Improved recovery of B‐phycoerythrin produced by the red microalga Porphyridium cruentum

A simplified process for the primary recovery and purification of B‐phycoerythrin (BPE) from Porphyridium cruentum exploiting aqueous two‐phase systems (ATPS) and isoelectric precipitation was developed in order to reduce the number of unit operations and benefit from increased purity and yield of the protein product. Evaluation of the partitioning behaviour of BPE in polyethylene glycol (PEG)/sulphate, PEG/dextran and PEG/phosphate ATPS was carried out to determine under what conditions the BPE and contaminants concentrated into opposite phases. An additional stage of isoelectric precipitation at pH 4.0 after cell disruption resulted in an increase in purity of the target protein from the BPE crude extract and enhanced the performance of the subsequent ATPS. PEG1000/phosphate ATPS proved to be suitable after isoelectric precipitation for the recovery of highly purified (defined as absorbance ratio A_{545 nm}/A_{280 nm} > 4.0) BPE with a potential commercial value as high as US$ 50/mg. An ATPS extraction stage comprising 29.5% (w/w) PEG1000, 9.0% (w/w) phosphate, a volume ratio (V_r) equal to 1.0, a system pH of 7.0 and loaded with 40% (w/w) of the BPE extract generated by precipitation allowed BPE recovery with a purity of 4.1±0.2 and an overall product yield of 72% (w/w). The purity of BPE from the crude extract increased 5.9‐fold after isoelectric precipitation and ATPS. The results reported herein demonstrate the benefits of the practical application of isoelectric precipitation together with ATPS for the recovery and purification of BPE produced by P. cruentum as a first step in the development of a commercial purification process. Copyright © 2006 Society of Chemical Industry     

Recovery of value‐added globular proteins from tannery wastewaters using PEG – salt aqueous two‐phase systems

Leather processing involves discharge of high‐value soluble globular proteins in the wastewater. The recovery of value‐added products from the wastewaters is gaining more importance in the context of recovery of wealth from waste. The recovery of these globular proteins from tannery wastewater was selected as a practical model system to study the implementation of polyethylene glycol (PEG)‐sulfate aqueous two‐phase systems (ATPS). The partition coefficient of bovine serum albumin is comparable to that of soluble proteins from tannery wastewaters. The influence of concentration of polymer, salt, pH and temperature on the partitioning of soluble proteins from tannery wastewaters has been studied. The PEG6000 + sodium sulfate + water system provide better partitioning of these soluble proteins as compared to PEG6000 + ammonium sulfate system. The maximum protein recovery yield for PEG6000 + sodium sulfate + water system at 20 °C is 92.75%. The influence of temperature indicates the recovery of proteins from tannery wastewater to be better at lower temperature. The findings of these studies raise the potential application of ATPS processes for protein recovery from complex biological systems. Copyright © 2006 Society of Chemical Industry     

Purification of biomolecules combining ATPS and membrane chromatography

Upstream processes for production of therapeutic proteins have been innovated and fermentation processes have been adopted for the use of recombinant microorganisms with high expression, but the downstream process is still the bottleneck in the biotechnological manufacturing process. A combined process consisting of aqueous two phase extraction (ATPE) and membrane chromatography is suggested to debottleneck downstream processing. ATPE has a large capacity, but the yield of the target product is from 74% to 97%. For this reason the product of ATPE waste stream is captured by membrane chromatography. In this work the binding capacity for the protein on protein A, ion exchange and hydrophobic exchange membrane chromatography was investigated experimentally with different concentration of polyethylene glycol (PEG), salt and protein. Protein A membrane was loaded with solutions resembling waste streams of ATPE for purifying IgG. For ion exchange and hydrophobic interaction membrane chromatography, the membrane was loaded with bovine serum albumin (BSA). PEG shows no significant effect on stability and capacity of membrane process. Even for small amount of BSA/IgG and high salt concentrations membrane adsorption is applicable. In this work it is demonstrated experimentally that a total product recovery of 99.9% for the purification of monoclonal antibody is possible.     

