A new procedure for the purification of spinach leaf photosynthetic fructose-1,6-bisphosphatase by affinity chromatography on mercaptoethylamine-Sepharose

A new purification procedure for spinach leaf fructose-1,6-bisphosphatase is proposed, which includes the use of affinity chromatography on mercaptoethylamine-Sepharose. A homogeneous preparation of the enzyme can be obtained in 48 hr, with a specific activity of 67 U/mg and a yield of 23%. The method may also be useful for the purification of other thioredoxin-activated chloroplast enzymes.     

Purification of thiogalactoside transacetylase by affinity chromatography

Thiogalactoside transacetylase, the product of the lacA gene of the lactose operon of Escherichia coli, has been purified by an improved procedure. The enzyme binds tightly to immobilized Cibacron Blue F3GA columns and can be eluted by potassium chloride in high concentrations. Final purification was obtained by affinity chromatography on an agarose-coenzyme A column followed by gel filtration.     

Purification of human DNA (cytosine-5-)-methyltransferase

We have developed a facile procedure for the purification of DNA methyltransferase activity from human placenta. The procedure avoids the isolation of nuclei and the dialysis and chromatography of large volumes. A purification of 38,000-fold from the whole cell extract has been achieved. The procedure employs ion exchange, affinity, and hydrophobic interaction chromatography coupled with preparative glycerol gradient centrifugation. A protein of 126,000 daltons was found to copurify with the activity and was the major band seen in the most highly purified material after SDS gel electrophoresis. This observation, coupled with an observed sedimentation coefficient of 6.3S, suggests that the enzyme is composed of a single polypeptide chain of this molecular weight. Hemimethylated DNA was found to be the preferred substrate for the enzyme at each stage in the purification. The ratio of the activity of the purified product on hemimethylated to that on unmethylated M13 duplex DNA was about 12 to 1. Thus, the purified activity has the properties postulated for a maintenance methyltransferase. The availability of highly purified human DNA methyltransferase should facilitate many studies on the structure, function, and expression of these activities in both normal and transformed cells.     

Affinity chromatography as a rapid and convenient method for purification of fungal laccases

A rapid and convenient method for graduation, isolation, and purification of laccase from Trametes versicolor and Fomes fomentarius culture fluids was developed. For purification affinity chromatography on syringyl- and vanillyl-controlled porosity glass (CPG) columns was applied. The purified laccase of F. fomentarius was immobilized on porous glass. Some properties of the immobilized enzyme in comparison to the free one are discussed.     

Partial purification of potato tuber invertase and its proteinaceous inhibitor

Improved purification of potato tuber invertase was achieved by utilizing a form of affinity chromatography between the enzyme and Concanavalin A (Con A) bound to Sepharose. Twenty-fold increases in specific activity were routinely obtained with this step and the enzyme was purified 190-fold over that found in the crude homogenate. The Con A-Sepharose chromatography step gave a greater purification than any other step in the invertase isolation procedure. There was up to 170% recovery of the activity loaded onto the column. α-Methyl-d-mannoside, sucrose, d-glucose and d-fructose eluted the enzyme from the Con A-Sepharose column with similar recoveries, although the volume of eluent required varied with the sugar. This unusually high recovery of invertase activity was obtained with some batches of tubers but not with others. There was evidence to suggest that the high recovery, or activation, may be due to the release of an inhibitor from the enzyme in the presence of Con A-Sepharose. Adsorption of invertase to Con A-Sepharose could be eliminated by incubation of the enzyme with α-mannosidase and β-glucosidase, indicating that potato tuber invertase is a glycoprotein. Proteinaceous inhibitor purification was improved by treatment of the tuber extract at low pH.     

Application of mixed modal resin for purification of a fibrinolytic enzyme

Recent advances in purification technologies for therapeutic molecules have stirred the research consortium. Mixed mode chromatography, having multiple interactions with the solute molecule, has drawn significant attention due to its overall advantage over traditional ion-exchange and reverse-phase chromatography. Capto adhere, a mixed mode chromatography resin with strong anion-exchange and reverse-phase interaction with solutes, was explored for purification of fibrinolytic enzyme from Bacillus sphaericus MTCC 3672. Static and dynamic resin binding study revealed that 30°C temperature, pH 8, and 0.5 mL/min flow rate were optimum for maximum binding of fibrinolytic enzyme. Maximum static dynamic binding and breakthrough capacities for Capto adhere were 249 and 196 U/mL of resin, respectively. Final purification with Sephadex G 100 gel chromatography resulted in 38-fold purity of fibrinolytic enzyme with 39% enzyme recovery. Purified enzyme was further characterized by sodium dodecyl sulfate polyacrylamide gel electrophoresis (SDS-PAGE) analysis to homogeneity, and molecular mass was found to be around 55–70 kD. Like most of the serine alkaline proteases, purified fibrinolytic enzyme was stable in a temperature range of 25–40°C and pH range of 7–9. Offshoots of our research findings have revealed a broad application area of mixed mode chromatography.     

