Potential application of aqueous two‐phase systems for the fractionation of RNase A and α‐Lactalbumin from their PEGylated conjugates

BACKGROUND: PEGylation reactions often result in a heterogeneous population of conjugated species and unmodified proteins that presents a protein separations challenge. Aqueous two‐phase systems (ATPS) are an attractive alternative for the potential fractionation of native proteins from their PEGylated conjugates. The present study characterizes the partition behaviors of native RNase A and α‐Lac and their mono and di‐PEGylated conjugates on polyethylene glycol (PEG)—potassium phosphate ATPS. RESULTS: A potential strategy to separate unreacted native protein from its PEGylated species was established based upon the partition behavior of the species. The effect of PEG molecular weight (400–8000 g mol^?1), tie‐line length (15–45% w/w) and volume ratio (V_R; 0.33, 1.00 and 3.00) on native and PEGylated proteins partition behavior was studied. The use of ATPS constructed with high PEG molecular weight (8000 g mol^?1), tie‐line lengths of 25 and 35% w/w, and V_R values of 1.0 and 3.0 allowed the selective fractionation of native RNase A and α‐Lactalbumin, respectively, from their PEGylated conjugates on opposite phases. Such conditions resulted in an RNase A bottom phase recovery of 99%, while 98% and 88% of mono and di‐PEGylated conjugates, respectively were recovered at the top phase. For its part, α‐Lac had a bottom phase recovery of 92% while its mono and di‐PEGylated conjugates were recovered at the top phase with yields of 77% and 76%, respectively. CONCLUSIONS: The results reported here demonstrate the potential application of ATPS for the fractionation of PEGylated conjugates from their unreacted precursors. Copyright © 2010 Society of Chemical Industry     

Kinetic study on biphasic recognition chiral extraction for separation of α‐cyclohexyl‐mandelic acid enantiomers

BACKGROUND: Chiral solvent extraction is a potentially attractive chiral separation technique. It is essential to know the intrinsic complexation kinetics for selection, design and operation of reactive extraction equipment and for reliable scale‐up. The objective of this research is to study the kinetics of biphasic recognition chiral extraction of α‐cyclohexyl‐mandelic acid (α‐CHMA) enantiomers using a modified Lewis cell. RESULTS: The experimental results demonstrate that the extraction reaction kinetics is fast, and the reactions are first order with respect to α‐CHMA and second order with respect to D‐IBTA, with forward rate constants of 6.54 × 10^?4 mol^?2 m⁶ s^?1 for S‐α‐CHMA and 6.84 × 10^?4 mol^?2 m⁶ s^?1 for R‐α‐CHMA. With increase of HP‐β‐CD concentration in aqueous phase, enantioselectivity increases, while the overall mass transfer coefficients decrease. CONCLUSIONS: Sufficient enantioselectivity and fast kinetics of extraction can be obtained in the BRCE system at HP‐β‐CD concentration of 0.1 mol L^?1 and D‐IBTA concentration of 0.2 mol L^?1. These data will be useful in the design of extraction processes. Copyright © 2012 Society of Chemical Industry     

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     

Flowsheet simulation of aqueous two‐phase extraction systems for protein purification

BACKGROUND: Aqueous two‐phase extraction (ATPE) has many advantages as an efficient, inexpensive large‐scale liquid–liquid extraction technique for protein separation. However, the realization of ATPE as a protein separation technology at industrial scales is rather limited due to the large, multidimensional design space and the paucity of design approaches to predict phase and product behavior in an integrated fashion with overall system performance. This paper describes a framework designed to calculate suitable flowsheets for the extraction of a target protein from a complex protein feed using ATPE. The framework incorporated a routine to set up flowsheets according to target protein partitioning behavior in specific ATPE systems and a calculation of the amounts of phase‐forming components needed to extract the target protein. The thermodynamics of phase formation and partitioning were modeled using Flory‐Huggins theory and calculated using a Gibbs energy difference minimization approach. RESULTS: As a case study, suitable flowsheets to recover phosphofructokinase from a simple model feedstock using poly(ethylene glycol)‐dextran (PEG6000‐DxT500) and poly(ethylene glycol)‐salt (PEG6000‐Na₃PO₄) two‐phase systems were designed and the existence of feasible solutions was demonstrated. The flowsheets were compared in terms of product yield, product purity, phase settling rate and scaled process cost. The effect of the mass flowrates of phase‐forming components on product yield and purity was also determined. CONCLUSION: This framework is proposed as a basis for flowsheet optimization for protein purification using ATPE systems. Copyright © 2010 Society of Chemical Industry     

Highly Enantioselective Phase‐Transfer Catalytic α‐Alkylation of α‐tert‐Butoxycarbonyllactams: Construction of β‐Quaternary Chiral Pyrrolidine and Piperidine Systems

A new enantioselective α‐alkylation of α‐tert‐butoxycarbonyllactams for the construction of β‐quaternary chiral pyrrolidine and piperidine core systems is reported. α‐Alkylations of N‐methyl‐α‐tert‐butoxycarbonylbutyrolactam and N‐diphenylmethyl‐α‐tert‐butoxycarbonylvalerolactam under phase‐transfer catalytic conditions (solid potassium hydroxide, toluene, −40 °C) in the presence of (S,S)‐3,4,5‐trifluorophenyl‐3,3′,5,5′‐tetrahydro‐2,6‐bis(3,4,5‐trifluorophenyl)‐4,4′‐spirobi[4H‐dinaphth[2,1‐c:1′,2′‐e]azepinium] bromide [(S,S)‐NAS Br] (5 mol%) afforded the corresponding α‐alkyl‐α‐tert‐butoxycarbonyllactams in very high chemical (up to 99%) and optical yields (up to 98% ee). Our new catalytic systems provide attractive synthetic methods for pyrrolidine‐ and piperidine‐based alkaloids and chiral intermediates with β‐quaternary carbon centers.     

