have five times higher catalytic activity on the synthetic substrate o-nitrophenyl-beta-D-galactopyranoside (ONPG) compared to the wild type enzyme. Moreover, the mutant enzyme was more thermo resistant compared to the wild type. This highly important technological characteristic can be exploited in food industry. Moreover, based on the IMAC patterns of wild type and mutant enzymes, similarities in their His topography were supposed.     

Rapid purification of the potato ADP-glucose pyrophosphorylase by polyhistidine-mediated chromatography

In an attempt to obtain facile methods to purify the heterotetrameric ADP-glucose pyrophosphorylase (AGPase), polyhistidine tags were attached to either the large (LS) or small (SS) subunits of this oligomeric enzyme. The addition of polyhistidine tag to the N-terminus of the LS or SS and co-expression with its unmodified counterpart subunit resulted in substantial induction of enzyme activity. In contrast, attachment of a polyhistidine-containing peptide through the use of a commercially available pET vector or addition of polyhistidine tags to the C-terminal ends of either subunit resulted in poor expression and/or production of enzyme activity. Preliminary experiment showed that these polyhistidine N-terminal-tagged enzymes interacted with Ni-NTA-agarose, indicating that immobilized metal affinity chromatography (IMAC) would be useful for efficient purification of the heterotetrameric AGPases. When ion-exchange chromatography step was employed prior to the IMAC, the polyhistidine-tagged AGPases were purified to near homogeneity. Comparison of kinetic parameters between AGPases with and without the polyhistidine tags revealed that attachment of the polyhistidine did not alter the allosteric and catalytic properties of the enzymes. These results indicate that polyhistidine tags will be useful for the rapid purification of preparative amounts of AGPases for biochemical and physical studies.     

Immobilised metal-ion affinity chromatography purification of histidine-tagged recombinant proteins: a wash step with a low concentration of EDTA

Immobilised metal-ion affinity chromatography (IMAC) is widely used for the purification of recombinant proteins in which a poly-histidine tag is introduced. However, other proteins may also bind to IMAC columns. We describe the use of a washing buffer with a low concentration of EDTA (0.5 mM) for the removal of proteins without histidine tag from IMAC columns. Four histidine-tagged recombinant proteins/protein complexes were purified to homogeneity from cell culture medium of insect cells by using an EDTA washing buffer. The presence of a low concentration of EDTA in washing buffers during IMAC may have a general application in the purification of histidine-tagged proteins.     

Biochemical characterization of a beta-galactosidase with a low temperature optimum obtained from an Antarctic arthrobacter isolate

A psychrophilic gram-positive isolate was obtained from Antarctic Dry Valley soil. It utilized lactose, had a rod-coccus cycle, and contained lysine as the diamino acid in its cell wall. Consistent with these physiological traits, the 16S ribosomal DNA sequence showed that it was phylogenetically related to other Arthrobacter species. A gene (bgaS) encoding a family 2 beta-galactosidase was cloned from this organism into an Escherichia coli host. Preliminary results showed that the enzyme was cold active (optimal activity at 18 degrees C and 50% activity remaining at 0 degrees C) and heat labile (inactivated within 10 min at 37 degrees C). To enable rapid purification, vectors were constructed adding histidine residues to the BgaS enzyme and its E. coli LacZ counterpart, which was purified for comparison. The His tag additions reduced the specific activities of both beta-galactosidases but did not alter the other characteristics of the enzymes. Kinetic studies using o-nitrophenyl-beta-D-galactopyranoside showed that BgaS with and without a His tag had greater catalytic activity at and below 20 degrees C than the comparable LacZ beta-galactosidases. The BgaS heat lability was investigated by ultracentrifugation, where the active enzyme was a homotetramer at 4 degrees C but dissociated into inactive monomers at 25 degrees C. Comparisons of family 2 beta-galactosidase amino acid compositions and modeling studies with the LacZ structure did not mimic suggested trends for conferring enzyme flexibility at low temperatures, consistent with the changes affecting thermal adaptation being localized and subtle. Mutation studies of the BgaS enzyme should aid our understanding of such specific, localized changes affecting enzyme thermal properties.     

