Aqueous-aqueous two-phase systems composed of low molecular weight of polyethylene glycols and dextrans for counter-current chromatographic purification of proteins

New aqueous-aqueous two-phase systems composed of relatively low molecular weight polymers such as polyethylene glycol (PEG) (Mr: 1000-4000) and dextran (Mr: 10,000 and 40,000) were evaluated for purification of proteins by counter-current chromatography (CCC). The compositions of aqueous two-phase systems were optimized by measuring parameters such as viscosity and volume ratio between the two phases. CCC purification of a glucosyltransferase (GTF) from Streptococcus mutans (SM) cell-lysate was successfully demonstrated with a 7.5% PEG 3350-10% dextran T40 system containing 10mM potassium phosphate buffer at pH 9.0. After CCC purification, both PEG and dextran contained in the CCC fractions were easily removed by ultrafiltration in a short period of time. The fractionated column contents containing GTF were analyzed by enzymatic activity as well as sodium dodecyl sulfate (SDS) polyacrylamide gel electrophoresis. The recovery of the enzyme from CCC fraction was over 95% as estimated by enzymatic activities.     

Purification of lactic acid dehydrogenase from crude bovine heart extract by pH-peak focusing counter-current chromatography

pH-peak focusing counter-current chromatography (CCC) was applied to the purification of lactic acid dehydrogenase (LDH) from a crude bovine heart extract using a cross-axis coil planet centrifuge (CPC). The experiment was performed with two sets of polymer phase systems composed of 16% (w/w) polyethylene glycol (PEG) 1000-12.5% (w/w) potassium phosphate buffer and 15% (w/w) PEG 1540-15% (w/w) ammonium sulfate each at various pH values. The best result was achieved from the PEG 1540-ammonium sulfate polymer phase system by adding a retainer (10 mM acetic acid) to the upper stationary phase and an eluter (100 mM sodium hydroxide) to the lower mobile phase. At a flow-rate of 0.5 ml/min, LDH was eluted as a sharp peak which was well resolved from other proteins. Collected fractions were analyzed by the LDH enzymatic activity and by sodium dodecyl sulfate-polyacrylamide slab gel electrophoresis to detect contaminated proteins. LDH was purified directly from crude bovine heart extract in a concentrated state.     

离子交换层析结合反向色谱纯化聚二氨基丙酸

ε-聚赖氨酸生产菌株Streptomyces albulus PD-1可合成一种新型非蛋白质氨基酸均聚物聚二氨基丙酸,采用离子交换层析和反向色谱,对聚二氨基丙酸的分离纯化进行研究。离子交换层析柱选用DEAE-Sepharose Fast Flow填料,50 mmol/L磷酸盐缓冲液(p H 7.5)平衡上样,含0.5 mol/L Na Cl的磷酸盐缓冲液(p H 7.5)洗脱,收集洗脱液用分子筛Sephadex G-25除去磷酸盐缓冲液。然后用C18反相色谱进一步纯化,流动相为V(甲醇)/V(0.1%磷酸)=5/95。经过离子交换层析和反向色谱,纯化得到聚二氨基丙酸纯品,回收率为39.8%,样品纯度达98.4%,为后续的聚二氨基丙酸的深入研究奠定基础。     

Purification of turnip peroxidase and its kinetic properties

Peroxidase from turnip roots was purified using metal affinity chromatography up to a specific activity of 337 units/mg protein with 3.02 RZ and 63.5% recovery. After purification, the enzyme showed 2-3 bands on sodium dodecyl sulphate polyacrylamide gel electrophoresis (SDS-PAGE). The molecular weight of the purified enzyme was found to be 37-39 kD with matrix assisted laser desorption ionization mass spectrometer (MALDI-MS). The enzyme showed maximum activity in phosphate buffer, pH 6.0, and lowest activity in borate buffer at the same pH. The Km of the enzyme was found to be 7.07 x 104 mM. Turnip peroxidase also contains an iron moiety which is found to be about 0.28%. The enzyme showed 50% inhibition of its specific activity with ethylene diamine tetraacetic acid (EDTA).     

