两次双水相萃取结合高效液相色谱法选择性分离唾液蛋白质的初步研究（英文）

双水相萃取是一种新型的液-液萃取技术,具有方法简单,易操作,成本低,易放大,条件温和,可保持蛋白质活性等明显优势,特别适用于生物样品的前处理和组分分离。本文建立了15% PEG-4000/8% NaH₂PO₄双水相体系,通过两次双水相萃取结合高效液相色谱法（HPLC）分离了唾液中的多种蛋白质。经过双水相萃取,对上、下两相中的蛋白质进行色谱的梯度洗脱分析。50 min内蛋白质的色谱峰可分为10组,根据其在上、下两相的分配规律还可划分为6个组分区。结果表明,两次双水相萃取结合HPLC可以实现唾液中的蛋白质的选择性分离。该法为复杂生物样品中的蛋白质多维度、选择性分离和分析提供了新的思路。     

双水相萃取-磁性阳离子交换剂联用分离蛋白质

双水相萃取(ATPS)分离蛋白质是基于蛋白质在上下两相间分配系数不同而达到彼此分离,它是一种简单、快速、低成本的蛋白质分离富集方法.表面修饰的磁性粒子与目标蛋白结合,在外加磁场作用下快速与原溶液分离,可实现目标蛋白分离和富集.双水相萃取与磁性分离均具有简单快速、条件温和的优点,在生物分离工程领域具有重要的应用价值.本文将双水相体系与热溶剂法制备的表面羧基功能化的磁性阳离子交换剂联用,用于蛋白质的逐级分离.     

聚乙二醇-硫酸铵-锌试剂体系中铜、镧、铀、铈萃取性能研究

对4种金属离子[铜（Ⅱ），镧（Ⅲ），铀（Ⅵ）及铈（Ⅳ）]在双水相液-液萃取体系[聚乙二醇2000（PEG）-（NH4）2SO4-锌试剂]中的萃取行为，特别是影响萃取的条件（包括溶液的酸度，锌试剂用量；硫酸铵加入量及有无表面活性剂存在等）作了研究。结果表明，铜（Ⅱ）在pH3～8的条件下，以锌试剂螯合物的形态被定量萃取进入PEG相，萃取率在95％以上；镧（Ⅲ）在pH1～7之间不被萃取，仍以离子状态留在下层水相中；而铀（Ⅵ）及铈（IV）在pH1～11范围内萃取不完全，萃取率在30％～65％之间。试验表明，在pH6的条件下，铜（Ⅱ）可与共存的镧（Ⅲ）定量分离，铜（Ⅱ）进入PEG相的萃取率在95．6％～98．3％之间，而共存的镧（Ⅲ）仅有4．5％～5．1％进入PEG相中。对锌试剂作为螯合剂与上述4种金属离子在萃取过程的反应机理作了初步探讨。     

双水相浮选过程中青霉素的分离行为

基于双水相浮选技术(ATPF)分离富集水相中青霉素的方法,研究了双水相浮选过程中青霉素的分离行为.在常温下,2.5 g/L青霉素水溶液300 mL、初始pH 7、(NH4)2SO4浓度350 g/L、浮选溶剂为50%(w/w)PEG1000水溶液10 mL条件下,分别研究了青霉素在双水相浮选过程中的动力学行为和分离后的...     

Co(Ⅱ)-4-(2-吡啶偶氮)间苯二酚-聚乙二醇-(NH4)2SO4萃取体系的研究和应用

研究了Co(Ⅱ)-4-(2-吡啶偶氮)间苯二酚(PAR)-聚乙二醇(PEG)-(NH4)2SO4体系的萃取行为及最佳分相条件,建立了测定生物样品中微量钴的非有机溶剂萃取光度法。结果表明,在pH 8.6的六次甲基四胺缓冲溶液中,在(NH4)2SO4存在下,Co(Ⅱ)-PAR的络合物可被PEG相富集萃取。在PEG相中络合物的最大吸收波长为519 nm,表观摩尔吸光系数4.68×104L.mol-1.cm-1,钴量在0~1.8μg/mL范围内服从比尔定律。方法已用于粮食、茶叶等生物样品中痕量钴的测定,回收率97.2%~103%。     

