双水相体系逆流色谱技术在蛋白质分离中的应用

双水相体系逆流色谱技术结合了逆流色谱的高效率、高制备量以及双水相体系适于蛋白质分离的特点,因此在蛋白质的分离方面具有独特的应用价值。本文综述了近年来基于正交轴逆流色谱仪器的双水相体系逆流色谱技术在多种蛋白质分离中的应用。并对一些新兴的蛋白质逆流色谱分离技术及新型逆流色谱柱分离系统进行了介绍。     

双水相技术在抗生素分离中的应用

简单阐明了双水相技术在抗生素的分离中应用的发展状况,分析了影响双水相系统分离抗生素的各种因素,提出了导致双水相中抗生素非对称分配的主要作用力为疏水作用力,并对双水相技术在抗生素分离中应用的发展方向作了探讨。     

双水相萃取技术新进展

本文简要介绍了双水相萃取技术在生物活性物质的纯化及分析上的应用,并且从四个方面总结了双水相萃取技术的新进展和发展方向。     

微生物胞内产物分离的新方法—双水相萃取技术

本文简要地介绍了双水相萃取技术的概念,综述了双水相取技术的特点及其在内产物分离中的应用,讨论了影响细胞碎片的去除和双水相萃取效果的参数,以及成相材料的回收利用等问题,展示了双水相萃取技术的新发展。     

利用双水相萃取技术分离纯化尿激酶

通过研究双水相萃取系统的各种影响因素：乙醇／（NH4）2SO4的组成比例、pH值、无机盐的加入、粗酶的浓度等,探索以乙醇／（NH4）2SO4组成的双水相萃取体系纯化尿激酶的最佳条件。建立以乙醇／（NH4）2SO4组成的双水相萃取体系分离纯化尿激酶的新途径。结果表明：双水相萃取系统冰乙醇浓度为65％,（NH4）2SO4浓度为10．0％,pH8．0,酶加入量为30％,且不加入任何其他无机盐的条件下,尿激酶的纯化倍数可达到9．2倍,回收率最高达92％。     

双水相技术在抗生素分离中的应用

简单阐明了双水相技术在抗生素的分离中应用的发展状况,分析了影响双水相系统分离抗生素的各种因素,提出了导致双水相中抗生素非对称分配的主要作用力为疏不作用力,并对双水相技术在抗生素分离中应用的发展方向作了探讨。     

现代分离技术在抗生素提取中的应用*

详细介绍了膜分离技术在抗生素分离提取中的应用进展,并简单阐明了高效毛细管电泳技术、双水相技术和反胶束萃取技术在抗生素提取中的应用情况。对这些现代分离技术的发展前景作了简要探讨。     

木聚糖酶分离纯化技术

木聚糖酶应用广泛,其分离纯化是进行酶学性质研究、分子研究的前提条件,是成功确定氨基酸序列和三维结构的基础。综述微生物木聚糖酶分离纯化的方法,分析了常用方法在其分离纯化中的优缺点;强调了特异性分离纯化技术是高效的分离纯化方法;并对其它方法进行了概括。     

天然植物多糖分离纯化技术研究现状和进展

植物多糖因具有抗肿瘤、增强免疫、抗氧化等功效而备受关注,多糖的分离纯化是多糖结构和生物活性研究的首要前提。本文系统介绍了传统的水提醇沉法以及酶提取法、超声波辅助提取法、超临界流体萃取法、超高压提取技术微波辅助提取法和双水相萃取等新技术,对其分离原理、处理方式和效果进行分析比较和综述;从物理分离方式、分子间作用力及化学性质分离的角度,综述植物粗多糖分离和纯化方法及途径,为天然植物中多糖的分离纯化和综合利用提供参考。     

Geotrichum sp．SYBC WU-3脂肪酶的双水相萃取和酶学性质

初步研究双水相体系对Geotrichum sp．SYBC WU-3脂肪酶的萃取分离效果,选用PEC4000／NaH2 PO4作为戍相系统进行系统研究,考察影响脂肪酶萃取的各种因素（如PEG相对分子质量及质量分数、NaH2PO4质量浓度、pH）,并采用正交实验进一步优化实验条件,确定双水相萃取体系为PEG质量分数为30％、NaH2PO4质量分数为20％、体系pH为6,在此条件下Geotrichum sp．SYBC WU-3脂肪酶经硫酸铵沉淀和双水相萃取两步纯化的纯化倍数达到最大,较Geotrichum sp．SYBC WU-3脂肪酶粗酶纯化了22倍。Geotrichum sp．SYBC WU-3脂肪酶纯酶为低温碱性脂肪酶,最适反应温度为15oC,最适pH为9．5,相对分子质量为3．58×10^4。     

