Affinity precipitation of Aspergillus niger pectinase by microwave-treated alginate

Affinity precipitation is a simple, single plate separation process in which the complex of a smart macroaffinity ligand with the target protein (from a crude broth) can be selectively precipitated by application of a suitable stimulus. Alginate is a copolymer of guluronic acid and mannuronic acid residues and precipitates with Ca(2+) ions. It was found to bind to pectinase present in a commercial preparation of Aspergillus niger, Pectinex Ultra-SPL. Microwave pretreatment of alginate at 75 degrees C was found to enhance the selectivity of the affinity precipitation. Using microwave-treated alginate, 83% of the enzyme activity with 20-fold purification could be recovered. SDS-PAGE upon silver staining confirmed the enhanced selectivity of affinity precipitation when microwave-treated alginate was used.     

Macroaffinity ligand-facilitated three-phase partitioning for purification of glucoamylase and pullulanase using alginate

Starch-degrading enzymes glucoamylase (from Aspergillus niger), and pullulanase (from Bacillus acidopullulyticus) were purified using alginates (polysaccharides consisting of mannuronic acids and guluronic acids) by a recently developed technique called macroaffinity ligand-facilitated three-phase partitioning (MLFTPP). In this process, a crude preparation of the enzyme was mixed with alginate. On addition of appropriate amounts of ammonium sulfate and t-butanol, the alginate bound enzyme appeared as an interfacial precipitate between the lower aqueous and the upper t-butanol phase. Enzyme activity from this interfacial precipitate was recovered using 1M maltose. Glucoamylase and pullulanase were purified 20- and 38-fold with 83% and 89% activity recovery, respectively. Both the purified preparations showed a single band on SDS-PAGE.     

Macroaffinity ligand-facilitated three-phase partitioning (MLFTPP) for purification of xylanase

It is shown that eudragit S-100, a copolymer of methylacrylic acid and methylmethacrylate, undergoes three-phase partitioning. It was found that 95% eudragit S-100 could be recovered as the interfacial precipitate by using 30% (w/v) ammonium sulfate, 1:1 ratio of t-butanol to polymer solution at 40 degrees C. Three-phase partitioning of proteins uses simultaneous addition of ammonium sulfate and t-butanol to precipitate proteins in an interfacial layer separating the aqueous phase and organic solvent. Exploiting the affinity of xylanases towards eudragit S-100, it was possible to purify xylanase from Aspergillus niger; 60% recovery of activity with 95-fold purification could be obtained by this process. The purified enzyme showed A single band on SDS-PAGE. The technique shows promise to develop into a general method that could be termed "macroaffinity ligand-facilitated three-phase partitioning (MLFTPP).     

One-step purification of glucoamylase by affinity precipitation with alginate.

It was found that alginate binds to glucoamylase, presumably through the recognition of starch binding domain of the latter. The present work exploits this for purification of glucoamylases from commercial preparation of Aspergillus niger and crude culture filtrate of Bacillus amyloliquefaciens by affinity precipitation technique in a single-step protocol. Glucoamylase is selectively precipitated using alginate as macroaffinity ligand and later eluted with 1.0 M maltose. In the case of A. niger, 81% activity is recovered with 28-fold purification. The purified glucoamylase gave a single band on SDS-PAGE corresponding to 78 kDa molecular weight. The developed affinity precipitation process also works efficiently for purification of Bacillus amyloliquefaciens glucoamylase from its crude culture filtrate, giving 78% recovery with 38-fold purification. The purified preparation showed a major band corresponding to 62 kDa and a faint band about 50 kDa on SDS-PAGE. The latter corresponds to the molecular weight for alpha-amylase of Bacillus amyloliquefaciens.     

Free polymeric bioligands in aqueous two-phase affinity extractions of microbial xylanases and pullulanase

Two reversibly soluble-insoluble polymers (viz. Eudragit S-100 and alginate) were used as free macroaffinity bioligands in polyethylene glycol (PEG)/salt two-phase systems for separation of enzymes. Incorporation of Eudragit S-100 and alginate in the PEG phase led to considerable selectivity in separation of microbial xylanases and pullulanase, respectively. Xylanase from Aspergillus niger was recovered 93% with 56-fold purification, whereas the enzyme from Trichoderma reesei and Bacillus amyloliquefaciens was obtained with 93% activity recovery (31-fold purification) and 90% activity recovery (32-fold purification), respectively. From Bacillus acidopullulyticus pullulanase, 85% enzyme activity recovery with 44-fold purification was obtained. The approach described here shows the potential of developing into a general approach for use of reversibly soluble-insoluble macroaffinity ligand in two-phase affinity extraction.     