Purification of adenovirus messenger ribonucleic acid by an aqueous polymer two-phase system.

An aqueous polymer phase system containing 6.3% (w/w) dextran and 3.5% (w/w) poly(ethylene glycol) in 10 mM phosphate buffer (pH 8.0) was developed to select RNA-DNA hybrids from unhybridized RNA. The top phase of this phase system, which contains DNA and the RNA-DNA hybrids, can be used to purify adenovirus messenger RNA both early and late in the infectious cycle. The hybrids can be melted by heat in the top phase and the messenger RNA selected by oligo(dT)cellulose chromatography whereupon the polymers and the DNA percolate and the polyadenylated messenger RNA absorb to the column. The isolated messenger RNA appears to be almost quantitatively recovered at a purity from 70 to 90% depending on the concentration of the specific messenger RNA in the starting material. Early and late viral messenger RNA were selected on the complementary strands of adenovirus DNA according to this procedure.     

Application of a PEG/salt aqueous two-phase partition system for the recovery of monoclonal antibodies from unclarified transgenic tobacco extract

Aqueous two-phase partition systems (ATPS) have been widely used for the separation of a large variety of biomolecules. In the present report, the application of a polyethylene glycol/phosphate (PEG/phosphate) ATPS for the separation of anti-HIV monoclonal antibodies 2G12 (mAb 2G12) and 4E10 (mAb 4E10) from unclarified transgenic tobacco crude extract was investigated. Optimal conditions that favor opposite phase partitioning of plant debris/mAb as well as high recovery and purification were found to be 13.1% w/w (PEG 1500), 12.5% w/w (phosphate) at pH 5 with a phase ratio of 1.3 and 8.25% w/w unclarified tobacco extract load. Under these conditions, mAb 2G12 and mAb 4E10 were partitioned at the bottom phosphate phase with 85 and 84% yield and 2.4- and 2.1-fold purification, respectively. The proposed ATPS was successfully integrated in an affinity-based purification protocol, using Protein A, yielding antibodies of high purity and yield. In this study, ATPS was shown to be suitable for initial protein recovery and partial purification of mAb from unclarified transgenic tobacco crude extract.     

Purification and Characterization of Polyphenol Oxidase From Waste Potato Peel by Aqueous Two-Phase Extraction

Potato peel from food industrial waste is a good source of polyphenol oxidase (PPO). This work illustrates the application of an aqueous two-phase system (ATPS) for the extraction and purification of PPO from potato peel. ATPS was composed of polyethylene glycol (PEG) and potassium phosphate buffer. Effect of different process parameters, namely, PEG, potassium phosphate buffer, NaCl concentration, and pH of the system, on partition coefficient, purification factor, and yield of PPO enzyme were evaluated. Response surface methodology (RSM) was utilized as a statistical tool for the optimization of ATPS. Optimized experimental conditions were found to be PEG1500 17.62% (w/w), potassium phosphate buffer 15.11% (w/w), and NaCl 2.08 mM at pH 7. At optimized condition, maximum partition coefficient, purification factor, and yield were found to be 3.7, 4.5, and 77.8%, respectively. After partial purification of PPO from ATPS, further purification was done by gel chromatography where its purity was increased up to 12.6-fold. The purified PPO enzyme was characterized by sodium dodecyl sulfate polyacrylamide gel electrophoresis (SDS-PAGE), followed by K_m value 3.3 mM, and V_max value 3333 U/mL, and enzyme stable ranges for temperature and pH of PPO were determined. These results revealed that ATPS would be an attractive option for obtaining purified PPO from waste potato peel.     

