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.     

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

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

Production and purification of single chain human insulin precursors with various fusion peptides

For the production and purification of a single chain human insulin precursor four types of fusion peptides β-galactosidase (LacZ), maltose binding protein (MBP), glutathione-S-transferase (GST), and (His)₆-tagged sequence (HTS) were investigated. RecombinantE. coli harboring hybrid genes was cultivated at 37°C for 1 h, and gene induction occurred when 0.2 mM of isopropyl-D-thiogalactoside (IPTG) was added to the culture broth, except forE. coli BL21 (DE3) pLysS harboring a pET-BA cultivation with 1.0 mM IPTG, followed by a longer than 4 h batch fermentation respectively. DEAE-Sphacel and Sephadex G-200 gel filtration chromatography, amylose affinity chromatography, glutathione-sepharose 4B affinity chromatography, and a nickel chelating affinity chromatography system as a kind of immobilized metal ion affinity chromatography (IMAC) were all employed for the purification of a single chain human insulin precursor. The recovery yields of the HTS-fused, GST-fused, MBP-fused, and LacZ-fused single chain human insulin precursors resulted in 47%, 20%, 20%, and 18% as the total protein amounts respectively. These results show that a higher recovery yield of the finally purified recombinant peptides was achieved when affinity column chromatography was employed and when the fused peptide had a smaller molecular weight. In addition the pET expression system gave the highest productivity of a fused insulin precursor due to a two-step regulation of the gene expression, and the HTS-fused system provided the highest recovery of a fused insulin precursor based on a simple and specific separation using the IMAC technique     

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.     

Production of interferon-α in high cell density cultures of recombinant Escherichia coli and its single step purification from refolded inclusion body proteins

Escherichia coli TG1 transformed with a temperature-regulated interferon-α expression vector was grown to high cell density in defined medium containing glucose as the sole carbon and energy source, utilizing a simple fed-batch process. Feeding was carried out to achieve an exponential increase in biomass at growth rates which minimized acetate production. Thermal induction of such high cell density cultures resulted in the production of ∼4 g interferon-α/l culture broth. Interferon-α was produced exclusively in the form of insoluble inclusion bodies and was solubilized under denaturing conditions, refolded in the presence of arginine and purified to near homogeneity, utilizing single-step ion-exchange chromatography on Q-Sepharose. The yield of purified interferon-α was ∼300 mg/l with respect to the original high cell density culture broth (overall yield of ∼7.5% active interferon-α). The purified recombinant interferon-α was found by different criteria to be predominantly monomeric and possessed a specific bioactivity of ∼2.5 × 10⁸ IU/mg based on viral cytopathic assay. Received: 8 October 1999 / Received revision: 8 December 1999 / Accepted: 12 December 1999     

Enhancement of polysialic acid yield by reducing initial phosphate and feeding ammonia water to <Emphasis Type="Italic">Escherichia coli</Emphasis> CCTCC M208088

Polysialic acid (PSA) is a capsular polysaccharide obtained from aerobic fermentation with Escherichia coli. To enhance PSA production and eliminate the influence of phosphate on the PSA purification process, a lower level of initial phosphate was adopted with pH control. The resulting PSA yield reached 4.1 g/L in fed-batch fermentation with 2.5 g/L K₂HPO₄ and E. coli strain CCTCC M208088. In addition, an ammonia water (NH₄OH) feeding strategy to control the pH at 6.4 was developed resulting in PSA production that reached as high as 5.2 g/L. NMR spectra confirmed the purified biopolymer as a α-2,8 linked PSA, identical to the published NMR spectra, with a molecular weight in the range of 16 ∼ 50 kDa.     

Cloning and characterization of a thermostable xylitol dehydrogenase from Rhizobium etli CFN42

An NAD⁺-dependent xylitol dehydrogenase from Rhizobium etli CFN42 (ReXDH) was cloned and overexpressed in Escherichia coli. The DNA sequence analysis revealed an open reading frame of 1,044 bp, capable of encoding a polypeptide of 347 amino acid residues with a calculated molecular mass of 35,858 Da. The ReXDH protein was purified as an active soluble form using GST affinity chromatography. The molecular mass of the purified enzyme was estimated to be ∼34 kDa by sodium dodecyl sulfate–polyacrylamide gel and ∼135 kDa with gel filtration chromatography, suggesting that the enzyme is a homotetramer. Among various polyols, xylitol was the preferred substrate of ReXDH with a K _m = 17.9 mM and k_cat /K _m = 0.5 mM⁻¹ s⁻¹ for xylitol. The enzyme had an optimal pH and temperature of 9.5 and 70 °C, respectively. Heat inactivation studies revealed a half life of the ReXDH at 40 °C of 120 min and a half denaturation temperature (T _1/2) of 53.1 °C. ReXDH showed the highest optimum temperature and thermal stability among the known XDHs. Homology modeling and sequence analysis of ReXDH shed light on the factors contributing to the high thermostability of ReXDH. Although XDHs have been characterized from several other sources, ReXDH is distinguished from other XDHs by its high thermostability.     