正负离子表面活性剂与高聚物混合双水相体系的相行为及蛋白质的分配

报道了由正负离子表面活性剂与高聚物混合溶液形成的一种可用于蛋白质的分离及分析的新型双水相萃取体系.研究了正负离子表面活性剂(溴化十二烷基三乙铵/十二烷基硫酸钠)分别与葡聚糖和聚乙二醇混合双水相体系的形成规律、相行为及牛血清蛋白和溶菌酶在双水相体系中的分配.通过在高聚物分子中接上亲和配基,研究蛋白质在双水相体系中的亲和分配.结果表明,在该体系中,表面活性剂与高聚物分别富集于不同相中.升高温度及加入无机盐均可促进双水相体系的形成,不同蛋白质可分配于不同的相中.亲和配基的引入极大地增强了蛋白质分配的选择性.     

组合表面活性剂-盐-水双水相体系萃取水杨酸和洛美沙星

通过实验选择聚乙二醇(PEG1500)与聚乙烯吡咯烷酮(PVP30000)组合表面活性剂(NH4)2SO4-H2O形成双水相体系及其成相条件。研究水杨酸(APC)和洛美沙星(LFXC)氢键型药物在该双水相体系中的分配行为。结果表明：该体系对APC和LFXC的萃取率分别为102％和69．0％。通过药物在该体系中的紫外吸收光谱及分子荧光光谱的变化,验证其萃取药物的机理。     

PEG-无机盐双水相体系萃取水榆花楸叶中总黄酮

水榆花楸叶中所含的黄酮类化合物具有一定的药用价值,利用双水相技术萃取水榆花楸叶中的黄酮是一种有效的分离纯化方法。本文考察了不同种类的无机盐与不同相对分子量的PEG组成的双水相体系的两相性质,研究了PEG1000-Na_2SO_4双水相体系中分离纯化水榆花楸黄酮时PEG的质量分数、Na_2SO_4的质量分数、温度、p H、KCl添加量这5个因素对分配行为的影响,并通过正交实验优化了试验条件。结果表明最佳双水相萃取条件为:Na_2SO_4的质量分数为15%,PEG1000质量分数为30%,p H为9,提取温度为25℃,KCl的添加量为3%,此时原料中黄酮的萃取率可高达97.01%。因此,该体系是一种高效分离纯化水榆花楸叶中黄酮的方法。     

聚乙二醇-硫酸铵-茜素S体系中镧、镨和镝的萃取分离研究

探讨了在聚乙二醇2000(PEG) 硫酸铵 茜素S双水相体系中,茜素S作萃取剂,稀土金属离子镧、镨、镝的萃取行为。镝离子在pH4～9范围萃取率皆在95%以上,可认为被定量萃取到PEG相;镨离子在pH3～12之间几乎不被萃取,仍以简单金属离子留在了下层水相,而在此酸度下,镧离子萃取率则为34%～60%,萃取不完全。通过控制一定条件,实现了镝与镨的定量分离,并初步探讨了PEG相的萃取机理。     

蛋白质在表面活性剂与高分子共组双水相体系中 的分配

高分子和正负离子表面活性剂混合物可形成一种新型双水相体系。研究蛋白质在溴化十二烷基三乙铵/十二烷基硫酸钠与聚氧乙烯(EO)-聚氧丙烯(PO)嵌段共聚物(EO~2~0PO~8~0)共组双水相体系中的分配。通过在高分子接上亲和配基,研究蛋白质在带有亲和配基高分子的双水相体系中的分配。将表面活性剂富集相稀释或加热高分子富集相,又可形成新的双水相体系,由此可进行蛋白质的多步分配。在蛋白质的分配完成之后,通过将表面活性剂富集相进一步稀释或将高分子富集相加热至高分子浊点以上可将表面活性剂和高分子与目标蛋白质分离。正负离子表面活性剂和高分子还可以循环使用。     