Purification of penicillin G acylase using immobilized metal affinity membranes

The immobilized metal affinity membrane (IMAM) with modified regeneration cellulose was employed for purification of penicillin G acylase (PGA). For studying PGA adsorption capacity on the IMAM, factors such as chelator surface density, chelating metal, loading temperature, pH, NaCl concentration and elution solutions were investigated. The optimal loading conditions were found at 4 degrees C, 0.5 M NaCl, 32.04 micromol Cu(2+) per disk with 10 mM sodium phosphate buffer, pH 8.5, whereas elution conditions were: 1 M NH(4)Cl with 10 mM sodium phosphate buffer, pH 6.8. By applying these chromatographic conditions to the flow experiments in a cartridge, a 9.11-fold purification in specific activity with 90.25% recovery for PGA purification was obtained. Meanwhile, more than eight-times reusability of the membrane was achieved with the EDTA regeneration solutions.     

Novel method for purification of staphylococcal enterotoxin A.

A novel single-step procedure for the purification of staphylococcal enterotoxin A (SEA), namely, dye ligand affinity chromatography with the triazine dye Red A, was developed. SEA purified by this method produced a single band when subjected to sodium dodecyl sulfate-polyacrylamide gel electrophoresis. The yield from 5 liters of culture supernatant was 0.113 g, corresponding to an overall yield of 55%. In some instances, purification of SEA from culture supernatants by dye ligand affinity chromatography produced two enterotoxin peaks that could be eluted from the column with 300 and 500 mM phosphate buffer (pH 6.8). Enterotoxin from these peaks produced a single band when subjected to sodium dodecyl sulfate-polyacrylamide gel electrophoresis, but multiple bands were observed on isoelectric focusing gels. This method of purification represents a significant improvement in time, yields, and purity of enterotoxin over previously published purification methods.     

Novel method for purification of staphylococcal enterotoxin A

A novel single-step procedure for the purification of staphylococcal enterotoxin A (SEA), namely, dye ligand affinity chromatography with the triazine dye Red A, was developed. SEA purified by this method produced a single band when subjected to sodium dodecyl sulfate-polyacrylamide gel electrophoresis. The yield from 5 liters of culture supernatant was 0.113 g, corresponding to an overall yield of 55%. In some instances, purification of SEA from culture supernatants by dye ligand affinity chromatography produced two enterotoxin peaks that could be eluted from the column with 300 and 500 mM phosphate buffer (pH 6.8). Enterotoxin from these peaks produced a single band when subjected to sodium dodecyl sulfate-polyacrylamide gel electrophoresis, but multiple bands were observed on isoelectric focusing gels. This method of purification represents a significant improvement in time, yields, and purity of enterotoxin over previously published purification methods.     

Separation and quantification of muropeptides with high-performance liquid chromatography

About 80 different muropeptides, the subunits which comprise the polymer murein of Escherichia coli, were resolved by high-performance liquid chromatography. The muropeptides were released from isolated murein by complete digestion with muramidase from Chalaropsis spec. The separation method is based on reversed phase chromatography of the sodium borohydride-reduced compounds using ODS (C18) columns and a linear gradient elution with sodium phosphate buffer and methanol as organic modifier. The effect of temperature, pH, ionic strength, and the steepness of the gradient and of different support materials on the separation of the muropeptides was investigated. The new method represents a major improvement over previous methods with respect to resolution, sensitivity, and speed. Analytical as well as preparative separations can be realized. Quantitative analysis of murein composition is achieved by a linear gradient from 50 mM sodium phosphate, pH 4.31, to 75 mM sodium phosphate, pH 4.95, containing 15% methanol for 135 min on a 250 X 4.6 mm 3-micron Hypersil ODS column at 55 degrees C using a flow rate of 0.5 ml/min. With uv detection at 205 nm about 20 micrograms of murein per analysis is sufficient. The detection limit per compound is about 5 ng. A method for the evaluation of the analytical data allowing a convenient comparison of different muropeptide pattern is described.     