Impact of polyethylene glycol as additive on the formation and extraction behavior of ionic‐liquid based aqueous two‐phase system

Developing a novel Ionic‐liquid (IL) based aqueous two‐phase system (ATPS) with polyethylene glycol (PEG) as adjuvant for the separation of biomolecules is studied. This original work involves addition of various concentration of PEG (2000, 4000, and 6000 gr/mol) to 1‐butyl‐3‐methylimidazolium acetate+ potassium hydrogen phosphate ATPS to investigate their subsequent effect on phase diagrams and partitioning coefficient of α‐amylase. In another innovative aspect of this work, response surface methodology (RSM) based on three‐variable central composite design was employed to understand the effect of phase forming components on extraction studies of α‐amylase. The addition of small amount of PEG improved the partitioning coefficient of biomolecule. The effective excluded volume theory was applied to correlate the salting‐out ability. As a result, it can be stated that the proposed system can effectively be used in separation and purification studies instead of task specific ILs. © 2015 American Institute of Chemical Engineers AIChE J, 62: 264–274, 2016     

Practical application of aqueous two‐phase systems for the development of a prototype process for c‐phycocyanin recovery from Spirulina maxima

A novel process for the recovery of c‐phycocyanin from Spirulina maxima exploiting aqueous two‐phase systems (ATPS), ultrafiltration and precipitation was developed in order to reduce the number of unit operations and benefit from an increased yield of the protein product. The evaluation of system parameters such as PEG molecular mass, concentration of PEG as well as salt, system pH and volume ratio was carried out to determine under which conditions the c‐phycocyanin and contaminants concentrate to opposite phases. PEG1450–phosphate ATPS proved to be suitable for the recovery of c‐phycocyanin because the target protein concentrated in the top phase whilst the cell debris concentrated in the bottom phase. A two‐stage ATPS process with a phase volume ratio (V_r) equal to 0.3, PEG1450 7% (w/w), phosphate 20% (w/w) and system pH of 6.5 allowed c‐phycocyanin recovery with a purity of 2.4 (estimated as the relationship of the 620 nm to 280 nm absorbances). The use of ultrafiltration (with a 30 kDa membrane cut‐off) and precipitation (with ammonium sulfate) resulted in a recovery process that produced a protein purity of 3.8 ± 0.1 and an overall product yield of 29.5% (w/w). The results reported here demonstrated the practical implementation of ATPS for the design of a prototype recovery process as a first step for the commercial purification of c‐phycocyanin produced by Spirulina maxima. © 2001 Society of Chemical Industry     

Liquid-liquid extraction of protease from cold-adapted yeast Rhodotorula mucilaginosa L7 using biocompatible and biodegradable aqueous two-phase systems

This work aimed to optimize the extraction of an extracellular protease produced by the cold-adapted yeast Rhodotorula mucilaginosa L7 using aqueous two-phase systems (ATPS) comprising polyethylene glycol (PEG) and sodium citrate or sodium tartrate. First, the biocompatibility of the phase forming agents was assessed. The results obtained with PEG-2000, PEG-4000, and PEG-6000 demonstrated that even at large PEG concentrations (32 wt%) the protease maintains its activity after 3 h of reaction, whereas an increase in salt concentration provokes a gradual decrease in protease stability. Subsequently, the partitioning of the protease in both types of ATPS was assessed, evaluating the effect of temperature, molecular weight, and concentration of PEG on protease purification, using two 2³-full factorial designs. The best partitioning conditions were obtained in PEG-6000/sodium tartrate-based ATPS, at 30ºC (with a yield of 81.09 ± 0.66% and a purification factor of 2.51 ± 0.03). Thus, considering the biodegradable characteristics of the system, the PEG/sodium tartrate ATPS is a viable and economic low-resolution step in protease purification, with a strong potential for future industrial application.     

以双水相萃取法从猪心中快速制备细胞色素C

把化工上常用的双水相萃取法应用于生物分离,从猪心中纯化具有药用价值的细胞色素C。以14％聚乙二醇和12％硫酸铵两相系统对粗提液进行萃取,细胞色素C全部浓缩于盐相。对盐相进行去盐后,经人造沸石快速吸附与洗脱、三氯醋酸沉淀等制得细胞色素C半成品,以弱酸性阳离子交换柱进行精制。聚丙烯酰胺凝胶电泳、可见吸收光谱扫描等定性定量分析证明了此法所得产品纯度好,提取率也较高。与传统方法比较,此法工艺简单,成本低,耗时少,尤其适用于大规模生产。     

Multistage Processing of Tunable Aqueous Polymer Phase Impregnated Resins (TAPPIR®)

A promising concept of aqueous two‐phase extraction (ATPE) is the Tunable Aqueous Polymer Phase Impregnated Resins (TAPPIR®) technology. Thereby, one phase of an aqueous two‐phase system (ATPS) is immobilized inside porous solids, which are then dispersed in the second aqueous phase. Beside extraction performance, the reusability of the impregnated solids for several cycles decides upon the competitiveness of TAPPIR®. Multistage extraction experiments using a polyethylene glycol 4000/citrate ATPS to partition lysozyme were investigated for TAPPIR® and ATPE. A stable impregnation was demonstrated for multiple cycles. Moreover, it was found that multistage extraction processes should not be designed on basis of the first extraction as the yield changes in the following stages.     

