Purification and in situ immobilization of lipase from of a mutant of Trichosporon laibacchii using aqueous two-phase systems

The crude intracellular lipase (cell homogenate) from Trichosporon laibacchii was subjected to partial purification by aqueous two-phase system (ATPS) and then in situ immobilization by directly adding diatomites as carrier to the top PEG-rich phase of ATPS. A partition study of lipase in the ATPS formed by polyethylene glycol–potassium phosphate has been performed. The influence of system parameters such as molecular weight of PEG, system phase composition and system pH on the partitioning behaviour of lipase was evaluated. The ATPS consisting of PEG 4000 (12%) and potassium phosphate (K₂HPO₄, 13%) resulted in partition of lipase to the PEG-rich phase with partition coefficient 7.61, activity recovery 80.4%, and purification factor of 5.84 at pH of 7.0 and 2.0% NaCl. Moreover, the in situ immobilization of lipase in PEG phase resulted in a highest immobilized lipase activity of 1114.6 U g^?1. The above results show that this novel lipase immobilization procedure which couples ATPS extract and enzyme immobilization is cost-effective as well as time-saving. It could be potentially useful technique for the purification and immobilization of lipase.     

PEG-柠檬酸盐双水相体系纯化α-淀粉酶及模型构建

探索了采用PEG-柠檬酸盐双水相体系纯化α-淀粉酶的可行性和工艺条件,实验考察了PEG分子量。结线长度、pH、上清加入量和NaCl浓度对α-淀粉酶的分配的不同影响。双水相分离体系复杂,影响因素多,为进行分析、预测和优化,采用了响应面方法,以PEG3350浓度、柠檬酸盐浓度和NaCl浓度为自变量进行了α-淀粉酶分配系数、总蛋白分配系数、纯化因子和α-淀粉酶收率的优化,确定了特定的系统组成区域,通过实验验证了该区域内纯化因子大于2,收率约90％,并且具有较低的系统粘度。     

Purification of acetohydroxy acid synthase by separation in an aqueous two-phase system

Extraction in a polyethylene glycol (PEG)–phosphate aqueous two-phase system was considered as a primary step in purification of the acetohydroxy acid synthase III large catalytic subunit from an E. coli extract. Extraction optimization was achieved by varying the system parameters. Two systems with the following weight compositions were chosen for purification: PEG-2000 (16%)–phosphate (6%) and PEG-4000 (14%)–phosphate (5.5%)–KCl (8%), both at pH 7.0 and 1 mg total protein per 1 g system. Significant purification was achieved by a single extraction step with 70% recovery of the enzyme. After an additional ion-exchange chromatography step, pure enzyme was obtained in a 50% overall yield.     

Purification of pea nodule symbiosomes using an aqueous polymer two-phase system

Symbiosomes were obtained from mature pea (Pisum sativum cv. Argona) root nodules infected with a Rhizobium leguminosarum strain (biov. viciae 3841) and purified using an aqueous polymer two-phase system (APS). The APS consists of a mixture of polymers, usually dextran T500 and poly(ethylene glycol) 3350, prepared as aqueous solutions on a weight per weight basis, where each fraction distributes according to their surface characteristics. Results of ATPase activity, cytochrome c oxidase activity, glucan synthase II activity, NAD(P)H-cytochrome c reductase activity, NO₃⁻-sensitive ATPase activity, transport of [¹⁴C]malate vs. [¹⁴C]glutamate and MAC 57 antigen analysis showed that the APS method provided intact symbiosomes with low bacteroid, plasma membrane, endoplasmic reticulum and/or mitochondria contamination. No complicated equipment is needed and the method was simple and fast, compared with other purification techniques.     