Studies on the isolation of penicillin acylase from Escherichia coli by aqueous two-phase partitioning

A method of enzyme release and aqueous two-phase extraction is described for the separation of penicillin acylase from Escherichia coli cells. Butyl acetate, 12% (v/v), treatment combined with freeze-thawing gives up to 70% enzyme release. For polyethylene glycol (PEG) + phosphate two-phase extraction systems the enzyme purity and yield were rather low. Modified PEG, including PEG-ampicillin, PEG-aniline, PEG-phosphate, and PEG-trimethylamine, were synthesized and used in aqueous two-phase systems; PEG-trimethylamine is the most satisfactory. A system containing 12% (w/w) PEG4000, 8% (w/w) of which is PEG-trimethylamine, with 0.7M potasium phosphate at pH 7.2, resulted in the enzyme selective partition being greatly enhanced by charge directed effects. Possible mechanisms for the separation process are discussed. (c) 1992 John Wiley & Sons, Inc.     

Magnetic aqueous two-phase separation: a new technique to increase rate of phase-separation, using dextran-ferrofluid or larger iron oxide particles

A new technique to speed up the phase separation of aqueous two-phase systems is described. The technique is based on the addition of magnetically susceptible additives (ferrofluids or iron oxide particles). In a magnetic field such additives will induce a faster phase separation. In one approach, dextran-stabilized ferrofluid was added to an aqueous two-phase system containing polyethylene glycol and dextran. The ferrofluid was totally partitioned to the dextran phase. After mixing of the two-phase system, it was possible to reduce the separation time by a factor of 35 by applying a magnetic field to the system. Another approach involved the use of 1-micron iron oxide particles instead of ferrofluid. In this case also, the phase-separation time was reduced, by a factor of about 70, when the system was placed in a magnetic field. The addition of ferrofluid and/or iron oxide particles was shown to have no influence on enzyme partitioning or on enzyme activity. The partitioning of chloroplasts, on the other hand, was influenced unless the ferrofluid used had been treated with epoxysilane. A column system comprising 15 magnetic separation stages was constructed and was used for semicontinuous separation of enzyme mixtures.     

Technical aspects of separation using aqueous two-phase systems in enzyme isolation processes.

Technical aspects of the separation of aqueous two-phase systems in a commercial separator were studied in detail. For the Gyrotester B, the smallest available separator, a flow rate of 200 ml/min and a length of the regulating screw in the outlet port of 13.5 mm were found as optimal operation parameters for the separation of a poly(ethylene glycol) (PEG)/dextran two-phase system. In the presence of cells and cell debris the characteristics of the carrier two-phase systems are changed, most notably the phase ratio. Nevertheless good separation and high throughput can be maintained up to 30% wet cell material in the complete system. Using this method the enzyme pullulanase was extracted from 6.65 kg Klebsiella pneumoniae in 88% yield in a single step in less than 2 hr. A yield of 90% was predicted for this step based upon laboratory data, indicating that the performance of the extraction and separation can be calculated with the necessary accuracy and the further scale-up of the process should be accomplished quite easily. The hydrophilic polymers Constituting the phase system will often stabilize the enzymes, So that the separation can be carried out at room temperature without extensive cooling. The method of enzyme solubilization or cell disruption is not decisive for the successful extraction of the enzymes, the only limitation being the necessity to find a suitable two-phase system where the desired product and the cells or cell debris will partition in opposite phases. This is shown for α-glucosidase from Saccharomyces carlsbergensis and three aminoacyl-tRNA-synthetases from Escherichia coli. The results obtained demonstrate that aqueous two-phase systems can be separated in commercially available separators with high capacity and efficiency. It can be expected that the advanced separation technology available from chemical engineering studies can also be used for the development of large-scale isolation processes for enzymes involving liquid–liquid partitions.     

