Separation of Flavonoids from Bamboo Leaves by Aqueous Two-Phase Extraction

以竹叶黄酮水提溶液为原料,采用PEG(聚乙二醇)/(NH4 )2SO4双水相体系对竹叶黄酮进行萃取,考察了PEG平均相对分子质量、PEG质量分数、(NH4)2SO4质量分数、pH值、NaCl质量分数、原液质量分数、萃取温度等对双水相及竹叶黄酮萃取效果的影响.双水相萃取法提取竹叶黄酮的最优条件为:PEG 400 31％,(NH4)2 SO4 11％,pH3.9,NaCl 0.7％,原液51.5％,萃取温度20℃,在此条件下得到的竹叶黄酮萃取率为97.8％.结果说明,双水相萃取法操作简单方便,成本低,不会引起生物质失活或变性,适合于黄酮类化合物的萃取分离.     

响应面法优化白头翁总黄酮提取工艺

采用无水乙醇C2H5OH/硫酸铵(NH4)2SO4双水相体系分离白头翁中的黄酮。确定双水相体系组成为21%C2H5OH/22%(NH4)2SO4,通过单因素试验和Box-Benhnken实验设计探讨黄酮粗提液质量分数、NaCl质量分数和pH值对萃取效果的影响。确定最佳萃取条件为:黄酮粗提液质量分数12.5%,NaCl质量分数1.5%,pH 5.99,在此条件下,白头翁总黄酮主要分布在上相,萃取率可达73.6%。     

双水相体系萃取人参根中人参皂苷的研究

建立稳定的聚乙二醇(PEG)与(NH4)2SO4双水相体系以分离人参根中人参皂苷。通过上下相体积比(R)、分配系数(K)和回收率(Y)分析双水相体系对人参皂苷的萃取效果,研究了PEG分子量、PEG/(NH4)2SO4质量分数、pH值和温度等因素对双水相成相及人参皂苷萃取的影响。结果表明:PEG分子量为3350、PEG3350的质量分数为12%、(NH4)2SO4质量分数为16%、溶液pH为7.0、温度为60℃时,双水相体系对人参皂苷有较高的萃取率,回收率可到达88.94%。     

双水相萃取丽江山慈菇中的秋水仙碱

建立了由聚乙二醇(PEG6000)与(NH4)2SO4形成的双水相体系萃取丽江山慈菇中秋水仙碱的新方法。考察了PEG分子量、PEG的浓度、(NH4)2SO4的浓度和pH值对双水相成相及秋水仙碱萃取率的影响,并结合HPLC对萃取相进行检测。结果表明:PEG6000质量分数为8%,(NH4)2SO4质量分数为20%,pH为7.0时,双水相体系对丽江山慈菇粗提液中秋水仙碱萃取率达82.09%,富集倍数为6.84倍。此方法可用于丽江山慈菇中秋水仙碱的初步分离富集,且操作简单,绿色无污染。     

1-辛基-3-甲基咪唑二氰铵盐/硫酸铵双水相体系分离纯化银杏黄酮

建立了由亲水性离子液体1-辛基-3-甲基咪唑二氰铵盐([C8mim][N(CN)2])和(NH4)2SO4形成的双水相萃取体系并应用于银杏黄酮的分离纯化研究。研究了盐浓度、体系温度、pH值、NaCl量等因素对银杏黄酮萃取效率的影响;并对下相中无机盐进行回收。体系由18.52%[C8mim][N(CN)2],25.93%(NH4)2SO4构成,加入1.5 mmol NaCl,在室温下进行萃取时萃取效率最佳,在最佳的条件下[C8mim][N(CN)2]/(NH4)2SO4体系对银杏黄酮的萃取效率达96.73%。与传统的双水相体系相比,该体系的萃取效率高,粘度低,同时(NH4)2SO4的回收率达90.54%。[C8mim][N(CN)2]/(NH4)2SO4双水相体系是一种很好的分离纯化银杏黄酮的方法。     

白地霉Cryytococcus neoformans脂肪酶的双水相萃取

本文研究了不同无机盐的双水相体系对白地霉脂肪酶的萃取分离效果,对PEG/（NH4）2SO4成相系统进行了系统的研究,通过考察体系PEG分子量、不同的无机盐、PEG浓度、（NH4）2SO4浓度、离子强度、pH值及（NH4）2SO4浓度对反萃取的影响,并通过正交实验进一步优化了实验条件,初步确定在PEG浓度15%,（NH4）2SO4浓度22.5%,pH8.0,不加NaCl的条件下进行双水相萃取,脂肪酶分离系数和纯化倍数分别为6.8和7.5,比活力达到40.3 U/mg蛋白。     