A Monoclonal Antibody to Rabbit Brain GABA Transaminase

A monoclonal antibody of class IgG (subclass IgG1) has been prepared to rabbit brain GABA transaminase (GABA-T). This antibody reveals a single band of molecular weight 52,000 on a nitrocellulose filter blotted with purified GABA-T. On a filter blotted with unfractionated rabbit brain supernatant a major band of molecular weight 58,000 is revealed. An immunoaffinity column was prepared by coupling proteins from ascites fluid containing anti-rabbit GABA-T antibody to Bio-Rad Affi-Gel 15. This column bound purified GABA-T and extracted from unfractionated rabbit brain supernatant a protein of molecular weight 58,000, which was almost homogeneous and which had GABA-T enzyme activity. Using immunoaffinity chromatography, therefore, a high degree of purification of GABA-T may be achieved in a single step. Further, this technique may preserve an authentic form of the enzyme that is lost during the conventional purification procedure. The antibody inhibits GABA-T enzyme activity, up to a maximum of 35%.     

Purification of swine kidney alkaline phosphatase by immunoaffinity chromatography

A homogeneous alkaline phosphatase preparation was obtained from swine kidney cortex by a simple purification step of immunoaffinity chromatography. The enzyme was purified 426 times that of the initial acetone powder with a recovery of 69.6% and a specific activity of 1206 units/mg of protein. The sodium dodecyl sulfate-gel electrophoretic pattern showed a single 80,000-M_r protein band as the monomer of the purified enzyme.     

Efficient and rapid purification of recombinant human alpha-galactosidase A by affinity column chromatography

The lysosomal enzyme alpha-galactosidase A (alpha-Gal A) metabolizes neutral glycosphingolipids that possess alpha-galactoside residues at the non-reducing terminus, and inherited defects in the activity of alpha-Gal A lead to Fabry disease. We describe here an efficient and rapid purification procedure for recombinant alpha-Gal A by sequential Concanavalin A (Con A)-Sepharose and immobilized thio-alpha-galactoside (thio-Gal) agarose column chromatography. Optimal elution conditions for both columns were obtained using overexpressed human alpha-Gal A. We recommend the use of a mixture of 0.9 M methyl alpha-mannoside and 0.9 M methyl alpha-glucoside in 0.1 M acetate buffer (pH 6.0) with 0.1 M NaCl for the maximum recovery of glycoproteins with multiple high-mannose type sugar chains from Con A column chromatography, and that the Con A column should not be reused for the purification of glycoproteins that are used for structural studies. Binding of the enzyme to the thio-Gal column requires acidic condition at pH 4.8. A galactose-containing buffer (25 mM citrate-phosphate buffer, pH 5.5, with 0.1 M galactose, and 0.1 M NaCl) was used to elute alpha-Gal A. This procedure is especially useful for the purification of mutant forms of alpha-Gal A, which are not stable under conventional purification techniques. A protocol that purifies an intracellular mutant alpha-Gal A (M279I) expressed in COS-7 cells within 6h at 62% overall yield is presented.     

蛋白质层析用离子交换和疏水作用层析介质的发展概况

层析是蛋白质纯化的关键技术之一 ,作为层析技术的核心———层析介质一直以来是层析技术研究的一个热点。近年来 ,越来越多的新型层析介质被开发出来 ,如粒度均匀的交联多糖、人工合成的大孔聚合物、触角型吸附剂、软胶包裹在硬胶表面等介质。主要介绍应用较为广泛的IEC和HIC介质的组成、特性及其在蛋白质纯化中的应用 ,还研究了与HIC技术相关的两种新技术 :亲硫层析和疏水电荷诱导层析 (HCIC) ,重点介绍了HCIC的介质及其应用 ,同时也讨论了在蛋白质纯化中应用的三相纯化策略 (富集、中间纯化和精制 )。结合我国的实际情况 ,就当前蛋白质纯化的离子交换和疏水层析介质面临的挑战和未来的发展进行讨论并提出了建议     

Purification of alternanase by affinity chromatography

The enzyme alternanase, produced by Bacillus sp. NRRL B-21195, hydrolyzes alternan, a polysaccharide produced by certain strains of Leuconostoc mesenteroides that consists of glucose linked by alternating α(1→6), α(1→3) linkages. The main product of enzymatic hydrolysis by alternanase is a novel cyclic tetrasaccharide of glucose that also has alternating linkages between the glucose moieties. An improved purification scheme for alternanase has been developed that incorporates the use of isomaltosyl units linked to agarose for selectively binding the alternanase enzyme. Bound enzyme was eluted with 0.5 M sodium chloride and was nearly pure after this procedure. When followed by preparative isoelectric focusing, a single band of 117 kDa was measured when the purified protein was analyzed by HPLC size-exclusion chromatography/multiangle light scattering. The purification procedure can be scaled to permit large quantities of enzyme to be purified in high (36%) yield. Electronic Publication     

