Bioprocess intensification: a potential aqueous two-phase process for the primary recovery of B-phycoerythrin from Porphyridium cruentum

A process for the primary recovery of B-phycoerythrin from Porphyridium cruentum exploiting aqueous two-phase systems (ATPS) 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 poly(ethylene glycol) (PEG) molecular mass, concentration of PEG as well as salt, system pH and volume ratio was carried out to determine under which conditions the B-phycoerythrin and contaminants concentrate to opposite phases. PEG 1450-phosphate ATPS proved to be suitable for the recovery of B-phycoerythrin because the target protein concentrated to the top phase whilst the protein contaminants and cell debris concentrated in the bottom phase. An extraction ATPS stage comprising volume ratio (Vr) equal to 1.0, PEG 1450 24.9% (w/w), phosphate 12.6% (w/w) and system pH of 8.0 allowed B-phycoerythrin recovery with a purity of 2.9 (estimated as the relation of the 545-280 nm absorbances). The use of ATPS resulted in a primary recovery process that produced a protein purity of 2.9 +/- 0.2 and an overall product yield of 77.0% (w/w). The results reported demonstrated the practical implementation of ATPS for the design of a primary recovery process as a first step for the commercial purification of B-phycoerythrin produced by P. cruentum.     

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.     

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.     

Potential Aqueous Two‐Phase Processes for the Primary Recovery of Colored Protein from Microbial Origin

The primary recovery of c‐phycocyanin and b‐phycoerythrin from Spirulina maxima and Porphyridium cruentum, respectively, using an established extraction strategy was selected as a practical model system to study the generic application of polyethylene glycol (PEG)‐phosphate aqueous two‐phase systems (ATPS). The generic practical implementation of ATPS extraction was evaluated for the recovery of colored proteins from microbial origin. A comparison of the influence of system parameters, such as PEG molecular mass, concentration of PEG as well as salt, system pH and volume ratio, on the partition behavior of c‐phycocyanin and b‐phycoerythrin was carried out to determine under which conditions target colored protein and contaminants concentrate to opposite phases. One‐stage processes are proposed for the primary recovery of the colored proteins. PEG1450‐phosphate ATPS extraction (volume ratio (V_R) equal to 0.3, tie‐line length (TLL) of 34 % w/w and system pH 7.0) for the recovery of c‐phycocyanin from Spirulina maxima resulted in a primary recovery process that produced a protein purity of 2.1 ± 0.2 (defined as the relationship of 620 nm to 280 nm absorbance) and a product yield of 98 % [w/w]. PEG1000‐phosphate ATPS extraction (i.e., V_R = 1.0, PEG 1000, TLL 50 % w/w and system pH 7.0) was preferred for the recovery of b‐phycoerythrin from Porphyridium cruentum, which resulted in a protein purity of 2.8 ± 0.2 (defined as the relationship of 545 nm to 280 nm absorbance) and a product yield of 82 % [w/w]. The purity of c‐phycocyanin and b‐phycoerythrin from the crude extract increased 3‐ and 4‐fold, respectively, after ATPS. The results reported herein demonstrated the benefits of the practical generic application of ATPS for the primary recovery of colored proteins from microbial origin as a first step for the development of purification processes.     

Simplified two-stage method to B-phycoerythrin recovery from Porphyridium cruentum

A simplified two-stage method for B-phycoerythrin (BPE) recovery from Porphyridium cruentum was developed. The proposed method involved cell disruption by sonication and primary recovery by aqueous two-phase partition. The evaluation of two different methods of cell disruption and the effect of increasing concentration of cell homogenate from P. cruentum culture upon aqueous two-phase systems (ATPS) performance was carried out to avoid the use of precipitation stages. Cell disruption by sonication proved to be superior over manual maceration since a five time increase in the concentration of B-phycoerythrin release was achieved. An increase in the concentration of crude extract from disrupted P. cruentum cells loaded to the ATPS (from 10 to 40%, w/w) proved to be suitable to increase the product purity and benefited the processing of highly concentrated disrupted extract. Kinetics studies of phase separation performed suggested the use of batch settlers with height/diameter (H/D) ratio less than one to reduce the necessary time for the phases to separate. The proposed ATPS stage comprising of 29% (w/w) polyethylene glycol (PEG) 1000g/mol, 9% (w/w) potassium phosphate, tie-line length (TLL) of 45% (w/w), volume ratio (V(R)) of 4.5, pH 7.0 and 40% (w/w) crude extract loaded in a batch settler with H/D ratio of 0.5 proved to be efficient for the recovery of 90% of B-phycoerythrin at the top PEG-rich phase. The purity of B-phycoerythrin increased up to 4.0 times after the two-stage method. The results reported here demonstrate the potential implementation of a strategy to B-phycoerythrin recovery with a purity of 3.2 (estimated by the absorbance relation of 545-280nm) from P. cruentum.     