白地霉脂肪酶的双水相萃取和反胶团提取

对影响双水相萃取和反胶团提取脂肪酶的各种因素进行了探讨,并通过正交实验进一步优化提取条件,PEG浓度15%,(NH4)2SO4浓度22.5%,pH8.0的条件下进行双水相萃取,脂肪酶纯化倍数达到7.5倍;CTAB浓度150mmol/L,相体积比4/2,水相pH8.0,温度40℃的条件下进行反胶团提取,脂肪酶的比活力达到最大,但其比活力稍有下降,约为原来的0.9倍。     

聚乙二醇共沉淀物复溶萃取辣根过氧化物酶的条件优化

为了改进辣根过氧化物酶的提纯方法,在双水相萃取的基础上使用聚乙二醇(PEG6000)在高饱和度(NH4)2SO4中沉淀辣根提取液中的过氧化物酶,利用磷酸盐溶液复溶解共沉淀物形成的双水相萃取体系能高效回收高纯度酶蛋白。研究了pH、PEG浓度和(NH4)2SO4饱和度对酶活性的影响,并考察不同液固比、pH和NaCl浓度对目标酶在双水相体系中的分配行为,并通过响应面法优化出最优萃取条件。结果表明:在液固比0.3 m L/g、pH7.02和NaCl 42 g/L的优化萃取条件下,辣根过氧化物酶回收率达88.1%,酶纯度较优化前提高了21.7倍。该方法的建立对于微量蛋白质的高效率提纯具有重量的参考价值。     

PEG／（NH4）2SO4双水相体系在加杨叶总黄酮萃取分离中的应用

目的：寻找加杨叶粗提液中的总黄酮的有效方法。方法：利用双水相体系萃取分离、紫外分光光度法直接测定。结果：萃取分离加杨叶总黄酮的最佳双水相体系是25％PEG400与12％（NH4）2SO4,最佳萃取条件为：pH=9,NaCl的添加量为3％,粗提液3mL,温度25℃。结论：该方法的相对标准偏差（RSD）≤0．28％（n=5）,具有良好的精密度和选择性,为黄酮类化合物萃取分离的一种有效方法。     

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％。     

双水相体系萃取分离杜仲叶中桃叶珊瑚甙的研究

建立了由高分子化合物聚乙二醇(PEG4000)与葡聚糖40000(D40)形成的双水相体系萃取分离杜仲叶中桃叶珊瑚甙的新方法.考察了萃取体系相图,研究了PEG4000/D40质量分数、样品溶液加入量、pH值和温度等因素对双水相成相及桃叶珊瑚甙萃取率的影响.结果表明:PEG4000的质量分数为11%,D40质量分数为8%、样品溶液加入量为8 g,温度为60℃,溶液pH为7时,双水相体系对桃叶珊瑚甙有较高的萃取率,重复三次可达到66.32%,而且萃取得到的桃叶珊瑚甙产品的纯度达到48.67%,远远高于粗提物中的8.750%.     

Purification of hyperthermophilic archaeal amylolytic enzyme (MJA1) using thermoseparating aqueous two-phase systems

Purification of a recombinant, thermostable alpha-amylase (MJA1) from the hyperthermophile, Methanococcus jannaschii, was investigated in the ethylene oxide-propylene oxide random copolymer (PEO-PPO)/(NH(4))(2)SO(4), and poly(ethylene glycol) (PEG)/(NH(4))(2)SO(4) aqueous two-phase systems. MJA1 partitioned in the top polymer-rich phase, while the remainder of proteins partitioned in the bottom salt-rich phase. It was found that enzyme recovery of up to 90% with a purification factor of 3.31 was achieved using a single aqueous two-phase extraction step. In addition, the partition behavior of pure amyloglucosidase in polymer/salt aqueous two-phase systems was also evaluated. All of the studied enzymes partitioned unevenly in these polymer/salt systems. This work is the first reported application of thermoseparating polymer aqueous two-phase systems for the purification of extremophile enzymes.     

牛血清白蛋白在聚乙二醇/葡聚糖双水相体系中分配特性的研究

采用考马斯亮蓝G250染色法测得室温下BSA在PEG/dextran双水相体系中的分配系数。以BSA在PEG/dextran体系的下相富集为目标,研究了PEG的分子量、浓度、dextran浓度以及所加入中性盐的种类与浓度、体系pH诸因素对其分配特性的影响。实验结果表明,在PEG4000/dextran体系中,采用PEG质量分数9%-dextran质量分数9%的浓度组成,同时在pH=7.0,NaC l浓度为0.2 mol.L-1或pH6.0,NaC l浓度为0.34 mol.L-1的工艺条件下萃取BSA均可达最小分配系数,其值为0.014。     