现代分离技术在抗生素提取中的应用

详细介绍了膜分离技术在抗生素分离提取中的应用进展,并简单阐明了高效毛细管电泳技术、双水相技术和反胶束萃取技术在抗生素提取中的应用情况。对这些现代分离技术的发展前景作了简要探讨。     

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.     

纳豆激酶集成化分离技术

综述了纳豆激酶的分离纯化技术的研究现状和发展趋势。通过对常规分离技术的分析,重点讨论了集成化分离技术的应用及其优势,包括集成化双水相分配技术、扩张床吸附技术以及耐盐性混合模式吸附技术等分离方法。并指出集成化分离技术在生产纳豆激酶以及其他活性蛋白方面,具有广阔的应用前景。     

Bioconversion with whole cell penicillin acylase in aqueous two-phase systems

The deacylation of Pen G was carried out by using recombinant E. coli in an aqueous two-phase system consisting of polyethylene glycol and potassium phosphate solution, which partitions the cells to the bottom phase and the products to the top phase. Bioconversion and product separation were carried out in the same reactor. Repeated batch conversion was employed ten times and enzymic activity showed only a slight decline. When pure enzyme was used for bioconversion in an aqueous two-phase system, the decline was fast and bioconversion using whole cell penicillin acylase was better than that obtained using the pure acylase.     

Ucon-benzoyl dextran aqueous two-phase systems: protein purification with phase component recycling

Benzoyl dextran with a degree of substitution of 0.18 was synthesized by reacting dextran T500 with benzoyl chloride. A new type of aqueous two-phase system composed of benzoyl dextran as bottom phase polymer and the random copolymer of ethylene oxide and propylene oxide (Ucon 50-HB-5100) as top phase polymer has been formed. The phase diagram for the system Ucon 50-HB-5100-benzoyl dextran with a degree of substitution of 0.18 was determined at room temperature. This two-phase system has been used to purify 3-phosphoglycerate kinase from bakers' yeast. The top-phase polymer (Ucon) can be separated from target enzyme by increasing the temperature. The bottom-phase polymer (benzyol dextran) could be recovered by addition of salt. Yeast homogenate was partitioned in a primary Ucon 50-HB-5100-benzoyl dextran aqueous two-phase system. After phase separation the top phase was removed and temperature-induced phase separation was used for formation of a water phase and a Ucon-rich phase. The benzoyl dextran-enriched bottom phase from the primary system was diluted, and the polymer was separated from water by addition of Na₂SO₄.     

Aqueous two-phase partition applied to the isolation of plasma membranes and Golgi apparatus from cultured mammalian cells

Partitioning in dextran–poly(ethylene)glycol (PEG) aqueous–aqueous phase systems represents a mature technology with many applications to separations of cells and to the preparation of membranes from mammalian cells. Most applications to membrane isolation and purification have focused on plasma membranes, plasma membrane domains and separation of right side-out and inside-out plasma membrane vesicles. The method exploits a combination of membrane properties, including charge and hydrophobicity. Purification is based upon differential distributions of the constituents in a sample between the two principal compartments of the two phases (upper and lower) and at the interface. The order of affinity of animal cell membranes for the upper phase is: endoplasmic reticulum<mitochondria<Golgi apparatus<lysosomes and endosomes<plasma membranes. Salt concentrations and temperature affect partitioning behavior and must be precisely standardized. In some cases, it is more fortuitous to combine aqueous two-phase partition with other procedures to obtain a more highly purified preparation. A procedure is described for preparation of Golgi apparatus from transformed mammalian cells that combines aqueous two-phase partition and centrifugation. Also described is a periodic NADH oxidase, a new enzyme marker for right side-out plasma membrane vesicles not requiring detergent disruptions for measurement of activity.     

α-Amylase production in aqueous two-phase systems with Bacillus amyloliquefaciens

-Amylase production was studied in Bacillus amyloliquefaciens in aqueous two-phase systems composed of polyethyleneglycol (PEG)/dextran T500. Cells and enzyme were obtained in different phases when phase systems were applied to the growth media. Effects of different molecular weights and concentrations of polymers on differences of enzyme separation were established. The effect of PEG used in the system to the release of enzyme was investigated.