Physical characterisations of a single-stage Kühni-type aqueous two-phase extraction column

The main parameters which influence the behaviour of phase separation in a single-stage Kühni-type aqueous two-phase extraction column containing polyethylene (PEG) and di-potassium hydrogen phosphate were characterised. Two aqueous two-phase system (ATPS) composed of 12% (w/w) PEG 1450 and 12% (w/w) di-potassium hydrogen phosphate (designated as 12/12) and 12% (w/w) PEG 1450 and 11% (w/w) di-potassium hydrogen phosphate (designated as 12/11) were chosen in this study. The hold-up ɛ_D increased with increasing impeller speeds and mobile phase flow rates. Phase separation for the 12/11 system was slower than that for the 12/12 system, which resulted in higher dispersed phase hold-up values for the 12/11 system. For 12/12 system, mass transfer of plasmid DNA (pDNA) from the dispersed mobile phase to the stationary phase increased rapidly with increasing impeller speeds of 130, 160 and 200 rpm which was reflected in the decreased values for C_T/C_To. The degree of back-mixing quantified by the axial dispersion coefficient D_ax was estimated to be 2.7 × 10⁻⁶ m² s⁻¹.     

Partitioning of protease from stomach of albacore tuna (Thunnus alalunga) by aqueous two-phase systems

Partitioning of protease from stomach of albacore tuna using an aqueous two-phase system (ATPS) was investigated. The best ATPS conditions for protease partitioning from stomach extract (SE) and acidified counterpart (ASE) were 25% PEG1000–20% MgSO₄ and 15% PEG2000–15% MgSO₄, which increased the purity by 7.2-fold and 2.4-fold with the recovered activity of 85.7% and 89.1%, respectively. Electrophoretic study revealed that SE had a major protein with a molecular weight (MW) of 40.6 kDa, while protein with MW of 32.7 kDa was predominant in ASE and ATPS fractions. Pepsinogen in SE might be activated to pepsin by acidification and partitioning process. SE was quite stable at 0 and 4 °C up to 14 days. The loss in protease activity in ASE and selected ATPS fractions was more pronounced when storage time and temperature increased. Therefore, ATPS can be effectively used to recover and purify protease from albacore tuna stomach.     

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.     

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.     

Two phase partitioning and collagen hydrolysis of bromelain from pineapple peel Nang Lae cultivar

Extraction of bromelain from pineapple peel (Nang Lae cultv.) using aqueous two phase system (ATPS) was optimized. Some biochemical properties including collagen hydrolysis were also investigated. Bromelain predominantly partitioned to the polyethylene glycol (PEG)-rich phase. The highest enzyme activity recovery (113.54%) and purification fold (2.23) were presented in the top phase of 15% PEG2000–14% MgSO₄. Protein pattern and activity staining showed the molecular weight (MW) of bromelain to be about 29 kDa. The extracted bromelain showed the highest relative activity at pH 7.0 and 55 °C. Its activity was decreased continuously by increasing NaCl concentration (up to 1.5% (w/v)). The bromelain extract was applied to hydrolyze the skin collagen of beef and giant catfish (0–0.3 units). The β, α₁, α₂ of giant catfish skin collagen extensively degraded into small peptides when treated with 0.02 units of the bromelain extract. Bovine collagen was hydrolyzed using higher bromelain up to 0.18 units. This study showed the ATPS can be employed to partially purify bromelain from Nang Lae pineapple peel and the enzyme effectively hydrolyzed the collagens.     

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.     

Two-step process for initial capture of plasmid DNA and partial removal of RNA using aqueous two-phase systems

In this paper, a two-step process for initial capture of plasmid DNA (pDNA) and partial removal of RNA using polyethylene glycol (PEG) and di-potassium hydrogen phosphate aqueous two-phase systems (ATPS) has been investigated. A Kühni-type ATPS extraction column was prepared with 50 ml (12% (w/w) PEG 1450, 12% (w/w) phosphate) of stationary phase and loaded with crude mobile phase (26% (w/w) PEG 1450, 4% (w/w) phosphate and 70% (w/w) lysate) at a flow rate of 6 ml min⁻¹ at an impeller speed of 200 rpm. The experiment was terminated after 100 min, and after complete resettling of the phases, 45 ml of stationary phase was harvested. During a subsequent second extraction step contained 18% (w/w) PEG 300 and 14% (w/w) phosphate, a proportion of RNA, which was also concentrated during the column process, was removed. It was demonstrated that the recovery of pDNA in the second bottom phase was 89.4%, which was similar to the initial recovery after column extraction (92.1%).     