Purification of plasmid DNA vectors by aqueous two-phase extraction and hydrophobic interaction chromatography

The current study explores the possibility of using a polyethyleneglycol(PEG)-ammonium sulphate aqueous two-phase system (ATPS) as an early step in a process for the purification of a model 6.1 kbp plasmid DNA (pDNA) vector. Neutralised alkaline lysates were fed directly to ATPS. Conditions were selected to direct pDNA towards the salt-rich bottom phase, so that this stream could be subsequently processed by hydrophobic interaction chromatography (HIC). Screening of the best conditions for ATPS extraction was performed using three PEG molecular weights (300, 400 and 600) and varying the tie-line length, phase volume ratio and lysate load. For a 20% (w/w) lysate load, the best results were obtained with PEG 600 using the shortest tie-line (38.16%, w/w). By further manipulating the system composition along this tie-line in order to obtain a top/bottom phase volume ratio of 9.3 (35%, w/w PEG 600, 6%, w/w NH4)2 SO4), it was possible to recover 100% of pDNA in the bottom phase with a three-fold increase in concentration. Further increase in the lysate load up to 40% (w/w) with this system resulted in a eight-fold increase in pDNA concentration, but with a yield loss of 15%. The ATPS extraction was integrated with HIC and the overall process compared with a previously defined process that uses sequential precipitations with iso-propanol and ammonium sulphate prior to HIC. Although the final yield is lower in the ATPS-based process the purity grade of the final pDNA product is higher. This shows that it is possible to substitute the time-consuming two-step precipitation procedure by a simple ATPS extraction.     

Selective separation and enrichment of proteins in aqueous two-phase extraction system

A simple aqueous two-phase extraction system(ATPS) of PEG/phosphate was proposed for selective separation and enrichment of proteins.The combination of ATPE with HPLC was applied to identify the partition of proteins in two phases.Five proteins (bovine serum albumin,Cytochrome C,lysozyme,myoglobin,and trypsin) were used as model proteins to study the effect of phosphate concentration and pH on proteins partition.The PEG/phosphate system was firstly applied to real human saliva and plasma samples,some pro...     

Affinity partitioning of human antibodies in aqueous two-phase systems

The partitioning of human immunoglobulin (IgG) in a polymer-polymer and polymer-salt aqueous two-phase system (ATPS) in the presence of several functionalised polyethylene glycols (PEGs) was studied. As a first approach, the partition studies were performed with pure IgG using systems in which the target protein remained in the bottom phase when the non-functionalised systems were tested. The effect of increasing functionalised PEG concentration and the type of ligand were studied. Afterwards, selectivity studies were performed with the most successful ligands first by using systems containing pure proteins and an artificial mixture of proteins and, subsequently, with systems containing a Chinese hamster ovary (CHO) cells supernatant. The PEG/phosphate ATPS was not suitable for the affinity partitioning of IgG. In the PEG/dextran ATPS, the diglutaric acid functionalised PEGs (PEG-COOH) displayed great affinity to IgG, and all IgG could be recovered in the top phase when 20% (w/w) of PEG 150-COOH and 40% (w/w) PEG 3350-COOH were used. The selectivity of these functionalised PEGs was evaluated using an artificial mixture of proteins, and PEG 3350-COOH did not show affinity to IgG in the presence of typical serum proteins such as human serum albumin and myoglobin, while in systems with PEG 150-COOH, IgG could be recovered with a yield of 91%. The best purification of IgG from the CHO cells supernatant was then achieved in a PEG/dextran ATPS in the presence of PEG 150-COOH with a recovery yield of 93%, a purification factor of 1.9 and a selectivity to IgG of 11. When this functionalised PEG was added to the ATPS, a 60-fold increase in selectivity was observed when compared to the non-functionalised systems.     

聚乙二醇双水相萃取光度法测定镍

用水溶性高聚物、表面活性剂及有机物与无机盐形成的双水相体系萃取分离色素、蛋白质及测定金属离子已有报道[1-5].     