Production, purification and characterization of laccase from Pleurotus ostreatus grown on tomato pomace

A strain of Pleurotus ostreatus was grown in tomato pomace as sole carbon source for production of laccase. The culture of P. ostreatus revealed a peak of laccase activity (147 U/L of fermentation broth) on the 4th day of culture with a specific activity of 2.8 U/mg protein. Differential chromatographic behaviour of laccase was investigated on affinity chromatographic matrices containing either urea, acetamide, ethanolamine or IDA as affinity ligands. Laccase exhibited retention on such affinity matrices and it was purified on a Sepharose 6B—BDGE—urea column with final enzyme recoveries of about 60%, specific activity of 6.0 and 18.0 U/mg protein and purification factors in the range of 14–46. It was also possible to demonstrate that metal-free laccase did not adsorb to Sepharose 6B—BDGE—urea column which suggests that adsorption of native laccase on this affinity matrix was apparently due to the specific interaction of carbonyl groups available on the matrix with the active site Cu (II) ions of laccase. The kinetic parameters (V _max, K _m , K _cat, and K _cat/K _m ) of the purified enzyme for several substrates were determined as well as laccase stability and optimum pH and temperature of enzyme activity. This is the first report describing the production of laccase from P. ostreatus grown on tomato pomace and purification of this enzyme based on affinity matrix containing urea as affinity ligand.     

Cloning and characterization of a ribitol dehydrogenase from Zymomonas mobilis

Ribitol dehydrogenase (RDH) catalyzes the conversion of ribitol to d-ribulose. A novel RDH gene was cloned from Zymomonas mobilis subsp. mobilis ZM4 and overexpressed in Escherichia coli BL21(DE3). DNA sequence analysis revealed an open reading frame of 795 bp, capable of encoding a polypeptide of 266 amino acid residues with a calculated molecular mass of 28,426 Da. The gene was overexpressed in E. coli BL21(DE3) and the protein was purified as an active soluble form using glutathione S-transferase affinity chromatography. The molecular mass of the purified enzyme was estimated to be ∼28 kDa by sodium dodecyl sulfate-polyacrylamide gel and ∼58 KDa with gel filtration chromatography, suggesting that the enzyme is a homodimer. The enzyme had an optimal pH and temperature of 9.5 and 65°C, respectively. Unlike previously characterized RDHs, Z. mobilis RDH (ZmRDH) showed an unusual dual coenzyme specificity, with a k _cat of 4.83 s⁻¹ for NADH (k _cat/K _m = 27.3 s⁻¹ mM⁻¹) and k _cat of 2.79 s⁻¹ for NADPH (k _cat/K _m = 10.8 s⁻¹ mM⁻¹). Homology modeling and docking studies of NAD⁺ and NADP⁺ into the active site of ZmRDH shed light on the dual coenzyme specificity of ZmRDH.     

High constitutive peroxidase activity and constitutive thermotolerance in <Emphasis Type="Italic">Neurospora crassa</Emphasis>