The potential application of aqueous two-phase systems for in situ recovery of 6-pentyl-infinity-pyrone produced by Trichoderma harzianum

Commercial production of aroma compounds by de novo microbial biosynthesis has been principally limited by the low productivity so far achieved. Production of 6-pentyl-alpha-pyrone (6PP), a coconut-like aroma compound, by Trichoderma harzianum has been limited by the toxic effect that occurs even at low concentration (<100 ppm). This work evaluated the feasibility of the use of aqueous-two phase systems (ATPS), as in situ extraction systems, in order to overcome the toxic effects of 6PP and to improve culture productivity. The partition behaviour of 6-pentyl-alpha-pyrone and Trichoderma harzianum mycelium in polyethylene glycol (PEG)-salt and PEG-dextran two-phase systems was investigated and it is reported for the first time. The evaluation of system parameters such as PEG molecular mass, concentration of PEG as well as salt, volume ratio (Vr) and dextran molecular mass, was carried out to determine under which conditions the 6PP partitions to the opposite phase that mycelium does. PEG-dextran systems proved to be unsuitable for the in situ recovery of 6PP because either 6PP and biomass partitioned to the same phase or a large extraction phase was required for the process. ATPS extraction comprising Vr = 0.26, PEG 1450 (7.2% w/w) and sulphate (16.6% w/w) provided the best conditions for the maximum accumulation of the biomass into the bottom phase and concentrated the 6PP in the opposite phase (i.e. 86% of biomass and 56% of 6PP of the total amount loaded from the fermentation extract into the ATPS) for ex situ bioseparation. However, this system caused complete inhibition of the growth of the microorganism during the in situ bioseparation, probably as a consequence of the high ionic strength resulting from the salt concentration. Consequently, two ATPS PEG 8000-sulphate (12%/7% and 6%/14%) were evaluated and proved to be more suitable in the potential application for the in situ recovery of 6PP.     

Recovery of laccase from the residual compost of Agaricus bisporus in aqueous two-phase systems

The potential use of aqueous two-phase systems (ATPS) to establish a viable protocol for the recovery of laccase from the residual compost of Agaricus bisporus was evaluated. The evaluation of system parameters such as poly (ethylene glycol) (PEG) molecular mass, concentration of PEG as well as salt and system pH was carried out to determine under which conditions the laccase concentrates predominantly to the top PEG-rich phase. PEG 1000–phosphate ATPS proved to be suitable for the primary recovery of laccase. An extraction ATPS stage comprising volume ratio equal to 1.0, PEG 1000 18.2% (w/w), phosphate 15.0% (w/w), system pH of 7.0 and loaded with 5% (w/w) of crude extract from residual compost allowed the laccase recovery. The use of ATPS resulted in one-single primary recovery stage process that produced an overall yield of 95%. The results reported here demonstrated the potential application of ATPS for the valorisation of residual material and the potential establishment of a downstream process to obtain value added products with commercial application.     