Simultaneous refolding/purification of xylanase with a microwave treated smart polymer

Affinity precipitation with a smart polymer, Eudragit S-100 (a methyl methacrylate polymer), was exploited for simultaneous refolding and purification of xylanase. Affinity precipitation consisted of this reversibly soluble-insoluble polymer-binding xylanase selectively. The complex was precipitated by lowering the pH and xylanase was eluted off the polymer using 1 M NaCl. For refolding experiments, the commercial preparation of Aspergillus niger xylanase was denatured with 8 M urea. Addition of microwave irradiated Eudragit S-100 and affinity precipitation led to recovery of 96% enzyme activity by refolding. Simultaneously, the enzyme was purified 45 times. Thermally inactivated preparation, when subjected to similar steps, led to 95% recovery of enzyme activity with 42-fold purification. The strategy has the potential for recovering pure proteins in active forms from overexpressed proteins, which generally form inclusion bodies in E. coli.     

Purification of alpha-galactosidase by affinity precipitation with alginate

Affinity precipitation is a technique which is known for over 20 years, but has recently received more attention due to the development of new materials for its implementation. It is a relatively simple, convenient, and reproducible technique that results in high target molecule recovery at high specificity. We describe, here, an efficient and rapid purification procedure for Vicia faba alpha-galactosidase (EC 3.2.1.22) by using affinity precipitation with alginate. The enzyme was purified with 43% activity yield and 40-fold purification. SDS-PAGE of the purified enzyme showed a single band and a subunit weight of 44 kDa. The properties of the enzyme were also searched. The results showed that the general properties of the enzyme offer potential for use of this alpha-galactosidase in several production processes.     

Simultaneous refolding and purification of recombinant proteins by macro-(affinity ligand) facilitated three-phase partitioning

A strategy called macro-(affinity ligand) facilitated three-phase partitioning (MLFTPP) is described for refolding of a diverse set of recombinant proteins starting from the solubilized inclusion bodies. It essentially consists of: (i) binding of the protein with a suitable smart polymer and (ii) precipitating the polymer-protein complex as an interfacial layer by mixing in a suitable amount of ammonium sulfate and t-butanol. Smart polymers are stimuli-responsive polymers that become insoluble on the application of a suitable stimulus (e.g., a change in the temperature, pH, or concentration of a chemical species such as Ca(2+) or K(+)). The MLFTPP process required approximately 10min, and the refolded proteins were found to be homogeneous on sodium dodecyl sulfate-polyacrylamide gel electrophoresis. The folded proteins were characterized by fluorescence emission spectroscopy, circular dichroism spectroscopy, biological activity, melting temperature, and surface hydrophobicity measurements by 8-anilino-1-naphthalenesulfonate fluorescence. Two refolded antibody fragments were also characterized by measuring K(D) by Biacore by using immobilized HIV-1 gp120. The data demonstrate that MLFTPP is a rapid and convenient procedure for refolding a variety of proteins from inclusion bodies at high concentration. Although establishing the generic nature of the approach would require wider trials by different groups, its success with the diverse kinds of proteins tried so far appears to be promising.     

Three phase partitioning of carbohydrate polymers: separation and purification of alginates

Three phase partitioning, a technique described for protein purification, has been employed for precipitation and purification of three different commercial preparations of alginates. Three phase partitioning works by the addition of t-butanol to aqueous solution of the polymer containing 20–30% ammonium sulphate (w/v). Three phases formed are: upper t-butanol layer, interfacial polymer precipitate and lower aqueous phase. In all the three cases, the process optimization was carried out by varying ammonium sulphate concentration, volume of t-butanol, alginate concentration and temperature. Fluorescence spectroscopy was used to show that repeated cycles of TPP also resulted in considerable reduction in polyphenol content of a crude alginate preparation.     

Purification of α-Galactosidase by Affinity Precipitation with Alginate

Abstract

Affinity precipitation is a technique which is known for over 20 years, but has recently received more attention due to the development of new materials for its implementation. It is a relatively simple, convenient, and reproducible technique that results in high target molecule recovery at high specificity. We describe, here, an efficient and rapid purification procedure for Vicia faba α-galactosidase (EC 3.2.1.22) by using affinity precipitation with alginate. The enzyme was purified with 43% activity yield and 40-fold purification. SDS-PAGE of the purified enzyme showed a single band and a subunit weight of 44 kDa. The properties of the enzyme were also searched. The results showed that the general properties of the enzyme offer potential for use of this α-galactosidase in several production processes.     