HPLC analysis of the second-generation antidepressant sertraline and its main metabolite N-desmethylsertraline in human plasma

A liquid chromatographic method with ultraviolet detection was developed for the analysis of the recent antidepressant sertraline and its main metabolite N-desmethylsertraline in human plasma. The analytes were separated on a C8 reversed phase column, using a mobile phase composed of acetonitrile and a 12.3 mM, pH 3.0 phosphate buffer containing 0.1% triethylamine (35:65, v/v). Clomipramine was used as the Internal Standard. Using a solid phase extraction procedure with C2 cartridges high extraction yields (>94%) and good purification from matrix interference were obtained. Good linearity was obtained in the 7.5-250.0 ng mL(-1) range for sertraline and in the 10-500 ng mL(-1) range for N-desmethylsertraline. The analytical method was validated in terms of precision, extraction yield and accuracy. These assays gave R.S.D.% values for precision always lower than 3.9% and mean accuracy higher than 90%. Thanks to its good selectivity, the method proved to be suitable for the analysis of plasma samples from patients treated with sertraline as either monotherapy or polypharmacy.     

Developing procedures for the large-scale purification of human serum butyrylcholinesterase

Human serum butyrylcholinesterase (Hu BChE) is the most viable candidate for the prophylactic treatment of organophosphate poisoning. A dose of 200 mg/70 kg is predicted to protect humans against 2× LD₅₀ of soman. Therefore, the aim of this study was to develop procedures for the purification of gram quantities of this enzyme from outdated human plasma or Cohn Fraction IV-4. The purification of Hu BChE was accomplished by batch adsorption on procainamide-Sepharose-CL-4B affinity gel followed by ion-exchange chromatography on a DEAE-Sepharose column. For the purification of enzyme from Cohn Fraction IV-4, it was resuspended in 25 mM sodium phosphate buffer, pH 8.0, and fat was removed by decantation, prior to batch adsorption on procainamide-Sepharose gel. In both cases, the procainamide gel was thoroughly washed with 25 mM sodium phosphate buffer, pH 8.0, containing 0.05 M NaCl, and the enzyme was eluted with the same buffer containing 0.1 M procainamide. The enzyme was dialyzed and the pH was adjusted to 4.0 before loading on the DEAE column equilibrated in sodium acetate buffer, pH 4.0. The column was thoroughly washed with 25 mM sodium phosphate buffer, pH 8.0 containing 0.05 M NaCl before elution with a gradient of 0.05–0.2 M NaCl in the same buffer. The purity of the enzyme following these steps ranged from 20% to 40%. The purity of the enzyme increased to >90% by chromatography on an analytical procainamide affinity column. Results show that Cohn Fraction IV-4 is a much better source than plasma for the large-scale isolation of purified Hu BChE.     

Optimized production and quantification of the tryptophan-deficient sweet-tasting protein brazzein in Kluyveromyces lactis

Abstract

The sweet-tasting protein brazzein is a candidate sugar substitute owing to its sweet, sugar-like taste and good stability. To commercialize brazzein as a sweetener, optimization of fermentation and purification procedure is necessary. Here, we report the expression conditions of brazzein in the yeast Kluyveromices lactis and purification method for maximum yield. Transformed K. lactis was cultured in YPGlu (pH 7.0) at 25?°C and induced by adding glucose:galactose at a weight ratio of 1:2 (%/%) during the stationary phase, which increased brazzein expression 2.5 fold compared to the previous conditions. Cultures were subjected to heat treatment at 80?°C for 1?h, and brazzein containing supernatant was purified using carboxymethyl-sepharose cation exchange chromatography using 50?mM NaCl in 50?mM sodium acetate buffer (pH 4.0) as a wash buffer and 400?mM NaCl (pH 7.0) for elution. The yield of purified brazzein under these conditions was 2.0-fold higher than that from previous purification methods. We also determined that the NanoOrange assay was a suitable method for quantifying tryptophan-deficient brazzein. Thus, it is possible to obtain pure recombinant brazzein with high yield in K. lactis using our optimized expression, purification, and quantification protocols, which has potential applications in the food industry.     

Micellar electrokinetic capillary chromatography determination of +S and -R arotinolol in serum using UV detection and solid phase extraction.