Evaluation of recombinant phenylalanine dehydrogenase behavior in aqueous two-phase partitioning

Recombinant Bacillus sphaericus phenylalanine dehydrogenase (PheDH) partitioning was studied in polyethylene glycol (PEG) and ammonium sulfate aqueous two-phase systems (ATPS). The objectives of this work were to investigate influences; varying the molecular mass and concentration of PEG, pH, phase volume ratio (V_R), tie-line length (TLL) and concentration of (NH₄)₂SO₄ on the partition behavior of PheDH. It was revealed that the partitioning was not affected by V_R, while PEG molecular mass and concentration and (NH₄)₂SO₄ concentration had significant effects on enzyme partitioning. Longer TLL and higher pH resulted in better partitioning into the top phase. Under the most favorable partition conditions with 8.5% (w/w) PEG-6000, 17.5% (w/w) (NH₄)₂SO₄ and V_R = 0.25 at pH 8.0, partition coefficient (K_E), recovery (R%), yield (Y%) and TLL were achieved 58.7%, 135%, 94.42% and 39.89% (w/w), respectively. Overall, the promising results obtained in this research indicated that the ATPS partitioning can be provided an efficient and powerful tool for recovery and purification of recombinant PheDH.     

Extraction of protease from Calotropis procera latex by polyethylene glycol–salts biphasic system

The protease from the latex of Calotropis procera was isolated by an aqueous two-phase system (ATPS). The systems consist of polyethylene glycol (PEG 4000, 6000 and 8000) at concentrations of 9, 12 and 15% (w/w) with salts (Na-citrate, MgSO₄, K₂HPO₄, and (NH₄)₂SO₄) at concentrations of 11, 14 and 17% (w/w) were investigated. The highest protease recovery was found in the PEG-rich phase of the system, comprising of 12% PEG 4000–17% MgSO₄. For optimization of the system to obtain the higher yield of protease, the system pH (4, 7 and 10) or NaCl addition (2, 4 and 6%, w/w) was studied. At acidic (pH 4.0) and alkaline (9.0) conditions of the systems the reduction of K_E and protease recovery was clearly observed compared to that of the neutral pH (7.0). The addition of NaCl up to a final concentration of 6% (w/w) significantly increased the yield to 107% of the control. Molecular weight distribution and activity staining showed that the isolated protease had the molecular weight of ∼38 kDa. However, the isolated protease had no activity under reducing condition (βME). Under cathodic electrophoresis, protease from C. procera showed the same protein pattern to purified papain.     

Aqueous biphasic system for the partial purification of Bacillus subtilis carboxymethyl cellulase

Carboxymethyl cellulase (CMCase) hydrolyses cellulose into glucose and is useful in various industrial applications. Conventional CMCase purification methods are rather complicated and time-consuming; thus, a cost-effective strategy for CMCase recovery is on demand. Polyethylene-glycol (PEG)/sodium citrate aqueous biphasic system (ABS) was adopted in this study to investigate the effectiveness of the ABS in the recovery of extracellular Bacillus subtilis CMCase from fermentation broth. Comprehensive optimization steps were executed that took into consideration the ABS variables of PEG molecular weight, tie-line length (TLL), volume ratio (V_R), crude loading, pH and the addition of sodium chloride (NaCl). A CMCase recovery yield (Y_B) of 88.82% ± 0.69, a purification fold (P_F) of 4.8 and a partition coefficient (K) of 0.44 ± 0.03 were achieved from the bottom phase of the PEG 6000/citrate ABS with TLL of 42.16% (w/w), V_R of 0.29, 1% of (w/w) NaCl, pH 7.0, and 20% (w/w) crude loading. CMCase was mainly segregated to the salt-rich bottom phase because of the hydrophilicity of the enzyme surface. The highly effective recovery technique was further confirmed by SDS-PAGE analysis. Overall, the present study suggests that the ABS is a potential purification strategy for extracellular CMCase.     