An improved purification procedure of alkaline phosphatase from calf intestine by applying partition in aqueous two-phase systems and dye-ligand chromatography.

Aqueous two-phase partitioning has been elaborated in order to improve the purification of alkaline phosphatase from calf intestine in larger scale. The laborious precipitation and centrifugation steps for the removal of the enzyme from the cell debris and from the bulk protein were replaced by this technique yielding a high recovery (88%) and a significant lower time requirement. For the preparation of 100.000 units (46 mg) of a homogeneous enzyme 2.0 kg of a system containing 200 g PEG 4000 and only 10 g dextran M 70 is necessary. Affinity partitioning in aqueous two-phase systems was used to screen 41 dyes for selecting a suitable ligand for the dye-ligand chromatography of the enzyme. In the case of alkaline phosphatase the results obtained by affinity partitioning coincide with the experimental requirements for the affinity chromatography of the enzyme. Procion Navy HE-R (Blue 171) exhibits a high affinity, selectivity and binding capacity for the enzyme compared with other dyes investigated. The purification procedure provided the same degree in purity (2200 U/mg) and yield (59%) if mucosa or chyme was applied as starting material. In the range of practical use the purified enzyme contains no detectable activities of DNAses (endonucleases) and DNA-nicking activities. The contamination with phosphodiesterase I (EC. 3.1.4.1.) is less than 0.01%.     

Pectinase partitioning in polyethylene glycol 1000/Na2SO4 aqueous two-phase system: statistical modeling of the experimental results

Statistical models concerning partitioning of pectinase in polyethylene glycol 1000/Na₂SO₄ aqueous two-phase system were established with response surface methodology. Concentrations of polyethylene glycol 1000 and Na₂SO₄ were selected as independent variables to evaluate their impact on parameters of partitioning in aqueous two-phase system—the partition coefficient of pectinase, purification factor and pectinase yield. An experimental space where over 2.5-fold purification was achieved, followed by over 90% yield of pectinase. The established models showed good prediction of partitioning parameters.     

Three-phase partitioning for simultaneous renaturation and partial purification of Aspergillus niger xylanase

Three-phase partitioning (TPP) is carried out by mixing ammonium sulfate and t-butanol to obtain organic phase, interfacial precipitate and aqueous phase. It is shown that TPP of an 8 M urea/100 mM dithiothreitol-denatured xylanase preparation resulted in simultaneous renaturation and purification. This integrated novel approach gave recovery of 93% enzyme activity with 21-fold purification. The implications of this in the context of recovering activity from inclusion bodies are discussed.     

Recovery of endo-polygalacturonase using polyethylene glycol-salt aqueous two-phase extraction with polymer recycling

The partitioning behaviour of endo-polygalacturonase (endo-PG) and total protein from a clarified Kluyveromyces marxianus fermentation broth in polyethylene glycol (PEG)-ammonium sulfate and PEG-potassium phosphate (pH=7) aqueous two-phase systems was experimentally investigated. Both the enzyme and total protein partitioned in the bottom phase for these two kinds of systems. The enzyme partitioning coefficient can be lower than 0.01 in PEG8000-(NH₄)₂SO₄ ATPS with a large phase volume ratio and a moderate tie-line length, which implies the possibility of concentration operation using aqueous two phase partitioning. An ion-exchange separation of high purification efficiency was applied to analyze the clarified and dialyzed fermentation broth. A total purification factor of only 2.3 was obtained, which indicated the high enzyme protein content in the total protein of the fermentation broth. Consequently, the main purpose for separating endo-PG is concentration rather than purification. A separation scheme using an aqueous two-phase extraction process with polymer recycling and a dialysis was proposed to recover endo-PG from the fermentation supernatant of K. marxianus for commercial purpose. A high enzyme recovery up to 95% and a concentration factor of 5 to 8 with a purification factor of about 1.25 were obtained using the single aqueous two-phase extraction process. More than 95% polymer recycled will not affect the enzyme recovery and purification factor. Dialysis was used mainly to remove salts in the bottom phase. The dialysis step has no enzyme loss and can further remove small bulk proteins. The total purification factor for the scheme is about 1.7.     

Three-phase partitioning for simultaneous renaturation and partial purification of Aspergillus niger xylanase

Three-phase partitioning (TPP) is carried out by mixing ammonium sulfate and t-butanol to obtain organic phase, interfacial precipitate and aqueous phase. It is shown that TPP of an 8 M urea/100 mM dithiothreitol-denatured xylanase preparation resulted in simultaneous renaturation and purification. This integrated novel approach gave recovery of 93% enzyme activity with 21-fold purification. The implications of this in the context of recovering activity from inclusion bodies are discussed.     