A method for the simultaneous determination of +S and -R arotinolol in serum by micellar electrokinetic capillary chromatography is described. Stereoselective resolution of the arotinolol enantiomers was achieved using 5 mM sodium taurocholate in 10 mM sodium dihydrogen phosphate buffer of pH 2.5. A 72-cm uncoated fused-silica capillary at a constant voltage of 15 kV was used for the analysis. The analytes of interest were extracted from serum using solid phase extraction. An octadecyl cartridge gave good recoveries in excess of 87% for both +S and -R arotinolol without any interference. The calibration curves were linear over the range of 50-500 ng ml(-1) with +S propranolol as the internal standard and the coefficient of determination was greater than 0.999 (n = 3). The limit of quantitation was 50 ng ml(-1) for each enantiomer and the detection limit using 1 ml serum and a UV detection set et 220 nm was 25 ng ml(-1) (S/N = 2). Precision and accuracy of the method were in the range 0.8-2.7% and 1.2-6.4%, respectively, for +S arotinolol and 1.1-3.9% and 2.2-6.5%, respectively, for -R arotinolol.     

Double Triton X-114 Phase Partitioning for the Purification of Plant Cytochromes P450 and Removal of Green Pigments

A double Triton X-114 phase partitioning procedure that separates plant cytochromes P450 from green pigments and provides an extract highly enriched in total cytochromes P450 has been developed. Upon phase partitioning in Triton X-114, plant cytochromes P450 have previously been found to partition to the pigmented detergent rich phase. These partitionings were carried out using phosphate buffer. We found that the partitioning of the cytochromes P450 could be shifted to a pigment-free Triton X-114 poor phase by changing the buffer component to borate. The protein extract containing the cytochromes P450 but devoid of green pigment was subjected to a second phase partitioning step before which the buffer was changed from borate to phosphate. This second phase partitioning step produced a Triton X-114-rich phase highly enriched in cytochromes P450 proteins compared to the microsomal starting material as monitored by sodium dodecyl sulfate–polyacrylamide gel electrophoresis, cytochrome P450 reconstitution assays, and Western blotting. The yield of the double phase partitioning purification procedure is about 26% which is high compared to the yields obtained at similar stages of purification using column chromatography. The double phase partitioning procedure takes 3–4 h to complete. This is very fast compared to traditional purification schemes for cytochromes P450 which involve multiple of column chromatographic steps. Plant cytochromes P450 are labile, low abundant proteins that are difficult to isolate. The double Triton X-114 phase partitioning here reported thus constitutes a versatile, efficient purification procedure circumventing many of the problems previously encountered.     

Purification of alcohol dehydrogenase from bovine liver crude extract by dye-ligand affinity counter-current chromatography

Alcohol dehydrogenase (ADH) was extracted from a crude bovine liver homogenate by dye-ligand affinity counter-current chromatography (CCC) using a cross-axis coil planet centrifuge (x-axis CPC). The purification was performed using two types of polymer phase systems composed of 4.4% polyethylene glycol (PEG) 8000-7.0% dextran T500-0.1 M potassium phosphate buffers and 16% PEG 1000-12.5% potassium phosphate buffers, both containing a procion red dye as an affinity ligand at various pH values. The best purification was achieved using the PEG 1000-potassium phosphate system at pH 7.3 containing 0.05% procion red as a ligand. The upper PEG-rich phase containing procion red was used as the stationary phase and a crude bovine liver homogenate was eluted with the potassium phosphate-rich lower phase at 0.5 ml/min. After elution of bovine liver proteins in the homogenate, ADH still retained in the stationary phase was collected from the column by eluting with the PEG 1000-rich upper phase. Collected fractions were analyzed by ADH enzymatic activity and by sodium dodecyl sulfate (SDS)-polyacrylamide gel electrophoresis (PAGE) to detect contaminant proteins in the ADH fractions. The ADH was purified directly from crude bovine liver extract within 6h with minimum loss of its enzymatic activity.     