 During the isolation of mutations in the heat-inducible hsp70-1 gene of Neurospora crassa by RIP (repeat-induced point mutations), several transformants were generated by electroporation of conidia with a plasmid harboring an incomplete copy of this gene. One isolate, designated E-45, containing ectopically integrated hsp70-1 DNA, exhibited a slow growth rate, low-temperature sensitivity, constitutive thermotolerance (without prior heat shock), and high constitutive peroxidase activity. The constitutive form of peroxidase (CP) was distinguishable from the heat-inducible form (HIP) by immunoinactivation employing polyclonal antiserum against the latter enzyme and by electrophoretic resolution in nondenaturing polyacrylamide gels. This enzyme was purified to near homogeneity and some of its properties examined. The relative molecular mass of native CP was in the range of 118–136 kDa, as estimated by gel filtration analysis on size exclusion matrices, whereas SDS-PAGE analysis yielded a size of ∼37 kDa for the polypeptide. Substrate saturation kinetics studies were conducted using ABTS [2,2′-azino-bis (3-ethylbenzthiazole-6-sulfonic acid)] and H₂O₂ as substrates: K _m, V _max, and K _cat values for H₂O₂ were ∼22 μM, ∼447 nmol mg⁻¹, and 0.33 s⁻¹, respectively, and those for ABTS were ∼55 μM, ∼453 nmol mg⁻¹, and 0.3 s⁻¹, respectively. Guaiacol was not used as a substrate by this enzyme. CP peroxidase was shown to be a heme-containing enzyme, stable at temperatures up to 58°C. Received: August 5, 2002 / Accepted: January 22, 2003 Acknowledgments This work was supported by an operating grant from the Natural Sciences and Engineering Research Council (NSERC) of Canada (to M.K.). The financial support provided to A. M. in the form of a graduate studentship award by the AHFMR (Alberta Heritage Foundation for Medical Research) and of a graduate teaching assistantship to A. S. by the Department of Biological Sciences, University of Calgary, is gratefully acknowledged. Correspondence to:M. Kapoor     

Liquid fermentation to produce biomass of mycoherbicidal strains of Fusarium oxysporum

Conditions for optimizing spore production, especially chlamydospores, by host-specific mycoherbicidal strains of Fusarium oxysporum causing vascular wilts in coca (Erythroxylum coca) and poppy (Papaver somniferum) were studied in 2.5-1 fermentors. The fermentor dissolved oxygen and pH had significant effects on the growth characteristics of F. oxysporum strains. The effect of the fungal strain, however was not significant for most of the variables studied except for chlamydospore formation. After 14 days of fermentation, the spore types produced were microconidia and chlamydospores, with very little production of macroconidia. While the total viable counts were significantly higher under high than under low dissolved O₂, the chlamydospore counts were significantly higher under low than under high dissolved O₂. The percentage of chlamydospores obtained, as a proportion of total viable was significantly higher when the fermentor pH was increased, than when it was not. Scaling-up the liquid fermentation to 20 l, yielded log₁₀ c = 6.8 (where c = chlamydospores ml⁻¹) after 14 days' fermentation, with biomass viable counts of log₁₀ v∼8.0 (where v = viable counts g⁻¹ air-dried biomass). A single-step liquid fermentation reported in this study increased chlamydospore yields and reduced the time required for their production with techniques currently available from 5 weeks to less than 2 weeks. Received: 24 April 1997 / Received revision: 6 August 1997 / Accepted: 29 August 1997     

Purification, characterization, and immunolocalization of hydroxycinnamoyl-CoA: tyramine N-(hydroxycinnamoyl)transferase from opium poppy

A development-specific and elicitor-inducible acyltransferase [hydroxycinnamoyl-CoA: tyramine N-(hydroxycinnamoyl)transferase (THT; EC 2.3.1.110)] that catalyzes the transfer of hydroxycinnamic acids from hydroxycinnamoyl-CoA esters to hydroxyphenethylamines was purified 988-fold to apparent homogeneity from opium poppy (Papaver somniferum L.) cell-suspension cultures. The purification procedure, which resulted in a 6.8% yield, involved hydrophobic interaction and anion-exchange chromatography, followed by affinity chromatography on Reactive Yellow-3-Agarose using the acyl donor (feruloyl-CoA) as eluent. Purified THT had an isoelectric point of 5.2, a native molecular mass of approximately 50 kDa, and consisted of two apparently identical 25-kDa subunits as determined by two-dimensional polyacrylamide gel electrophoresis. The purified enzyme was able to synthesize a variety of amides due to a relatively low specificity for cinnamoyl-CoA derivatives and hydroxyphenethylamines. The best substrates were feruloyl-CoA (VK _m ⁻¹13.4 mkat g⁻¹ M⁻¹) and tyramine (VK _m ⁻¹6.57 mkat g⁻¹ M⁻¹). The THT activity increased during development of opium poppy seedlings, occurred at high levels in roots and stems of mature plants, and was induced in cell-suspension cultures after treatment with a pathogen-derived elicitor. Immunoblot analysis using THT mouse polyclonal antibodies did not always show a correlation between THT polypeptide and enzyme activity levels. For example, despite low THT activity in leaves, an abundant 25-kDa immunoreactive polypeptide was detected. Immunohistochemical localization showed that THT polypeptides occur in cortical and xylem parenchyma, immature xylem vessel elements, root periderm, anthers, ovules, and the inner layer of the seed coat, but are most abundant in phloem sieve-tube members in roots, stems, leaves, and anther filaments. Received: 19 January 1999 / Accepted: 3 March 1999     