Solvent systems for countercurrent chromatography: an aqueous two phase liquid system based on a room temperature ionic liquid

A new aqueous two phase liquid system (ATPS) based on the ionic liquid 1-butyl-3-methyl imidazolium chloride (BMIM Cl), potassium dibasic phosphate (K(2)HPO(4)) and water was recently proposed in the literature. The full phase diagram of this ATPS was prepared and some tie lines were fully determined. It was compared to classical ATPSs based on polyethylene glycol with an average molecular mass of 1000 (PEG 1000) and 10,000 (PEG 10000) and K(2)HPO(4). Two countercurrent chromatography (CCC) columns, a hydrostatic Sanki and a J type hydrodynamic CCC columns were used to test the liquid phase retention of these ATPSs in all possible configurations. It was found that the BMIM Cl ATPS liquid phases were much easier to retain in the two CCC columns than the PEG 1000 ATPS phases. Using protein and alcohol solutes, it was established that the BMIM Cl ATPS has a polarity completely different from that of the PEG 1000 ATPS. For example, ovalbumin partitions equally between the two phases of the PEG 1000 ATPS (K(D)=1.4) when it is completely located in the BMIM Cl upper phase of the ionic liquid ATPS (K(D)=180). The discrimination factor of the ionic liquid system and its intrinsic hydrophobicity were respectively found three times higher and ten times lower than the respective values of the PEG 1000 ATPS.     

Evaluation of a PEG/hydroxypropyl starch aqueous two‐phase system for the separation of monoclonal antibodies from cell culture supernatant

In this study, an aqueous two‐phase system (ATPS) with PEG and hydroxypropyl starch (HPS) was used to separate monoclonal antibody (mAb) from Chinese hamster ovary cell culture supernatant. The phase diagram of the PEG/HPS ATPS was determined, and the effects of NaCl addition were investigated. The results showed that NaCl addition could lead to a shift of the binodal curve and that phase separation would occur at higher PEG and HPS concentrations. The effects of NaCl addition, pH, and the load of cell supernatant on the partitioning of mAb in a PEG/HPS ATPS were investigated. It was found that with 6% cell supernatant and 15% NaCl addition at pH 6.0, the yield of mAb in the upper phase was 96.7% with a purity of 96.0%. The back‐extraction of mAb with a PEG/phosphate ATPS were also studied, and the results showed that after the two‐step extraction with ATPSs the purity of mAb could reach 97.6 ± 0.5% with a yield of 86.8 ± 1.0%, which was comparable to the purification with Protein A chromatography. These results indicate that the two‐step extraction with PEG/HPS and PEG/phosphate ATPSs might be a promising alternative for the separation of mAb from cell culture supernatant.     

Aqueous two-phase partitioning of milk proteins

Milk of transgenic pigs secreting recombinant human Protein C (rHPC) was used as a model system to determine the utility of aqueous two-phase extraction systems (ATPS) for the initial step in the purification of proteins from milk. The major challenges in purification of recombinant proteins from milk are removal of casein micelles (that foul processing equipment) and elimination of the host milk proteins from the final product. When milk was partitioned in ATPS composed of polyethylene glycol (PEG) and ammonium sulfate (AS), the phases were clarified and most of the caseins precipitated at the interphase. The partition coefficients of the major milk proteins and rHPC were dependent upon the molecular weight of the PEG used in the ATPS. Higher-partition coefficients of the major whey proteins, Β-lactoglobulin, and α-lactalbumin were observed in ATPS made up of lower molecular-weight PEG (1000 or 1450) as compared to systems using higher molecular-weight PEG. Lowering the pH of the ATPS from 7.5 to 6.0 resulted in increased precipitation of the caseins and decreased their concentration in both phases. rHPC had a partition coefficient of 0.04 in a system composed of AS and PEG 1450. The rHPC in pig milk was shown to be highly heterogenous by two-dimensional gel electrophoresis. The heterogeneity was owing to inefficient proteolytic processing of the single chain to the heterodimeric form and differences in glycosylation and other post-translational processing. Differential partitioning of the multiple forms of purified rHPC in the ATPS was not observed. rHPC after processing in ATPS was recovered in a clear phase free of most major milk proteins. ATPS are useful as the initial processing step in the purification of recombinant proteins from milk because clarification and enrichment is combined in a single step.     