Purification of Glucose Oxidase and β‐Galactosidase by Partitioning in a PEG‐Salt Aqueous Two‐Phase System in the Presence of PEG‐Derivatives

Abstract

Purification of glucose oxidase from Aspergillus niger and that of β‐galactosidase from Kluyveromyces lactis have been attempted using poly(ethylene glycol) (PEG)‐sodium sulfate aqueous two phase system (ATPS) in the presence of PEG‐derivatives, i.e. PEG‐Coomassie brilliant blue G‐250 and PEG‐benzoate, PEG‐palmitate and PEG‐TMA, respectively. The enzymes showed poor partitioning towards the PEG phase in comparison with other proteins in ATPS containing no ligands. Selective partitioning of other proteins was observed towards the PEG phase in the presence of PEG‐benzoate and PEG‐palmitate enriching β‐galactosidase in the salt phase whereas in the case of glucose oxidase, PEG‐Coomassie brilliant blue G‐250 derivative worked as a better affinity ligand for other proteins. A 19‐fold purification was obtained with the PEG dye derivative after 5 stage cross extractions with 80% recovery of glucose oxidase and an enrichment factor upto ～7 for β‐galactosidase with the PEG‐TMA derivative. The interaction of PEG‐benzoate and PEG‐TMA ligands with the active site of β‐galactosidase has been evaluated by molecular modeling. The effect of the molecular weight of glucose oxidase on its partitioning was confirmed as the molecular simulation shows strong affinity interaction of PEG‐glucoside with the enzyme.     

Partitioning behaviour of cephalexin and 7‐aminodeacetoxicephalosporanic acid in PEG/ammonium sulfate aqueous two‐phase systems

In order to develop an aqueous two‐phase system (ATPS) for cephalexin synthesis with extractive bioconversion, the partitioning behaviour of cephalexin and 7‐aminodeacetoxicephalosporanic acid (7‐ADCA) in poly(ethylene glycol) (PEG)/salt ATPS were examined. Parameters such as PEG size, salt type and tie line length were investigated to find a primary extraction system. In PEG400/ammonium sulfate and PEG400/magnesium sulfate systems, the partition coefficient of cephalexin (K_C) was larger than 1 while that of 7‐ADCA (K_A) deviated about 1.5. Addition of neutral salts, surfactants and water‐miscible solvents were also investigated in the primary ATPS in order to improve the separation efficiency. K_C greatly increased when neutral salts and surfactants were added to the PEG400/ammonium sulfate primary systems whereas K_A was only slightly higher than that of the additive‐free ATPS. In an improved ATPS for extractive bioconversion, consisting of PEG400 (20% w/w), ammonium sulfate (17.5% w/w), methanol (5% w/w) and NaCl (3% w/w), a K_C value of up to 15.2 was achieved; K_A was 1.8; K_P (partition coefficient of phenylglycine methyl ester) was 1.2 and the recovery yield of cephalexin was 94.2%. The results obtained from the extractive bioconversion of cephalexin in the improved ATPS showed that it is feasible to perform such an enzymatic process in an ATPS and the system offers the potential as a model for enzymatic synthesis of some water soluble products. © 2001 Society of Chemical Industry     

Practical implementation of aqueous two‐phase processes for protein recovery from yeast

A two‐stage extraction process for the recovery of intracellular proteins from brewers' yeast was selected as a practical model system to study the implementation of polyethylene glycol (PEG)–phosphate aqueous two‐phase systems (ATPS). Disrupted all suspensions generated by homogenisation and bead milling were used to study the impact of cell debris upon the partition behaviour of the intracellular products (bulk protein, fumarase and pyruvate kinase). Regardless of their origin debris particles did not significantly influence the partition behaviour of the intracellular products in selected ATPS distant from the binodal and at volume ratios greater than one. Recycling of used PEG into the initial extraction stage did not significantly influence the protein partition behaviour in batch ATPS. In the polymer recycling studies in continuous ATPS using spray columns, the addition of fresh materials to make up the deficits of phase‐forming chemicals compensate any negative effect of the continuous recycling of the top PEG‐rich phase. The findings of these studies raise the potential application of ATPS processes for protein recovery from complex biological systems. © 2000 Society of Chemical Industry     