Downstream processing of human antibodies integrating an extraction capture step and cation exchange chromatography

In this paper we explore an alternative process for the purification of human antibodies from a Chinese hamster ovary (CHO) cell supernatant comprising a ligand-enhanced extraction capture step and cation exchange chromatography (CEX). The extraction of human antibodies was performed in an aqueous two-phase system (ATPS) composed of dextran and polyethylene glycol (PEG), in which the terminal hydroxyl groups of the PEG molecule were modified with an amino acid mimetic ligand in order to enhance the partition of the antibodies to the PEG-rich phase. This capture step was optimized using a design of experiments and a central composite design allowed the determination of the conditions that favor the partition of the antibodies to the phase containing the PEG diglutaric acid (PEG-GA) polymer, in terms of system composition. Accordingly, higher recovery yields were obtained for higher concentrations of PEG-GA and lower concentrations of dextran. The highest yield experimentally obtained was observed for an ATPS composed of 5.17% (w/w) dextran and 8% (w/w) PEG-GA. Higher purities were however predicted for higher concentrations of both polymers. A compromise between yield and purity was achieved using 5% dextran and 10% PEG-GA, which allowed the recovery of 82% of the antibodies with a protein purity of 96% and a total purity of 63%, determined by size-exclusion chromatography. ATPS top phases were further purified by cation exchange chromatography and it was observed that the most adequate cation exchange ligand was carboxymethyl, as the sulfopropyl ligand induced the formation of multi-aggregates or denatured forms. This column allowed the elution of 89% of the antibodies present in the top phase, with a protein purity of 100% and a total purity of 91%. The overall process containing a ligand-enhanced extraction step and a cation exchange chromatography step had an overall yield of 73%.     

Technical improvement in the purification of enzymes from red algae using an aqueous two-phase partitioning system

The effective elimination of phycobiliproteins from crude enzyme preparation of the red alga Caloglossa continua (Okamura) King et Puttock (Ceramiales, Florideophyceae) was investigated in an aqueous two‐phase partitioning system (ATPS) by changing the concentrations of polyethylene glycol (PEG) and ammonium sulfate (AS). The phycobiliproteins shifted from the AS‐rich lower phase to the PEG‐rich upper phase in high PEG and AS concentrations. The best ATPS condition for the elimination of phycobiliproteins from the lower phase was obtained by the combination of 20% (weight/volume; w/v) PEG and 16% (w/v) AS. However, the recovery of aldolase and mannitol‐1‐phos‐phatase activities was significantly reduced. For purification of the enzymes, a combination of 15% (w/v) PEG and 16% (w/v) AS was the best ATPS condition, because a high specific activity and recovery of the enzymes were obtained. Under these conditions, 98% of the phycobiliproteins were removed from the lower phase. Therefore, the ATPS proved to be a very useful method as a first step in the purification of enzymes from red algae.     

Application of a PEG/salt aqueous two-phase partition system for the recovery of monoclonal antibodies from unclarified transgenic tobacco extract

Aqueous two-phase partition systems (ATPS) have been widely used for the separation of a large variety of biomolecules. In the present report, the application of a polyethylene glycol/phosphate (PEG/phosphate) ATPS for the separation of anti-HIV monoclonal antibodies 2G12 (mAb 2G12) and 4E10 (mAb 4E10) from unclarified transgenic tobacco crude extract was investigated. Optimal conditions that favor opposite phase partitioning of plant debris/mAb as well as high recovery and purification were found to be 13.1% w/w (PEG 1500), 12.5% w/w (phosphate) at pH 5 with a phase ratio of 1.3 and 8.25% w/w unclarified tobacco extract load. Under these conditions, mAb 2G12 and mAb 4E10 were partitioned at the bottom phosphate phase with 85 and 84% yield and 2.4- and 2.1-fold purification, respectively. The proposed ATPS was successfully integrated in an affinity-based purification protocol, using Protein A, yielding antibodies of high purity and yield. In this study, ATPS was shown to be suitable for initial protein recovery and partial purification of mAb from unclarified transgenic tobacco crude extract.     

Optimisation of aqueous two-phase extraction of human antibodies

The purification of human antibodies in an aqueous two-phase system (ATPS) composed of polyethylene glycol (PEG) 6000 and phosphate was optimised by surface response methodology. A central composite design was used to evaluate the influence of phosphate, PEG and NaCl concentration and of the pH on the purity and extraction yield of IgG from a simulated serum medium. The conditions that maximise the partition of IgG into the upper phase were determined to be high concentrations of NaCl and PEG, low concentrations of phosphate and low pH values. An ATPS composed of 12% PEG, 10% phosphate, 15% NaCl at pH 6 was further used to purify human monoclonal antibodies from a Chinese Hamster Ovary (CHO) concentrated cell culture supernatant with a recovery yield of 88% in the upper PEG-rich phase and a purification factor of 4.3. This ATPS was also successfully used to purify antibodies from a hybridoma cell culture supernatant with a recovery yield of 90% and a purification factor of 4.1.     