Production of glutamine synthetase in <Emphasis Type="Italic">Escherichia coli</Emphasis> using SUMO fusion partner and application to <Emphasis Type="SmallCaps">l</Emphasis>-glutamine synthesis

l-glutamine (Gln) is an important conditionally necessary amino acid in human body and potential demand in food or medicine industry is expected. High efficiency of l-Gln production by coupling genetic engineered bacterial glutamine synthetase (GS) with yeast alcoholic fermentation system has been developed. We report here first the application of small ubiquitin-related modifier (SUMO) fusion technology to the expression and purification of recombinant Bacillus subtilis GS. In order to obtain GS with high Gln-forming activity, safety and low cost for food and pharmaceutics industry, 0.1% (w/v) lactose was selected as inducer. The fusion protein was expressed in totally soluble form in E. coli, and expression was verified by SDS–PAGE and western blot analysis. The fusion protein was purified to 90% purity by nickel nitrilo-triacetic acid (Ni–NTA) resin chromatography with a yield of 625 mg per liter fermentation culture. After the SUMO/GS fusion protein was cleaved by the SUMO protease, the cleaved sample was reapplied to a Ni–NTA column. Finally, about 121 mg recombinant GS was obtained from 1 l fermentation culture with no less than 96% purity. The recombinant purified GS showed great transferase activity (23 U/mg), with 25 U recombinant GS in a 50 ml reaction system, a biosynthesis yield of 27.5 g/l l-Gln was detected by high pressure liquid chromatography (HPLC) or thin-layer chromatography. Thus, the application of SUMO technology to the expression and purification of GS potentially could be employed for the industrial production of l-Gln.     

Two-stage method for purification of ceruloplasmin based on its interaction with neomycin

A two-stage chromatography that yields highly purified ceruloplasmin (CP) from human plasma and from rat and rabbit serum is described. The isolation procedure is based on the interaction of CP with neomycin, and it provides a high yield of CP. Constants of inhibition by gentamycin, kanamycin, and neomycin of oxidase activity of CP in its reaction with p-phenylenediamine were assayed. The lowest K _i for neomycin (11 μM) corresponded to the highest specific adsorption of CP on neomycin-agarose (10 mg CP/ml of resin). Isolation of CP from 1.4 liters of human plasma using ion-exchange chromatography on UNO-Sphere Q and affinity chromatography on neomycin-agarose yields 348 mg of CP with 412-fold purification degree. Human CP preparation obtained with A ₆₁₀/A ₂₈₀ ∼ 0.052 contained neither immunoreactive prothrombin nor active thrombin. Upon storage at 37°C under sterile conditions, the preparation remained stable for two months. Efficient preparation of highly purified CP from rat and rabbit sera treated according to a similar protocol suggests the suitability of our method for isolation of CP from plasma and serum of other animals. The yield of CP in three separate purifications was no less than 78%.     

Evaluation of cell recycling in continuous fermentation of enzymatic hydrolysates of spruce with Saccharomyces cerevisiae and on-line monitoring of glucose and ethanol

The maximum growth rate of Saccharomyces cerevisiae ATCC 96581, adapted to fermentation of spent sulphite liquor (SSL), was 7 times higher in SSL of hardwood than the maximum growth rate of bakers' yeast. ATCC 96581 was studied in the continuous fermentation of spruce hydrolysate without and with cell recycling. Ethanol productivity by ATCC 96581 in continuous fermentation of an enzymatic hydrolysate of spruce was increased 4.6 times by employing cell recycling. On-line analysis of CO₂, glucose and ethanol (using a microdialysis probe) was used to investigate the effect of fermentation pH on cell growth and ethanol production, and to set the dilution rate. Cell growth in the spruce hydrolysates was strongly influenced by fermentation pH. The fermentation was operated in continuous mode for 210 h and a theoretical ethanol yield on fermentable sugars was obtained. Received: 25 May 1998 / Received revision: 11 August 1998 / Accepted: 12 August 1998     