Affinity extraction of dye- and metal ion-binding proteins in polyvinylpyrrolidone-based aqueous two-phase system

Affinity extraction of dye- and metal ion-binding proteins, respectively, in a polyvinylpyrrolidone (PVP40)-Reppal PES 100 two-phase system was investigated. Due to the ability of PVP to complex azo dyes and inorganic ions, covalent coupling of the ligands was not essential. Cibacron Blue F3GA was used as the ligand for extraction of lactate dehydrogenase (LDH) from porcine muscle, while copper ions were used for extraction of B. stearothermophilus LDH with a fusion tag of six histidine residues (His6-LDH) from recombinant Escherichia coli homogenate. The binding strength of the enzymes to their respective ligands was only slightly reduced in the presence of PVP. The partition coefficient of Cibacron Blue and Cu2+ ions in the two-phase systems composed of different concentrations of PVP and Reppal was in the range of 20-30, with maximal partitioning being observed in the 17% (w/w) PVP40-10% Reppal PES100 system. Only a minor leakage of the ligands to the bottom phase was observed with time. The partitioning of porcine LDH to the PVP phase was increased 100-fold, and a maximal recovery of 89% was obtained in the two-phase system loaded with 0.2% (w/w) Cibacron Blue. The enzyme was quantitatively recovered with further purification from the PVP-dye phase using a secondary extraction step with 170 mM phosphate or alternatively with 100 mM phosphate containing NADH or NaCl. A more than 10-fold increase in the partition coefficient of His6-LDH was achieved in the two-phase system loaded with 0.4% (w/w) copper sulfate compared to the system lacking the metal ions. The enzyme was also back-extracted into phosphate phase in the presence of imidazole.     

A simple procedure for obtaining large quantities of tubulin subunits from newborn mouse brain

A simple, efficient two-step procedure of DEAE--Sephadex A--50 column chromatography followed by hydroxyapatite column chromatography for purification of alpha- and beta-tubulin subunits from newborn mouse brain is described. Stored frozen mouse brains can be used as a convenient starting material. Differential elution of alpha and beta subunits from hydroxyapatite was achieved using a linear gradient of 0.2--0.3 M phosphate buffer containing 2 M urea, 0.1% sodium dodecyl sulphate and 1 mM dithiothreitol. 20 mg of alpha-tubulin (purity: greater than 85%) and 16 mg of beta-tubulin (purity greater than 95%) completely separated from each other can be obtained in one experiment.     

Purification and properties of mitochondrial malate dehydrogenase from unfertilized eggs of the sea urchin, Anthocidaris crassispina

Purification and characterization of mitochondrial malate dehydrogenase [EC 1.1.1.37] from unfertilized eggs of the sea urchin, Anthocidaris crassispina, are described. The purification method consisted of dextran sulfate fractionation, Blue Dextran Sepharose chromatography, Phenyl-Sepharose hydrophobic chromatography and DEAE-cellulose chromatography. The enzyme was purified 771-fold with a 7% yield from the crude extract. The purified enzyme appeared homogeneous on polyacrylamide gel electrophoresis under both native and denatured conditions. After incubation at 45 degrees C for 50 min, the enzyme lost about 90% of its activity. In the presence of NADH, however, the enzyme was protected against the heat denaturation. The native enzyme had a molecular weight of about 65,000 and probably consisted of two identical subunits. In the reduction of oxaloacetate with NADH, a broad optimum pH ranging from 8.2 to 9.4 was found with 50 mM Tris-HCl and glycine-NaOH buffers. Sodium phosphate buffer apparently activated the enzyme. The apparent Km values for oxaloacetate and NADH were 19 microM and 30 microM, respectively. The optimum pH for malate oxidation with NAD+ was 10.2 in 50 mM NaHCO3-Na2CO3 buffer. The apparent Km values for malate and NAD+ were 7.0 mM and 0.6 mM, respectively. Zinc ion, sulfite ion, p-chloromercuriphenylsulfonate and adenine nucleotides strongly inhibited the enzyme.