Application of TMA-PEG to promote C-phycocyanin extraction from S. platensis in the PEG ATPS

A novel aqueous two phase system (ATPS) using trimethylamine-polyethylene glycols (TMA-PEG) to promote the extraction of C-phycocyanin (C-PC) from S.platensis was introduced. The purity of C-PC (EP) obtained in the ATPS of PEG1000/Na₃PO₄ was increased 2.1 times by the addition of TMA-PEG1000. The purification factor was enhanced from 2.9 to 10.1 when 65% TMA-PEG1000 was added in the system. The ATPS operation must be carried out in the pH range of 6.0-7.0 and at temperatures less than 35 °C for maintaining the stability of C-PC. The partition coefficient and recovery ratio of C-PC increased with the increasing concentration of TMA-PEG. The system parameters like TMA-PEG1000 content, tie line length (TLL), pH, temperature and phase volume ratio (V_r) were screened and optimized using the fractional factorial design and Box-Behnken experiment design. The optimized system is composed of 11.8% PEG1000/TMA-PEG1000 (w/w), 64.42% TMA-PEG1000 (w/w PEG1000) and 9.5% Na₃PO₄ (w/w) with 38.19% TLL (w/w) and 0.89 V_r at pH 6.5 and 25 °C. The obtained value of EP was 5.21 in one-stage ATPS and 6.7 in two-stage ATPS. The recovery ratio of C-PC in the new ATPS extraction system was more than 97%.     

Affinity separation by protein conjugated IgG in aqueous two-phase systems using horseradish peroxidase as a ligand carrier

A novel affinity separation method in an aqueous two-phase system (ATPS) is suggested, using protein conjugated IgG as a ligand. For verification of the proposed approach, horseradish peroxidase (HRP) and human IgG was used as a ligand carrier and affinity ligand, respectively. The partition of the affinity ligand, human IgG, was controlled by the conjugation of HRP. Two ATPSs, one consisting of potassium phosphate (15%, w/w) and polyethylene glycol (PEG, M.W. 1450, 10%, w/w) and the other of dextran T500 (5%, w/w) and PEG (M.W. 8000, 5%, w/w), were used. The conjugated human IgG-HRP favored a PEG-rich top phase, whereas human IgG, rabbit anti-human IgG and goat anti-mouse IgG preferred a salt or dextran-rich bottom phase. Using the conjugated human IgG-HRP, rabbit anti-human IgG was successfully separated into a PEG-rich top phase from the mixture with goat anti-mouse IgG. The appropriate molar ratio between human IgG-HRP and rabbit anti-human IgG was around 3:1 and 1:1 for the salt and dextran-based ATPS, respectively. The dextran-based ATPS showed a better recovery yield and purity than the salt-based ATPS for the range of test conditions employed in this experiment. The yield and purity of the recovered rabbit anti-human IgG were 90.8 and 87.7%, respectively, in the dextran-based ATPS, while those in the salt-based ATPS were 78.2 and 73.2%.     