Purification, immobilization, and characterization of a specific lipase from Staphylococcus warneri EX17 by enzyme fractionating via adsorption on different hydrophobic supports

Staphylococcus warneri strain EX17 produces three lipases with different molecular weights of 28, 30, and 45 kDa. The 45 kDa fraction (SWL-45) has been purified from crude protein extracts by one chromatographic step based on the selective adsorption of this lipase by interfacial activation on different hydrophobic supports at low ionic strength. The adsorption of SWL-45 on octyl-Sepharose increased the enzyme activity by 60%, but the other lipases were also adsorbed on this support. Using butyl-Toyopearl, which is a lesser hydrophobic support, the purification factor was close to 20, and the only protein band detected on the sodium dodecyl sulfate-polyacrylamide electrophoresis analysis gel was that corresponding to the SWL-45, which could be easily desorbed from the support by incubation with triton X-100, producing a purified enzyme. SWL-45 was immobilized under very mild conditions on cyanogen bromide Sepharose, showing similar activities and stability as for its soluble form but without intermolecular interaction. The effects of different detergents over the activity of the immobilized SWL-45 were analyzed, which was hyperactivated by factors of 1.3 and 2.5 with 0.01% Tween 80 and 0.1% Triton X-100, respectively, while ionic detergents produced detrimental effects on the enzyme activity even at very low concentrations. Optimal reaction conditions and the effect of other additives on the enzyme activity were also investigated.     

Effects of IMAC specific peptide tags on the stability of recombinant green fluorescent protein

Immobilized metal ion affinity chromatography (IMAC) using peptide affinity tags has become a popular tool for protein purification. An important feature dictating the use of a specific affinity tag is whether its structure influences the properties of the target protein to which it is attached. In this work we have studied the influence on protein stability of two novel peptide affinity tags, namely NT1A and HIT2, and compared their effect to the commonly used hexa‐histidine tag, all attached to the C‐terminus of a enhanced green fluorescent protein (eGFP). A comparison of the influence of C‐ or N‐terminal orientation of the tags was also carried out by studying the NT1A tag attached at either terminus of the eGFP. Protein stability was studied utilising guanidine hydrochloride equilibrium unfolding procedures and CD and fluorescence spectroscopy. The novel peptide affinity tags, NT1A and HIT2, and the His₆ tag were found to not affect the stability of eGFP. Although these results are protein specific, they highlight, nevertheless, the need to employ suitable characterisation tools if the impact of a specific peptide tag on the folded status or stability of a recombinant tagged protein, purified by immobilized metal ion affinity chromatographic methods, are to be rigorously evaluated and the appropriate choice of peptide tag made. © 2011 American Institute of Chemical Engineers Biotechnol. Prog., 2011     

Affinity chromatography of plasma proteins (guanidinobenzoatase): use of mimetic matrices and mimetic soluble ligands to prevent the binding of albumin on target affinity matrices

Serum albumin is the most abundant protein in plasma and it has a high capacity to bind many small compounds and macromolecules. In this way, albumin may promote important interferences during affinity chromatography of plasma proteins. Guanidinobenzoatase (GB) is a very relevant plasma protease that seems to be related to tumoral processes. This enzyme may be adsorbed on tailor-made agmatine-amide-agarose (CH-A) supports (e.g., the ones having 2 μmol of guanidino groups per ml of agarose attached to the support, through a 6 C aliphatic chain). Such tailor-made supports containing a very low concentration of ionized groups are hardly able to adsorb any protein by anion-exchange. However, they are able to strongly adsorb albumin. In order to solve this problem new mimetic affinity matrices have been designed: (i) by using the same ligand immobilized through a different chemical linkage [guanidino groups attached via secondary amino bonds, (AEA)] or (ii) by using slightly different ligands (e.g., 1,8-octanediamine containing a primary amino group instead of a guanidino one) also attached to the support via amido bonds (CH-DAO). Albumin adsorbs on the target and on the two mimetic matrices while GB is mainly adsorbed on the target one. Moreover, the adsorption of albumin on the affinity matrix (CH-A) is very strongly inhibited by the presence of low concentrations of soluble ligands (e.g., 1,8-octanediamine containing two ionized primary amino groups). On the contrary, the adsorption of GB on CH-A is hardly inhibited by the presence of such mimetic soluble ligand. In this way, the former offering of crude GB samples to AEA plus the use of mimetic inhibitors during adsorption of the extract on CH-A completely prevent the undesirable adsorption of albumin. In a such way, an extremely selective adsorption of GB can be performed. Such an improved chromatography procedure allows a very easy affinity purification and detection of GB.     