Separation of endo-polygalacturonase using aqueous two-phase partitioning

The partitioning of endo-polygalacturonase (endo-PG) in polyethylene glycol (PEG)-polyvinyl alcohol (PVA10000) and PEG-hydroxypropyl starch (Reppal PES100) aqueous two-phase systems was studied, and revealed the possibility of using aqueous two-phase extraction to purify and concentrate endo-PG from its clarified fermentation broth. For the PEG8000-PVA10000 system, endo-PG presented in the fermentation broth (at concentration that is more than 40% of total protein) mainly dominates in the top phase with a partitioning coefficient of 6, while total protein concentrates in the bottom phase. A separation scheme consisting of two consecutive aqueous two-phase extraction steps was proposed: a first extraction in polyethylene glycol (PEG8000)-polyvinyl alcohol system, followed by a second extraction in PEG8000-(NH4)2SO4 system. This allowed the separation of endo-PG from polymer and the recycling of PEG polymer, since endo-PG was very strongly partitioned into the bottom phase of the PEG8000-(NH4)2SO4 system. Laboratory-scale experiments were performed to test the efficiency of this scheme. It was found that enzyme recovery was up to 91% with a total purification factor of about 1.9 and a concentration factor of more than 5. About 90% of the total PEG added into the systems can be recovered, and no reduction was obtained in the purification factor using recycled PEG.     

双水相体系选择性分离富集维生素B_(12)及电热原子吸收法测定

用异丙醇-硫酸铵双水相体系,利用维生素B12的疏水性和硫酸铵的盐析作用,在高浓度无机Co2+共存的情况下可有效地实现维生素B12的选择性分离富集.对双水相体系的组成、萃取时间和pH等实验参数进行了优化,在2.0mL样品、1.1g硫酸铵和200μL异丙醇组成的双水相体系中,对50μgL-1的维生素B12溶液经过萃取分离后富集倍数为11.8.取20μL双水相体系上相进行电热原子吸收检测,线性范围为2～100μgL-1,检出限为0.6μgL-1(3σ,n=11),相对标准偏差为2.8%(50μgL-1,n=9).将所建立的方法应用于功能饮料、保健药片、牛肝等实际样品中维生素B12的含量测定,加标回收率在97%～104%之间.     

Application of central composite design to the optimisation of aqueous two-phase extraction of human antibodies

The partition of human antibodies in aqueous two-phase systems (ATPSs) of polyethylene glycol (PEG) and phosphate was systematically studied using first pure proteins systems and then an artificial mixture of proteins containing 1mg/ml human immunoglobulin G (IgG), 10mg/ml serum albumin and 2mg/ml myoglobin. Preliminary results obtained using pure proteins systems indicated that the PEG molecular weight and concentration, the pH value and the salts concentration had a pronounced effect on the partitioning behaviour of all proteins. For high ionic strengths and pH values higher than the isoelectric point (pI) of the contaminant proteins, IgG could be selectively recovered on the top phase. According to these results, a face centred composite design was performed in order to optimise the purification of IgG from the mixture of proteins. The optimal conditions for the isolation of IgG were observed for high concentrations of NaCl and low concentrations of both phase forming components. The best purification was achieved using an ATPS containing 8% (w/w) PEG 3350, 10% (w/w) phosphate pH 6 and 15% (w/w) NaCl. A recovery yield of 101+/-7%, a purity of 99+/-0% and a yield of native IgG of 97+/-4% were obtained. Back extraction studies of IgG to a new phosphate phase were performed and higher yields were obtained using 10% phosphate buffer at pH 6. The total extraction yield was 76% and the purity 100%.