Isolation of plasmid DNA from cell lysates by aqueous two-phase systems

This work presents a study of the partitioning of a plasmid vector containing the cystic fibrosis gene in polyethylene glycol (PEG)/salt (K2HPO4) aqueous two-phase systems (ATPS). The plasmid was extracted from neutralized alkaline lysates using PEG with molecular weights varying from 200 to 8000. The effects of the lysate mass loaded to the ATPS (20, 40, and 60% w/w) and of the plasmid concentration in the lysate were evaluated. The performance of the process was determined by qualitative and quantitative assays, carefully established to overcome the strong interference of impurities (protein, genomic DNA, RNA), salt, and PEG. Plasmid DNA partitioned to the top phase when PEG molecular weight was lower than 400. The bottom phase was preferred when higher PEG molecular weights were used. Aqueous two-phase systems with PEG 300, 600, and 1000 were chosen for further studies on the basis of plasmid and RNA agarose gel analysis and protein quantitation. The recovery yields were found to be proportional to the plasmid concentration in the lysate. The best yields (>67%) were obtained with PEG 1000. These systems (with 40 and 60% w/w of lysate load) were able to separate the plasmid from proteins and genomic DNA, but copartitioning of RNA with the plasmid was observed. Aqueous two-phase systems with PEG 300 concentrated both plasmid and proteins in the top phase. The best system for plasmid purification used PEG 600 with a 40% (w/w) lysate load. In this system, RNA was found mostly in the interphase, proteins were not detected in the plasmid bottom phase and genomic DNA was reduced 7.5-fold.     

Purification and in situ immobilization of lipase from of a mutant of Trichosporon laibacchii using aqueous two-phase systems

The crude intracellular lipase (cell homogenate) from Trichosporon laibacchii was subjected to partial purification by aqueous two-phase system (ATPS) and then in situ immobilization by directly adding diatomites as carrier to the top PEG-rich phase of ATPS. A partition study of lipase in the ATPS formed by polyethylene glycol–potassium phosphate has been performed. The influence of system parameters such as molecular weight of PEG, system phase composition and system pH on the partitioning behaviour of lipase was evaluated. The ATPS consisting of PEG 4000 (12%) and potassium phosphate (K₂HPO₄, 13%) resulted in partition of lipase to the PEG-rich phase with partition coefficient 7.61, activity recovery 80.4%, and purification factor of 5.84 at pH of 7.0 and 2.0% NaCl. Moreover, the in situ immobilization of lipase in PEG phase resulted in a highest immobilized lipase activity of 1114.6 U g^?1. The above results show that this novel lipase immobilization procedure which couples ATPS extract and enzyme immobilization is cost-effective as well as time-saving. It could be potentially useful technique for the purification and immobilization of lipase.     

Downstream processing of luciferase from fireflies (Photinus pyralis) using aqueous two-phase extraction

The firefly luciferase has been extensively used for sensitive detection of bacteria, gene expression and environmental toxins (biosensors). The aim of the present study was to design a simple and more efficient method for the purification and concentration of luciferase using aqueous two-phase extraction (ATPE). Downstream processing of luciferase from North American Firefly Photinus pyralis was carried out, for the first time, using polymer/salt aqueous two phase system (ATPS) at 4 °C. The enzyme was observed to preferentially partition to the polyethylene glycol (PEG) rich top phase. The best results of purification (13.69 fold) and enzyme activity recovery (118.34%) were observed in the system containing 4.0% (w/w) PEG (1500) and 20.5% (w/w) (NH₄)₂SO₄ with a phase volume ratio of 0.21.     

Partitioning studies of α-lactalbumin in environmental friendly poly (ethylene glycol)—citrate salt aqueous two phase systems

Aqueous two-phase systems (ATPS) formed by polymer and salt have been utilized to enrich the desired biomolecule into one of the phase with higher yield and purity. The eco-friendly, biodegradable poly ethylene glycol (PEG) and different citrate salts were chosen as ATPS phase components to investigate the partitioning behavior of α-lactalbumin (α-La). System factors and process parameters such as type and concentration of salt, molecular weight and concentration of PEG, pH, temperature and the effect of additives were studied and the results are discussed in detail. PEG 1000–tri-potassium citrate system yields high partition coefficient of 20 with a better yield of 98 % in the top phase. The addition of NaCl as an additive and acidic pH lowers the yield of α-La in the top phase. Influence of phase volume ratio (V _r) on partitioning was studied and found that the partition coefficient remains almost constant along the tie line. High yield was achieved at a V _r of 3.5 at the tie line length of 50.63 (%, w/w).     