A novel downstream process for 1,3-propanediol from glycerol-based fermentation

In this paper, a downstream process for purification of 1,3-propanediol from glycerol-based fermentation broth was investigated. The purification of 1,3-propanediol from fermentation broth was achieved by a process combining microfiltration, charcoal treatment, vacuum distillation, and silica gel chromatography. The broth was first filtered through hollow fiber cartridge, wherein 98.7% of biomass was removed. Soluble proteins and other color impurities in the broth were removed by the use of activated charcoal at optimal concentration of 30 g l⁻¹ where the soluble proteins in the broth decreased to 0.1 g l⁻¹ (96.0% protein loss). The obtained broth when concentrated by vacuum distillation resulted in the crystallization of inorganic salts. Subsequently, 1,3-propanediol was purified by gradient chromatography using silica gel as a stationary phase and mixture of chloroform and methanol as a mobile phase. Finally, with the optimal flow rate of 10 ml min⁻¹ and loading amount of 80 ml, the yield of 1,3-propanediol achieved was 89%. The overall yield of 1,3-propanediol using the proposed procedure was 75.47%. The developed method was found to be a simple, rapid, and efficient procedure for the purification of 1,3-propanediol from fermentation broth.     

Purification and characterization of a glucokinase from young tomato (Lycopersicon esculentum L. Mill.) fruit

In order to clearly establish the properties of the enzymes responsible for hexose phosphorylation we have undertaken the separation and characterization of these enzymes present in tomato fruit (Martinez-Barajas and Randall 1996). This report describes the partial purification and characterization of glucokinase (EC. 2.7.1.1) from young green tomato fruit. The procedure yielded a 360-fold enrichment of glucokinase. Tomato fruit glucokinase is a monomer with a molecular mass of 53 kDa. Glucokinase activity was optimal between pH 7.5 and 8.5, preferred ATP as the phosphate donor (K _m = 0.223 mM) and exhibited low activity with GTP or UTP. The tomato fruit glucokinase showed highest affinity for glucose (K _m = 65 μM). Activity observed with glucose was 4-fold greater than with mannose and 50-fold greater than with fructose. The tomato fruit glucokinase was sensitive to product inhibition by ADP (K _i = 36 μM). Little inhibition was observed with glucose 6-phosphate (up to 15 mM) at pH 8.0; however, at pH 7.0 glucokinase activity was inhibited 30–50% by physiological concentrations of glucose 6-phosphate. Received: 4 October 1997 / Accepted: 10 January 1998     

N‐terminal processing of affinity‐tagged recombinant proteins purified by IMAC procedures

The ability of a new class of metal binding tags to facilitate the purification of recombinant proteins, exemplified by the tagged glutathione S‐transferase and human growth hormone, from Escherichia coli fermentation broths and lysates has been further investigated. These histidine‐containing tags exhibit high affinity for borderline metal ions chelated to the immobilised ligand, 1,4,7‐triazacyclononane (tacn). The use of this tag‐tacn immobilised metal ion affinity chromatography (IMAC) system engenders high selectivity with regard to host cell protein removal and permits facile tag removal from the E. coli‐expressed recombinant protein. In particular, these tags were specifically designed to enable their efficient removal by the dipeptidyl aminopeptidase 1 (DAP‐1), thus capturing the advantages of high substrate specificity and rates of cleavage. MALDI‐TOF MS analysis of the cleaved products from the DAP‐1 digestion of the recombinant N‐terminally tagged proteins confirmed the complete removal of the tag within 4‐12 h under mild experimental conditions. Overall, this study demonstrates that the use of tags specifically designed to target tacn‐based IMAC resins offers a comprehensive and flexible approach for the purification of E. coli‐expressed recombinant proteins, where complete removal of the tag is an essential prerequisite for subsequent application of the purified native proteins in studies aimed at delineating the molecular and cellular basis of specific biological processes. Copyright © 2015 John Wiley & Sons, Ltd.     

Purification of a bifunctional amylase/protease inhibitor from ragi (Eleusine coracana) by chromatography and its use as an affinity ligand

An ammonium sulphate fraction (20–60%) of bifunctional amylase/protease inhibitor from ragi (Eleusine coracana) was purified by affinity chromatography to give 6.59-fold purity with 81.48% yield. The same ammonium sulphate fraction was also subjected to ion exchange chromatography and was purified 4.28-fold with 75.95% yield. The ion exchange fraction was subjected to gel filtration and the inhibitor was purified to 6.67-fold with 67.36% yield. Further sodium dodecyl sulphate-polyacrylamide gel electrophoresis (SDS-PAGE) was performed to check the homogeneity of purified amylase/trypsin inhibitor obtained through affinity, ion exchange and gel chromatography. The molecular weight of the inhibitor was found to be 14 kDa. This purified inhibitor was used as affinity ligand for the purification of a commercial preparation of pancreatic amylase.