Recovery of a monoclonal antibody from hybridoma culture supernatant by affinity precipitation with Eudragit S-100

An IgG₁ monoclonal antibody (MAB) was isolated from hybridoma culture supernatant by affinity precipitation with an Eudragit S-100-based heterobifunctional ligand. Affinity binding was performed in a homogeneous aqueous phase at pH 7.5 followed by precipitation of the bound affinity complex by lowering the pH to 4.8. After two washing steps, elution of specifically bound MAB was achieved by incubating the precipitate with 0.1 M glycine.HCl pH 2.5. The influence of elution volume and time on the recovery of active MAB and the overall purification factor were studied. The best conditions enabled the recovery of 50.2% of active MAB with a purification factor of 6.2. A further dialysis against 50 mM Tris.HCl pH 8.0 increased the activity yield and the purification factor to 68.4% and 8.3, respectively. This result showed that part of the antibody activity loss during affinity precipitation was due to a reversible inactivation process, being easily recovered after a refining dialysis step.     

Affinity partitioning with polymer-bound Cibacron blue F3G-A for rapid,large-scale purification of phosphofructokinase from baker's yeast

Phosphofructokinase has been isolated in homogenous form from baker's yeast. The first two steps, fractional precipitation with polyethylene glycol and affinity partitioning in aqueous biphasic systems containing Cibacron blue F3G-A-polyethylene glycol, gave a 58-fold purification within 3 h. In these steps the amount of contaminating proteases was reduced by 2 orders of magnitude. After concentration using DEAE-cellulose followed by gel chromatography, homogeneous enzyme was obtained. The advantages of affinity partitioning for large-scale preparations are discussed.     

The partitioning of cholesterol oxidase in Triton X-114-based aqueous two-phase systems.

Cholesterol oxidase from various bacterial sources (membrane-bound and extracellular) was studied in Triton X-114R solutions above the cloud point. The influence of temperature, salt, enzyme concentration and source, and pH on phase equilibrium and enzyme partitioning was investigated in this detergent-based aqueous two-phase system. The method combines remarkable recovery (over 70% and 90% in the detergent-rich phase for the extracellular and membrane-bound forms, respectively) and 10 to 20-fold concentration of the enzyme in just one purification step. The results from cholesterol oxidase are compared with other proteins, both hydrophobic and hydrophilic. The system shows considerable promise for selectively partitioning proteins based on their surface hydrophobicity.     

Production of immobilized penicillin acylase using aqueous polymer systems for enzyme purification and in situ immobilization

A novel approach for the isolation and purification of penicillin acylase (PA), which couples aqueous two-phase partitioning and enzyme immobilization has been investigated.A PA yield of 90% was achieved by treating E. coli cells with 4% butyl acetate, freeze-thawing step, and pressure homogenization. PA purification (93% recovery) was achieved by (1) removing cell debris via precipitation with polyethylene glycol (PEG 2000); (2) aqueous two-phase partitioning using a PEG 2000 + phosphate system (87% recovery).An in situ enzyme immobilization approach, using oxirane acrylic or aldehyde-agarose beads dispersed in the PEG-rich phase, was explored for the conversion of penicillin G to 6-aminopenicillanic acid. An appropriate immobilization reaction time was found. The catalytic performance of the enzyme, when immobilized, was found not to be affected by recycling of the phase-forming components.     

Three-phase partitioning of α-galactosidase from fermented media of <Emphasis Type="Italic">Aspergillus oryzae</Emphasis> and comparison with conventional purification techniques

Simple, attractive and versatile technique, three-phase partitioning (TPP) was used to purify α-galactosidase from fermented media of Aspergillus oryzae. The various conditions required for attaining efficient purification of the α-galactosidase fractions were optimized. The addition of n-butanol, t-butanol, and isopropanol in the presence of ammonium sulfate pushes the protein out of the solution to form an interfacial precipitate layer between the lower aqueous and upper organic layers. The single step of three-phase partitioning, by saturating final concentration of ammonium sulfate (60%) with 1:1 t-butanol, gave activity recovery of 92% with 12-fold purification at second phase of TPP. The final purified enzyme after TPP showed considerable purification on SDS-PAGE with a molecular weight of 64 kDa. The enzyme after TPP showed improved activity in organic solvents. Results are compared with conventional established processes for the purification of α-galactosidase produced by Aspergillus oryzae and overall the proposed TPP technique resulted in 70% reduction of purification cost compared to conventional chromatographic protocols.