Polymerization‐induced bimodal phase separation in a rubber‐modified epoxy system

The bimodal phase separation process of a rubber‐modified epoxy system, consisting of diglycidyl ether of bisphenol A (DGEBA), and a hydroxyl‐terminated butadiene–acrylonitrile random copolymer (HTBN), during curing with tetrahydro‐phthalic anhydride was studied by time‐resolved small‐angle light scattering (TRSALS), differential scanning calorimetry (DSC), and digital image analysis (DIA). The HTBN/DGEBA mixture reveals an upper critical solution temperature (UCST). At higher curing temperatures, double‐peak structure from the matrix was investigated by TRSALS and confirmed by DIA. The special two characteristic size distribution behavior was explained qualitatively by nucleation growth coupled with spinodal decomposition (NGCSD) and the competition between phase separation and polymerization. © 1999 John Wiley & Sons, Inc. J Appl Polym Sci 72: 59–67, 1999     

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     

Kinetic model for simultaneous cell disruption and aqueous two‐phase extraction

A process of simultaneous cell disruption and aqueous two‐phase extraction demonstrated improved product yield and selectivity compared with the traditional process of cell disruption followed by extraction. Addition of aqueous two‐phase components did not decrease the efficiency of cell disruption. Moreover, ADH, LDH and G6PDH recovery was enhanced in this new process with recovery ratios of 97%, 93% and 95%, respectively. Cell disruption kinetics were established based on a new mechanism that was different from traditional first‐order kinetics, consisting of the release of intracellular proteins and enzymes, the denaturation and subsequent renaturation of these proteins that may be due to the protection of the aqueous two‐phase components during the cell disruption process. To account for this, the kinetics parameters were calculated, and the experimental data were regressed. The resulting kinetic model could provide a better fit for the experimental data with a correlation ratio of 99% (for total protein), and led to insights into the differences between the new process and the traditional one. Copyright © 2005 Society of Chemical Industry     

Partitioning of chicken egg white proteins in polyelectrolyte/salt aqueous two‐phase systems composed of polyethyleneoxide–maleic acid copolymer and potassium phosphate

Aqueous two‐phase systems were formed from solutions of a polyelectrolyte, polyethyleneoxide–maleic acid copolymer, and potassium phosphate. The properties of such aqueous two‐phase systems were highly dependent on pH. This was reflected in the partition behavior of three chicken egg white proteins: lysozyme, conalbumin and ovalbumin. Separability of these three proteins was improved by the use of the polyelectrolyte, in comparison with when uncharged polyethylene glycol (poly(1,2‐dihydroxyethane)) was used as a phase‐forming polymer. © 2002 Society of Chemical Industry     

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     

The temperature‐dependent surface energy of ceramic single crystals

Knowledge of the surface energy of ceramic single crystals at elevated temperatures is of fundamental importance. However, it is very hard to obtain this quantity from the existing experiments, simulations, and theories. In the present work, following the Orowan‐Polanyi and Gilman models’ principles, two theoretical models for the temperature‐dependent surface energy of the ceramic single crystals are proposed based on the authors’ previous studies on the temperature‐dependent ideal tensile strength of solids. Thus established models relate the temperature dependence of the surface energy to these of the specific heat at constant pressure, Young's modulus, and coefficient of the linear thermal expansion. The temperature‐dependent surface energies of α‐Al₂O₃ and β‐Si₃N₄ are calculated and agree well with the experimental data. The study shows that the surface energy firstly remains approximately constant and then decreases linearly as temperature increases from 0 K to melting point. However, it has stronger temperature dependence than Young's modulus, that is, surface energy decreases more rapidly with increasing temperature.     

Novel approach for neuronal stem cell differentiation using aqueous two‐phase systems in 3D cultures

Stem cell therapy has emerged as a promising alternative for replacing lost cells involved in neurodegenerative diseases. High efficiency of differentiation and full cell viability are actual challenges to achieve the translation of cell therapies to the clinic. To address this, the construction of aqueous two‐phase systems in three‐dimensional (ATPS‐3D) cultures has been proposed. This technique involves the combination of two polymers in which cells are confined in dextran droplets immersed over a substrate located in a poly(ethylene glycol) phase. The controlled placement of cells in a defined pattern promotes intercellular communication. This review aims to provide insight into the techniques used to enhance neural differentiation and current challenges to achieve the implementation of cell therapies. Cell density, colony size, interconnectivity and an appropriate substrate to modulate paracrine signaling are factors that determine neural differentiation efficiency during the construction of ATPS‐3D cultures. Hence, this contact‐free technique enables the design of neural niches to recapitulate in vivo environments more accurately. © 2020 Society of Chemical Industry (SCI)