Purification of a lectin from Canavalia ensiformis using PEG-citrate aqueous two-phase system

A PEG/citrate aqueous two-phase system was tested in the partition of commercial Concanavalin A (Con A) and subsequently applied to the extraction and purification of Con A from the crude extract of Canavalia ensiformis seeds. Con A was successfully extracted to the bottom phase of a system composed of 22% (w/w) PEG8000 and 12% (w/w) citrate at pH 6.0. The obtained purification factor was 11.5 without any loss in the hemagglutinating activity. The purity of extracted lectin was confirmed by SDS-PAGE analysis.     

Purification of plasmid DNA with polymer-salt aqueous two-phase system: optimization using response surface methodology

An experimental design was used to optimize plasmid purification from an alkaline lysate of Escherichia coli cells using PEG-sodium citrate aqueous two-phase systems (ATPS), and to evaluate the influence of pH, PEG molecular weight, tie line length, phase volume ratio, and lysate load. To build the mathematical model and minimize the number of experiments for the design parameters, response surface methodology (RMS) with an orthogonal rotatable central composite design was defined based on the conditions found for the highest purification by preliminary tests. The adequacy of the calculated models for the plasmid recovery and remaining RNA were confirmed by means of variance analysis and additional experiments. Analysis of contours of constant response as a function of pH, PEG molecular weight, tie line length, and cell lysate load for three different phase volume ratios revealed different effects of these five factors on the studied parameters. Plasmid recovery of 99% was predicted for a system with PEG 400, pH 6.9, tie line length of 38.7%, phase volume ratio of 1.5, and lysate load of 10% (v/v). Under these conditions the predicted RNA removal was 68%.     

Purification and characterization of crystallins by aqueous two-phase extraction

Crystallins are a family of water-soluble proteins that constitute up to 90% of the water-soluble proteins in mammalian eye lenses. We present in this paper an alternative purification method for these proteins using polyethylene glycol/dextran aqueous two-phase extraction. Under the appropriate conditions, we were able to recover the γ-crystallin fraction essentially free of the remaining proteins. High concentrations of salt at a neutral pH maximize the recovery of γ-crystallins in the top phase and minimize the contamination by the other proteins present in the lenses. The proposed protocol decreases the separation time by about 50% The complex partition behavior observed for these proteins reflects a delicate balance between protein/phase-forming species (various polymers and salts) and protein/protein interactions. This is evidenced in part, by the role played by the largest proteins in this group as a “pseudo” phase-forming species.     

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.     

海洋真菌Caldariomyces fumago产氯过氧化物酶的双水相提纯条件

采用聚乙二醇(PEG6000)在(NH4)2SO4高饱和度下沉淀夹带蛋白质富集氯过氧化物酶,再利用磷酸盐溶液复溶解共沉淀物形成的双水相萃取体系高浓度回收酶蛋白,最后再经Sephadex G100柱层析纯化获得高纯度酶试样。结果显示:氯过氧化物酶与PEG共沉淀总活力回收率达85.5%,酶在优化的PEG/磷酸盐双水相系统中上下相分配系数k在0.341以下,酶活力回收率达到69.1%,纯度提高了21.57倍,柱层析可使酶纯度进一步提高到24.79倍,总回收率为37.75%。     

Purification of trypsin by affinity precipitation and combining with aqueous two-phase extraction

Summary Soybean trypsin inhibitor was bound to a pH-sensitive reversibly soluble-insoluble polymer (AS-L) for affinity precipitation of trypsin. Trypsin was purified from a crude extract 5.4-fold and with 61% yield, however, the reusability of the ligand was poor. This can be overcome by combining aqueous two-phase extraction with affinity precipitation, which improved trypsin yield and purity factor after repeated ligand usage.     