Recovery of Recombinant Dog Gastric Lipase from Corn Endosperm Extract

Abstract

Two separation methods, aqueous two‐phase (ATP) partitioning and cation‐exchange chromatography, were compared as alternative methods for the recovery of recombinant dog gastric lipase (r‐DGL) from extracts of transgenic corn endosperm. r‐DGL is a hydrophobic, acid‐stable protein targeted for stable expression in endosperm. Polyethylene glycol (PEG) ‐ salt ATP system parameters of PEG molecular weight, phase‐forming salt, NaCl addition, Triton X‐100 concentration and phase ratio were adjusted to achieve favorable partitioning. The purification factor and yield of r‐DGL in the bottom phase of a PEG 3350 (14.2%)‐Na₂SO₄ (8.5%)‐NaCl (0.5%)‐Triton X‐100 (2 mM) system at pH 4 were 1.5 and 80%, respectively. A higher purification factor of 2.3 and nearly 100% yield of r‐DGL was obtained in the top phase of a PEG 3350 (9.4%)‐phosphate (14.3%)‐NaCl(1.5%)‐Triton X‐100 (2 mM) system at pH 4.0. The yield, purification factor, and concentration factor were 90%, 7.7, and 3.6, respectively, for the alternative of cation‐exchange on CM‐Sepharose. Countercurrent ATP partitioning with 3–7 stages was calculated to achieve a purification factor equivalent to that from cation exchange but with a lower concentration factor. While the cation exchange was favored on this basis, the two approaches were close enough that further optimization and economic analysis would be needed to be definitive.     

多元渗透维里方程通式的表达：双水相系统的液液平衡计算

提出了基于三元系修正Ｐｉｔｚｅｒ模型的多元渗透维里方程通式，并应用于双水相系统液液平衡性质的关联和预测，用汽液平衡数据关联模型参数，预测了聚乙二醇／硫酸镁双水相系统的液液平衡；用汽液平衡数据和尽可能少的液液平衡数据关联模型参数。同时预测了焦点或不含电解质的ＰＥＧ／葡萄糖双水相系统的液液平衡和ＫＣｌ电解质在ＰＥＧ／ＤＥＸ系统中的分配系数。计算结果表明，模型有较好的预测功能。     

Aqueous two‐phase systems for the recovery of a recombinant viral coat protein from Escherichia coli

In this study the use of an aqueous two‐phase system (ATPS) following the direct chemical extraction of a recombinant viral coat protein, from the cytoplasm of Escherichia coli, is evaluated. The driving force is the need to establish an economically‐viable process for the manufacture of a vaccine against human papilloma infection. The partition behaviour of recombinant L1 protein, the major structural protein of the virus, and DNA was investigated in a polyethylene glycol (PEG)–phosphate system. An evaluation of system parameters including PEG molecular mass and the concentrations of PEG and phosphate was conducted, to estimate conditions under which the L1 protein and DNA partition to opposite phases. ATPS extraction comprising a volume ratio of 1.00, PEG 1000 (18.0%(w/w)) and phosphate (15.0%(w/w)) provided the conditions for accumulation of DNA into the bottom phase and concentration of L1 protein into the opposite phase (ie partition coefficient of DNA; ln K_DNA < 0.0 and partition coefficient of L1; ln K_L1 > 2.5). The findings reported here demonstrate the potential of ATPS to recover recombinant protein released from E coli by direct chemical extraction. © 2002 Society of Chemical Industry     

Process Design for Purification of Muscle Lactate Dehydrogenase by Affinity Partitioning Using Free Reactive Dyes

ABSTRACT

It was shown that by using free reactive dyes as affinity ligands, lactate dehydrogen-ase (LDH) can be purified with affinity partitioning directly from rabbit muscle homogenization. The free reactive dyes not bound to polyethylene glycol (PEG) showed a strong tendency toward the top PEG-rich phase in aqueous two-phase systems, and thus enhanced the affinity partitioning effect. Wide-ranged reactive dyes were screened in terms of their partitioning abilities for LDH. The effects of various parameters on affinity partitioning behavior of LDH, such as phase composition, impurities in raw material, concentration of dyes, pH of the systems, and addition of salts, were studied. The optimized affinity extraction process has been carried out for the large-scale purification of LDH from rabbit muscle homogenization. The enzyme was recovered with a yield of 81*middot;3% and a purification factor of 7. Both PEG and dyes were recovered and reused directly without lowering the quality of the product.     