苦瓜籽蛋白的PEG/（NH4）2SO4双水相分离及抑菌作用的研究

优化试验条件影响因素,建立PEG/(NH4)2SO4双水相系统,确定出分离苦瓜籽蛋白的最适PEG6000和(NH4)2SO4质量分数分别是22%、25%,分配系数为0.089,回收率为96%。双水相分离的苦瓜籽蛋白经SDS-PAGE凝胶电泳显示,主要蛋白质是50 KD4、3 KD和10 KD亚基结合形成的多聚体12S(327 KD)球蛋白,还原条件下出现诸多小于35 kD的蛋白组分,表明蛋白质亚基是通过二硫键结合。抑菌试验显示苦瓜籽蛋白对受试细菌菌和真菌产生明显的抑菌活性,其MIC远低于苯甲酸钠,而且在不同盐离子浓度、温度、pH及紫外线等因素处理时,均具有一定的稳定性。此外试验还表明苦瓜籽蛋白也具有较强的清除羟自由基能力和总抗氧化能力。     

AQUEOUS TWO-PHASE EXTRACTION FOR THE PURIFICATION OF ALKALINE AGARASES FROM CULTURE EXTRACTS OF Pseudomonas aeruginosa AG LSL-11

The agarases were purified for the first time an using aqueous two-phase system (ATPS) consisting of polyethylene glycol (PEG) and phosphate salt. The three extracellular, alkaline agarases produced by Pseudomonas aeruginosa AG LSL-11 were efficiently extracted into the top PEG-rich layer. The influencing factors on the partition of agarases—molecular weight of the PEG, system pH, system temperature, and NaCl concentration—were investigated. All the factors were found to have a significant effect on the partition of agarases except NaCl. The optimal ATPS parameters for the partitioning and purification of agarases were found to be 12% PEG 600 and 11.9% (w/w) phosphate salt at pH 8.0 and 4°C. All three agarases were concentrated in the top PEG phase with 6.19-fold purity and 71.21% recovery. The ATPS was found to be more convenient and economical than the conventional ion-exchange chromatography (IEC) method for extraction of three agarases and could be significantly employed for the purification of agarases from fermentation broth.     

Role of polymer–protein interaction on partitioning pattern of bovine pancreatic trypsinogen and alpha-chymotrypsinogen in polyethyleneglycol/sodium tartrate aqueous two-phase systems

The partitioning pattern of bovine trypsinogen (TRPz) and alpha-chymotrypsinogen (ChTRPz) was investigated in a low impact aqueous two-phase system formed by polyethyleneglycol (PEG) and sodium tartrate (NaTart) pH 5.00. ChTRPz exhibited higher partition coefficients than TRPz did in all the assayed systems. The decrease in PEG molecular weight and the increase in tie line length were observed to displace the partitioning equilibrium of both proteins to the top phase, while phase volume ratios in the range 0.5–1.5 showed not to affect protein partitioning behaviour. Systems formed by PEG of molecular weight 600 with composition corresponding to a high tie line length (PEG 12.93%, w/w and NaTart 21.20%, w/w) are able to recover most of both zymogens in the polymer-enriched phase. A crucial role of PEG–protein interaction in the partitioning mechanism was evidenced by isothermal calorimetric titrations. The major content of highly exposed tryptophan rests, present in ChTRPz molecule, could be considered to be determinant of its higher partition coefficient due to a selective charge transfer interaction with PEG molecule. A satisfactory correlation between partition coefficient and protein surface hydrophobicity was observed in systems formed with PEGs of molecular weight above 4000, this finding being relevant in the design of an extraction process employing aqueous two-phase systems.     

Extraction of cephalosporin C from whole broth and separation of desacetyl cephalosporin C by aqueous two-phase partition

Cephalosporin C was extracted from diluted or whole broth by PEG/salt aqueous two-phase systems. Parameters such as PEG molecular weight, salt type, pH, and salt concentration were investigated for finding a suitable extraction system. In PEG 600/ammonium sulfate or phosphate systems, K(c) (partition coefficienct of cephalosporin C) was observed to be larger than 1, with K(d) (partition coefficient of desacetyl cephalosporin C) being smaller than 1. The particular values of these coefficients would imply that the difficult separation of cephalosporin C and desacetyl cephalosporin C could possibly be achieved via the aqueous two-phase extraction. The addition of surfactants, water-miscible solvents, and neutral salts for enhancement of the separation efficiency was also investigated. The addition of surfactants to the system did not affect the separation efficiency substantially. K(c) would increase whereas K(d) decreased as a result of the addition of acetone, MeOH, EtOH, IPA, and n-BuOH. Meanwhile both K(c) and K(d) would decrease whenever neutral salts, NaCl, KCl, Kl, or KSCN, were added. The partitioning behavior of cephalosporin C and desacetyl cephalosporin C in filtered, whole, and different batches of broth was notably quite similar to that of diluted broth. The recovery yield of cephalosporin C in whole broth extraction was observed to be a function of centrifugal force used in phase separation. (c) 1994 John Wiley & Sons, Inc.