双水相生物催化技术的研究进展

双水相生物催化是一种高效且易于放大的生物催化技术,可以有效解决传统生物催化过程中产物浓度低、产物和副产物的抑制、以及生物催化剂难以回收等缺点。介绍了该技术的操作工艺及设备研究及其在抗生素、激素、肽类和有机化舍物酶法合成中的应用研究现状,展望了该技术的可能发展方向。     

Purification of acid-proteases by affinity partitioning in aqueous two-phase systems

Summary An affinity polymer derivative was synthesized with the group specific acid protease inhibitor pepstatin attached to dextran (M.W. 500,0001). This derivative was used in an aqueous two-phase system with hydroxypropyldextran to purify crude solutions of chymosin and Endothia parasitica (EP) acid proteases. Chymosin was purified by a factor of 6.2 with an overall yield of 83%. EP protease was similarly purified. A new pepstatin binding protease was discovered in crude EP extracts.     

Purification of fusion proteins using affinity microspheres in aqueous two-phase systems

Affinity microspheres were prepared by immobilizing human -globulin (HGb) onto carboxylated poly (styrene/acrylamide) latex particles [P(St/AAm)-H; average diameter 0.33 m], which were prepared by emulsifier-free emulsion polymerization. HGB was covalently immobilized onto the latex particles with high efficiency by the carbodiimide method. A fusion protein (ZZB1B2) of immunoglobulin G and albumin-binding domains (ZZ and B1B2, respectively) was expressed intracellularly and extracellularly in Escherichia coli and was purified by the affinity microspheres. In poly (ethylene glycol) (PEG)/potassium phosphate aqueous two-phase system, the affinity microspheres were partitioned into the PEG-rich top phase, while cells and cell debris of E. coli were displaced into the salt-rich bottom phase. Therefore, ZZB1B2 was directly purified from cell disintegrate or culture broth by combining the affinity microspheres with the aqueous two-phase partitioning, and its purity was almost the same as that purified by conventional affinity chromatography. Therefore, by this purification method, the primary purification process and the subsequent high resolution purification process are combined, and the number of purification steps can be reduced. Correspondence to: A. Kondo     

Purification of recombinant phenylalanine dehydrogenase by partitioning in aqueous two-phase systems

This study presents the partitioning and purification of recombinant Bacillus badius phenylalanine dehydrogenase (PheDH) in aqueous two-phase systems (ATPS) composed of polyethylene glycol 6000 (PEG-6000) and ammonium sulfate. A single-step operation of ATPS was developed for extraction and purification of recombinant PheDH from E. coli BL21 (DE3). The influence of system parameters including; PEG molecular weight and concentration, pH, (NH(4))(2)SO(4) concentration and NaCl salt addition on enzyme partitioning were investigated. The best optimal system for the partitioning and purification of PheDH was 8.5% (w/w) PEG-6000, 17.5% (w/w) (NH(4))(2)SO(4) and 13% (w/w) NaCl at pH 8.0. The partition coefficient, recovery, yield, purification factor and specific activity values were of 92.57, 141%, 95.85%, 474.3 and 10424.97 U/mg, respectively. Also the K(m) values for L-phenylalanine and NAD(+) in oxidative deamination were 0.020 and 0.13 mM, respectively. Our data suggested that this ATPS could be an economical and attractive technology for large-scale purification of recombinant PheDH.     

Purification and aqueous two-phase partitioning properties of recombinant Vitreoscilla hemoglobin.

Soluble recombinant Vitreoscilla hemoglobin was purified from E. coli lysate by sequential two-phase extraction techniques. Extraction of lysate containing VHb in PEG/dextran gave a 3.6-fold increase in VHb purity in the PEG-rich phase via a size exclusion mechanism. Further extraction of the recovered PEG phase in PEG/sodium sulfate gave an additional 2.0-fold increase in purity in the PEG-rich phase due to an electrostatic mechanism. Final extraction of the PEG phase in PEG/magnesium sulfate gave an additional 1.3-fold increase in VHb purity in the magnesium sulfate-rich phase. The final yield from the extractive purification was 47% with purity of VHb estimated to be greater than 95%. Yields from the sulfate salt extractions are essentially quantitative due to the extreme partitioning behavior of VHb in these systems. VHb partition coefficients as large as 46 in PEG/sodium sulfate and as small as 0.06 in PEG/magnesium sulfate were observed. Similar small partition coefficients were obtained with PEG/manganese sulfate extractions. This dramatic effect of divalent cation content on the partition coefficient of VHb in PEG/sulfate salt systems was investigated by pH and magnesium ion titration experiments. Results show the effect to be largest and nearly constant for pH values greater than 6.0 and diminished at lower pH values. A model based on magnesium ion binding to negatively charged amino acids is shown to correlate with the data well. Based on model formulation and the partitioning behavior of contaminant proteins, the observed effect is expected to be applicable to other proteins.     