Partition behavior of CD133+ stem cells from human umbilical cord blood in aqueous two‐phase systems: In route to establish novel stem cell primary recovery strategies

Aqueous two‐phase systems (ATPS) represent a promising strategy for the recovery of CD133⁺ stem cells. This particular type of stem cells has great potential for research and clinical applications. Traditional [polyethylene glycol (PEG), dextran (DEX), and ficoll] and novel (Ucon) polymer–polymer ATPS were exploited to study the partitioning behavior of CD133⁺ stem cells and contaminants from human umbilical cord blood (HUCB). The aim of the study was to select conditions under which the product of interest and the contaminants concentrate in opposite phases. To accomplish this, three independent samples were tested: (1) enriched CD133⁺ sample, (2) whole HUCB (contaminants), and (3) complex sample (CD133⁺ stem cells and contaminants). The objective of this research was to evaluate the partition behavior of CD133⁺ in ATPS in route to establish the basis for the development of a novel and scalable purification bioprocess. In conclusion, the partitioning behavior of CD133⁺ stem cells and contaminants from complex samples was as follows: 59% of CD133⁺ stem cells fractionated to the top phase when employing ficoll 400,000–DEX 70,000 or 100% to the bottom phase with Ucon‐DEX 75,000 and PEG 8,000‐DEX 500,000 ATPS. In average, 35% of the contaminants partitioned to the top phase of the ficoll 400,000‐DEX 70,000 ATPS, 99% to the dextran rich phase of the Ucon‐DEX 75,000 systems and 97% to the bottom phase of the PEG 8,000‐DEX 500,000. Cell viability was at least 98% after ATPS recovery. © 2014 American Institute of Chemical Engineers Biotechnol. Prog., 30:700–707, 2014     

Downstream antibody purification using aqueous two‐phase extraction

The extraction of antibodies using a polyethylene glycol (PEG)‐citrate aqueous two‐phase system (ATPS) was investigated. Studies using purified monoclonal antibody (mAb) identified operating ranges for successful phase formation and factors that significantly affected antibody partitioning. The separation of antibody and host cell protein (HCP) from clarified cell culture media was examined using statistical design of experiments (DOE). The partitioning of antibody was nearly complete over the entire range of the operating space examined. A model of the HCP partitioning was generated in which both NaCl and citrate concentrations were identified as significant factors. To achieve the highest purity, the partitioning of HCP from cell culture fluid into the product containing phase was minimized using a Steepest Descent algorithm. An optimal ATPS consisting of 14.0% (w/w) PEG, 8.4% (w/w) citrate, and 7.2% (w/w) NaCl at pH 7.2 resulted in a product yield of 89%, an approximate 7.6‐fold reduction in HCP levels relative to the clarified cell culture fluid before extraction and an overall purity of 70%. A system consisting of 15% (w/w) PEG, 8% (w/w) citrate, and 15% (w/w) NaCl at pH 5.5 reduced product‐related impurities (aggregates and low molecular product fragments) from ～40% to less than 0.5% while achieving 95% product recovery. At the experimental conditions that were optimized in the batch mode, a scale‐up model for the use of counter‐current extraction technology was developed to identify potential improvements in purity and recovery that could be realized in the continuous operational mode. © 2010 American Institute of Chemical Engineers Biotechnol. Prog., 2010     

Potential of Aqueous Two-Phase Systems constructed on flexible devices: Human serum albumin as proof of concept

In the present research, the potential use of flexible disposable devices, specifically blood bags, for the fractionation of biological products using Aqueous Two-Phase Systems (ATPS) polymer–salt is studied and demonstrated. Purified human serum albumin (HSA) was used as model protein. Experiments were carried out on ATPS polyethylene glycol (PEG)–potassium phosphate constructed on rigid recipients (conical tubes) and flexible devices (blood bags). The device used for ATPS construction had no significant effect on HSA partition behavior. Protein partition towards the top phase was favored on systems constructed using PEG 1000 g/mol and TLL 45% (w/w), achieving up to 85% recovery. On the other hand a recovery of 92% was achieved at the bottom phase when PEG 3350 g/mol and TLL 25% (w/w) were used. Human serum was used as a complex sample on ATPS experiments. Selective fractionation of human serum proteins on ATPS constructed on flexible devices was achieved. ATPS constructed on blood bags required short equilibrium times (< 6 min), meaning it is feasible to use this approach on mass scale. The potential use of flexible disposable devices, for the fractionation of biological products using ATPS polymer–salt was demonstrated.