Expression and purification of hexahistidine-tagged human glutathione S-transferase P1-1 in Escherichia coli

The bacterial expression and purification of human pi class glutathione S-transferase (hGST P1-1) as a hexahistidine-tagged polypeptide was performed. The expression plasmid for hGST P1-1 was constructed by ligation of the cDNA which codes for the protein into the expression vector pET-15b. The expressed protein was purified by either glutathione or metal (Co(2+)) affinity column chromatography, which produced the pure and fully active enzyme in one step with a yield of more than 30 mg/liter culture. The activity of the purified protein was 130 units mg(-1) from the GSH affinity column and 112 units mg(-1) from the Co(2+) affinity column chromatography. The purity of the protein was assessed by electrospray ionization mass spectrometry and size-exclusion chromatography. It showed that the real molecular weight of the hexahistidine-tagged hGST P1-1 polypeptide chain agreed with the calculated value and that the purified protein eluted as an apparent homodimer on the gel filtration column. Our expression system allows the expression and purification of active hexahistidine-tagged hGST P1-1 in high yield with no need of removal of the hexahistidine tag and gives pure protein in one purification step allowing further study of this enzyme.     

Ion-exchange and affinity chromatography costs in alpha-galactosidase purification

The purification of alpha-galactosidase from soybean seeds is a five to six-step procedure consisting of cryoprecipitation, acid precipitation and ammonium sulfate fractionation followed by two or three chromatography steps. The procedures, while not optimized, were carried out in a manner that resulted in 414-515-fold purification, as reported previously. The costs of two purification sequences were compared. In the best case, the preparative-scale costs of stationary phase, reagents, and hardware were $790 per million enzyme units, excluding labor. Stationary phase costs predominated over extraction, chromatography reagent, and eluent costs when the stationary phase is replaced after 10-40 cycles of use. However, if stationary phase life exceeds 50-200 cycles, stationary phase costs become similar in magnitude to eluent and reagent costs. Labor costs, which are process-specific and difficult to estimate, exceed all other costs by a factor of 10-50 at a small scale of operation and constitute a major cost, regardless of scale. This case study provides equations and a frame-work for carrying out a first comparison of costs for multistep purification sequences. Column life, throughput, and scale of operation were found to determine not only the magnitude, but also the relative contributions, of the different components that make up purification costs. This analysis shows that there are major opportunities for reducing purification costs through the development of less expensive stationary phases and the implementation of intelligent process control and automation for process scale chromatography.     

Evaluation of modified chitosan as matrix for hydrophobic interaction chromatography

Chitosan beads were modified with glutaraldehyde and modified chitosan was investigated as matrix for hydrophobic interaction chromatography. The influence of temperature, type of salt and its ionic strength on the adsorption of -galactosidase was studied. -Galactosidase was found to bind in presence of high concentration of ammonium sulphate (3 M, w/v) and 90% of the bound enzyme was eluted with decreasing salt concentration in presence of 10% ethylene glycol. Attempt was made to purify -galactosidase from modified chitosan, -galactosidase showed 1.7-fold purification with 43.96% recovery of enzyme activity. The SDS–PAGE analysis of enzyme showed considerable purification and its molecular weight was found to be 63–64 kDa. Unlike other chromatographic matrices, the prepared chitosan beads were used five times. The results showed that purification and recovery of the enzyme did not change even when column size was increased.     

Heparin-agarose chromatography for the purification of tetrahydrofolate utilizing enzymes: C1-tetrahydrofolate synthase and 10-formyltetrahydrofolate synthetase

Rapid and convenient purification procedures based upon heparin-agarose chromatography for C1-tetrahydrofolate synthase from Saccharomyces cerevisiae and 10-formyltetrahydrofolate synthetase from Clostridium acidi-urici have been developed. The purification of the yeast enzyme involves three chromatographic steps that can be done rapidly, with no intervening dialyses, and results in high yield. The first step alone, heparin-agarose chromatography, is sufficient to purify the enzyme from yeast bearing a cloned copy of the ADE3 gene that overexpresses the protein. The other steps in the purification from wild-type yeast are matrex gel red A and phenyl-Sepharose chromatography. The purification of the clostridial enzyme involves protamine sulfate fractionation and heparin-agarose chromatography. Heparin-agarose also binds two other enzymes that use tetrahydrofolate, 5,10-methenyltetrahydrofolate cyclohydrolase and 5,10-methylenetetrahydrofolate dehydrogenase. Thus, heparin-agarose should prove useful in purification of a variety of enzymes that utilize tetrahydrofolate or its derivatives as a cofactor.     