Partitioning of yeast RNA in aqueous two-phase system

Summary The partition behaviour of RNA extracted from yeast was examined using three types of aqueous two-phase systems: potassium phosphate—polyethyleneglycol (PEG) system, ammonium sulphate—PEG system and dextran sulphate—PEG—NaCl system. The molecular weight of PEG showed rather remarkable effects of RNA partition than did the electrolyte. High molecular weight RNA was concentrated at the interface in these systems. This suggests the possibility of its simple concentration or extraction.     

Purification of recombinant protein A by aqueous two-phase extraction integrated with affinity precipitation

Aqueous two-phase extraction incorporated affinity precipitation was examined as a technique for protein purification. An enteric coating polymer, Eudragit S100, was employed as a ligand carrier. Eudragit was specifically partitioned to the top phase in the aqueous two-phase systems. For application of this method to purification of recombinant protein A using human IgG coupled to Eudragit in an aqueous two-phase system, 80% of protein A added was recovered with 81% purity. The purity was enhanced 26-fold by thid method. The IgG-Eudragit could be used repeatedly for the purification process. This seperation method should be applicable to industrial-scale purification as a new purification procedure combining the advantages and compensating for the disadvantages of the aqueous two-phase method and affinity precipitation method. (c) 1992 John Wiley & Sons, Inc.     

Purification of plasma membranes by aqueous two-phase affinity partitioning.

A rapid method for purifying rat liver plasma membranes of high purity and yield is described. Squashed liver was homogenized in an aqueous polyethylene glycol-dextran two-phase system. After phase separation and reextraction of the bottom phase with fresh top phase, the combined polyethylene glycol-rich top phases were affinity partitioned in the presence of borate buffer with new bottom phase containing dextran-linked wheat-germ agglutinin. Under these conditions the lectin selectively pulled plasma membranes into the dextran-rich bottom phase, while other membranes preferentially distributed in the top phase. The lectin-containing bottom phase was reextracted with fresh top phase before collecting the purified plasma membranes by centrifugation. This protocol resulted in a preparation that was 30- to 40-fold enriched compared to the homogenate in plasma membrane markers for both the apical and basolateral domains and had yields of 55-70%. The contamination by other membranes was low. The entire procedure was completed within 90 min. The method should be useful for purifying plasma membranes also from other sources.     

Purification of recombinant cutinase by extraction in an aqueous two-phase system facilitated by a fatty acid substrate

Purification of recombinant wild-type cutinase from the culture supernatant of Saccharomyces cerevisiae by extraction in aqueous two-phase system was investigated. The partition of the enzyme in a polyethylene glycol (PEG)-potassium phosphate system to the top phase was increased with lower molecular weight PEG. Enzyme partition in a 20% PEG/15% phosphate two-phase system was studied in the presence of detergents, fatty acids, and alcohols, respectively. Addition of 0.5% (w/w) butyrate increased the partition coefficient from 17 to 135 and the purification factor from 10 to 23. The effect of butyrate was also confirmed by using the countercurrent mode of extraction. Recovery of cutinase from the top phase was achieved by a secondary extraction into a new salt phase at a lower pH or a lower temperature. A specific interaction of butyrate to the active site of the enzyme was demonstrated by fluorescence spectroscopy. Size exclusion chromatography showed the cutinase-butyrate complex to be over two times the size of the free enzyme.