A new polymerization method and kinetics for acrylamide: Aqueous two‐phase polymerization

The concept of aqueous two‐phase polymerization and a new polymerization method for the preparation of water‐soluble polymers are presented. The phase diagram of poly(acrylamide) (PAAm)‐poly (ethylene glycol) (PEG)‐water two‐phase system was measured by the gel permeation chromatography (GPC). The aqueous two‐phase of PAAm‐PEG‐water system can be easily formed. The critical concentration of phase separation was affected by the molecular weight of PEG. The aqueous two‐phase polymerization of acrylamide (AAm) has been successfully carried out in the presence of PEG by using ammonium persulfate (APS) as the initiator. The polymerization behaviors with varying concentration of AAm, initiator and PEG, the polymerization temperature, the molecular weight of PEG, and emulsifier types were investigated. The activation energy of aqueous two‐phase polymerization of AAm was 132.3 kJ/mol. The relationship of initial polymerization rate (R_p0) with APS and AAm concentrations was R_p0 ∝ [APS]^0.72 [AAm]^1.28. © 2008 Wiley Periodicals, Inc. J Appl Polym Sci, 2009     

Partitioning of α-lactalbumin and β-lactoglobulin from cheese whey in aqueous two-phase systems containing poly (ethylene glycol) and sodium polyacrylate

Partitioning behavior of the whey proteins α-lactalbumin (α-la) and β-lactoglobulin (β-lg) in aqueous two-phase systems prepared with poly ethylene glycol (PEG) and sodium polyacrilate (NaPA) was investigated as a function of pH and polymer concentrations. It was observed that α-la concentrated in the PEG phase while β-lg concentrated in the NaPA phase. Response surface methodology was applied to optimize protein partitioning and to achieve the best conditions for their fractionation. Thermodynamic analysis based on isothermal titration microcalorimetry indicated that the partitioning of α-la was accompanied by endothermic heat and was entropically driven, while β-lg partitioning was accompanied by exothermic heat and was enthalpically driven at low polymer concentrations and entropically driven at high polymer concentrations. Purification and yield parameters were determined using fresh whey and the results allowed for conclusion of the great applicability of this new system for α-la and β-lg fractionation.     

Synthesis and aggregation behavior of four types of different shaped PCL‐PEG block copolymers

Biodegradable, amphiphilic, linear (diblock and triblock) and star‐shaped (three‐armed and four‐armed) poly[(ethylene glycol)‐block‐(ε‐caprolactone)] copolymers (PEG–PCL copolymers) were synthesized by ring‐opening polymerization of ε‐caprolactone (CL) with stannous octoate as a catalyst, in the presence of monomethoxypoly(ethylene glycol) (MPEG), poly(ethylene glycol) (PEG), three‐armed poly(ethylene glycol) (3‐arm PEG) or four‐armed poly(ethylene glycol) (4‐arm PEG) as an initiator, respectively. The monomer‐to‐initiator ratio was varied to obtain copolymers with various PEG weight fractions in a range 66–86%. The molecular structure and crystallinity of the copolymers, and their aggregation behavior in the aqueous phase, were investigated by employing ¹H‐NMR spectroscopy, gel permeation chromatography and differential scanning calorimetry, as well as utilizing the observational data of gel–sol transitions and aggregates in aqueous solutions. The aggregates of the PEG–PCL block copolymers were prepared by directly dissolving them in water or by employing precipitation/solvent evaporation technique. The enthalpy of fusion (ΔH_m), enthalpy of crystallization (ΔH_crys) and degrees of crystallinity (χ_c) of PEG blocks in copolymers and the copolymer aggregates in aqueous solutions were influenced by their PEG weight fractions and molecular architecture. The gel–sol transition properties of the PEG–PCL block copolymers were related to their concentrations, composition and molecular architecture. Copyright © 2006 Society of Chemical Industry     

双水相萃取法应用于从白萝卜中快速提取过氧化物酶

基于双水相萃取法在化工分离上的优点,研究了其应用于从白萝卜中快速提取过氧化物酶的可行性。结果表明,相对于传统盐析法,应用聚乙二醇/硫酸铵双水相萃取法从白萝卜中提取过氧化物酶具有快速、操作简单、提取率高、成本低及可以使生产规模化等优点。本研究对于过氧化物酶制剂的工业化生产或开发利用白萝卜等具有重要意义。     

双水相萃取在乳酸钙精制中的应用研究

研究了在聚乙二醇(PEG)-磷酸盐双水相体系中PEG分子量、PEG浓度等因素在萃取精制乳酸钙时对分配系数及提取率的影响，并得到较好的双水相萃取条件。结果表明，双水相萃取方法提取乳酸钙能有效去除乳酸钙中的蛋白质、葡萄糖、有机酸杂质，大大提高乳酸钙成品质量。