Protein Production in Yarrowia lipolytica Via Fusion to the Secreted Lipase Lip2p

We established a strategy for protein production and purification via expression in Yarrowia lipolytica as Lip2p fusion protein. To evaluate the expression system a cysteine-rich miniprotein, an antibody fragment and an enzyme showing galactose oxidase activity were chosen. These proteins have varying disulfide bond content, size, and structural complexity. Endogenous lipase Lip2p was used as a fusion partner to direct the fused proteins to the extracellular medium. A linker sequence was introduced at the junction of Lip2p and the respective fused protein that contains a hexahistidine tag followed by a TEV protease cleavage site. This allows for a specific and simple purification via IMAC for capturing the secreted proteins from the supernatant followed by a second IMAC for removing all contaminants after proteolytic release of the protein of interest. Up to 174 mg/L fusion protein was obtained using shake flask cultivation. Functionality of each of the purified proteins was confirmed by individual assays. Expression of proteins of interest via Lip2p fusion not only provides a convenient expression and purification scheme but also enables for an online monitoring of accumulation of secreted fusion proteins in the medium by exploiting the intrinsic lipase activity of the fusion.     

Human glutaredoxin 2 affinity tag for recombinant peptide and protein purification

Recombinant proteins are commonly expressed in fusion with an affinity tag to facilitate purification. We have in the present study evaluated the possible use of the human glutaredoxin 2 (Grx2) as an affinity tag for purification of heterologous proteins. Grx2 is a glutathione binding protein and we have shown in the present study that the protein can be purified from crude bacterial extracts by a one-step affinity chromatography on glutathione-Sepharose. We further showed that short peptides could be fused to either the N- or C-terminus of Grx2 without affecting its ability to bind to the glutathione column. However, when Grx2 was fused to either the 27 kDa green fluorescent protein or the 116 kDa beta-galactosidase, the fusion proteins lost their ability to bind glutathione-Sepharose. Insertion of linker sequences between the Grx2 and the fusion protein did not restore binding to the column. In summary, our findings suggest that Grx2 may be used as an affinity tag for purification of short peptides and possibly also certain proteins that do not interfere with the binding to glutathione-Sepharose. However, the failure of purifying either green fluorescent protein or beta-galactosidase fused to Grx2 suggests that the use of Grx2 as an affinity tag for recombinant protein purification is limited.     

Expression of human BK ion channels in Sf9 cells, their purification using metal affinity chromatography, and functional reconstitution into planar lipid bilayers

This report describes a procedure for purification of large conductance calcium-activated potassium (BK, maxi-K) channels using immobilised metal affinity chromatography (IMAC) under non-denaturing conditions. An amino-terminal histidine fusion tag was added to hSlo, the human BK channel, and expressed in Sf9 insect cells. Following IMAC purification and production of proteoliposomes, protein function was assessed electrophysiologically in planar bilayer lipid membranes. Single channel openings had conductances of 250-300 pS and were inhibited by paxilline, demonstrating that the BK channels remained functional following IMAC purification. This method to obtain functional human ion channels will be useful in assays to screen potential pharmaceuticals.