单克隆抗体亲和层析法纯化重组溶葡萄球菌酶

溶葡萄球菌酶能够特异性杀灭金黄色葡萄球菌且不易产生耐药性, 有望成为治疗葡萄球菌属细菌引发感染的特效药物。为获得高纯度的重组溶葡萄球菌酶以达到药用标准, 本研究构建了一种以重组溶葡萄球菌酶单克隆抗体为配体的亲和层析纯化方法。纯化后的重组溶葡萄球菌酶纯度大于95%, 得率大于90%, 即使重复使用30多次, 纯化效率不变。且经比色法鉴定纯化后的重组溶葡萄球菌酶仍具有良好的活性。该方法步骤简单, 纯化效果好, 为生产高纯度重组溶葡萄球菌酶奠定了基础。     

Optimization of continuous purification of recombinant patchoulol synthase from Escherichia coli with membrane adsorbers

The natural production of patchouli oil in developing countries cannot meet the increasing demand any more. This leads to socioecological consequences, such as the use of arable land, which is actually intended for food. Hence, the world market price increased up to $150/kg. An alternative is the biotechnological production of patchouli oil using a multiproduct sesquiterpene synthase, the patchoulol synthase (PTS). Here, we report the optimization of recombinant PTS purification from Escherichia coli lysate using continuous immobilized metal affinity chromatography. First, the purification conditions of the batch process were optimized in regard to optimal buffer composition and optimized chromatographic conditions. The best purification result was achieved with Co²⁺-immobilized metal affinity chromatography (Sartobind® IDA 75) with a triethanolamine buffer at pH 7, 0.5 M NaCl, 10% [vol/vol] glycerol, 5 mM MgCl₂ and 250 mM imidazole for product elution. This optimized method was then transferred to a continuous chromatography system using three membrane adsorber units (surface of 75 cm² each). Within 1.5 hr in total, 4.55 mg PTS with a final purity of 98% and recovery of 68% could be gained. The purified enzyme was used to produce 126 mg/L (-)-patchoulol from farnesyl pyrophosphate. Here, for the first time bioactive PTS was successfully purified using membrane adsorbers in a continuous downstream process.     

药用级微生物谷氨酰胺转胺酶的纯化工艺研究

为了提高谷氨酰胺转胺酶的纯度和扩展在医药领域的应用,探索了一种适合工业化生产的、安全高效的微生物谷氨酰胺转胺酶纯化方法。轮枝链霉菌发酵后,经离心10 000 r/min 4℃除去菌体,调节发酵液电导率至4.1mS/cm和pH6.0后,以直线流速60cm/h通过SP Sepharose FF阳离子交换层析柱对目的蛋白高 选择性和高载量地捕获,再通过phenyl sepharose 6 FF（high sub）疏水层析柱进行精细纯化。纯化后经SDS-PAGE鉴定纯度达到95%以上,HPLC分析纯度> 99%。鲎试剂测定内毒素含量为0.013EU/ml,达到中国药典中血制品要求的低于0.15EU/ml标准。     

Purification of intracellular phospholipase A2 from rat spleen supernatant by reverse-phase high-performance liquid chromatography

Intracellular phospholipase A₂ was purified to homogenity from rat spleen supernatant by reverse-phase high-performance liquid chromatography with a trifluoroacetic acid-acetonitrile solvent system. The method simplified the purification procedure, which includes three consecutive chromatographic steps. The recovery of the enzyme activity was greater than 70% with an about 23,000-fold purification. The solvent system did not affect the catalytic properties of the enzyme. Phospholipases A₂ from rat spleen, human pancreatic juice, and porcine pancreas were eluted in that order from a column of octadecasilyl silica gel in a similar concentration range of acetonitrile. This result suggests that the phospholipases A₂ examined have similar hydrophobicities. This method may be applicable to the purification of phospholipases A₂ from other sources.     

Characterization of Adenylate Cyclase Purified from Rat Brain by Hydrophobic Chromatography

Abstract. Hydrophobic chromatography of detergent-solubilized rat brain adenylate cyclase on dodecyl-Sepharose produced a species that was soluble in the absence of detergent and could be manipulated like a conventional hydrophilic protein. Sevenfold purification was achieved by this technique. Further purification could then be effected by affinity chromatography on ATP-Sepharose. The purified enzyme was no longer sensitive to fluoride or guanyl nucleotides. No interaction of brain adenylate cyclase was observed with immobilized triazinyl dyes such as Cibacron Blue 3GA nor with concanavalin A-Sepharose. The molecular weight of the fluoride-activated catalytic complex in a freeze-dried membrane preparation was estimated to be 133,000 by irradiation inactivation.