Evaluating aqueous two-phase systems for Yarrowia lipolytica extracellular lipase purification

In this study an aqueous two-phase system (ATPS) composed of polyethylene glycol (PEG) and potassium phosphate was tested for the purification of lipase from Yarrowia lipolytica IMUFRJ 50682. Ultrafiltration and precipitation with acetone and kaolin were also used as traditional comparison methods Ultrafiltration was a good method with a purification factor of 6.55, but protease was also purified in this extract. For the precipitation with acetone and kaolin lower values of lipase and protease activity were found in relation to the original crude enzyme extract. Under the best conditions of ATPS (pH 6 and 4 °C), the purification fold was greater than 40 and selectivity was almost 500. Lipase was recovered in the salty phase which makes it easier to purify it. The optimum pH and temperature ranges for purified lipase with this system was 6–7 and 35–40 °C, respectively. Lipase thermostability was increased in relation to crude extract after the purification with the PEG/phosphate buffer system for temperatures lower than 50 °C. All enzyme extracts showed good stability to a wide pH range. Y. lipolytca lipase was successfully purified by using ATPS in a single downstream processing step and presented good process characteristics after this treatment.     

Synthesis and application of two light-sensitive copolymers forming recyclable aqueous two-phase systems

Recycling aqueous two-phase systems (ATPS) are hopeful application techniques in bioseparation and biocatalysis engineering areas. In this study, two novel light-sensitive and reversible water-soluble copolymers were synthesized and used in recycling ATPS. Polymer P_NBAC was polymerized by using N-isopropylacrylamide (NIPA), n-butylmethacrylate (BMA), acrylic acid (AA) and chlorophyllin sodium copper salt (CHL) as monomers. Copolymer P_NDBC was synthesized by NIPA, 2-(dimethylamino) ethylmethacrylate (DMAEMA), BMA and CHL as monomers. The synthesis yields of two copolymers are 66.9% and 77.2%, respectively. It can be calculated from ¹H NMR graph that the molar ratios of monomers in P_NBAC (NIPA:BMA:AA:CHL) and P_NDBC (NIPA:DMAEMA:BMA:CHL) was 82:4:1:10 and 16:4:3:1, respectively. They could be precipitated by laser irradiation in 488 nm with the least light density of 1.70 × 10⁵ W/m². The precipitate energy is 1.79 kJ and 3.52 kJ/g, respectively. Five batches of average recoveries of two copolymers in the ATPS are 96.6% and 97.4%. BSA and l-phenylalanine were partitioned in the novel P_NDBC–P_NBAC ATPS, and their partition coefficients were 2.1 and 0.52. By applying this ATPS to partition of penicillin, the best partition coefficient K is 4.25.     

Lysozyme extraction from hen egg white in an aqueous two-phase system composed of ethylene oxide–propylene oxide thermoseparating copolymer and potassium phosphate

The recovery and purification of lysozyme from hen egg white has been investigated in an aqueous two-phase systems composed of thermoseparating random copolymers of ethylene oxide (EO), propylene oxide (PO) and potassium phosphate. In the primary extraction step lysozyme was satisfactorily partitioned to the top polymer-rich phase in a system composed of 40% (w/w) EO₅₀PO₅₀, 10% (w/w) potassium phosphate, and 0.85 M sodium chloride at pH 9.0, diluted 3-fold with crude egg white, where contaminating proteins were discarded in the bottom phosphate-rich phase. After the primary phase separation the upper EO₅₀PO₅₀ phase was removed and subjected to temperature-induced (65 °C) phase separation, which resulted in the partitioning of pure lysozyme to the top water phase. The separation system was found to be efficient in achieving the purification of lysozyme in a high yield of 85% and specific activity of 32,300 U/mg of protein, with a purification factor of 16.9 and a concentration of lysozyme in the water phase of 2.3 g/l in two extraction steps.     

Purification of plant-esterase in PEG1000/NaH2PO4 aqueous two-phase system by a two-step extraction

Purification of plant-esterase from flour in an aqueous two-phase system (ATPS) was investigated. The effects of various process parameters such as the type of aqueous two-phase systems, the phase-forming salt, the molecular weight and concentration of PEG, the system pH, and the types and concentrations of neutral salts on partitioning of plant-esterase were evaluated. Optimized conditions for the purification of plant-esterase were found in polymer–salt systems, with especially promising results in the PEG1000/NaH₂PO₄ system. Using 27.0% PEG1000/13.0% NaH₂PO₄ (w/w, pH 5.0), and 27.0% PEG1000/13.0% NaH₂PO₄/6.0% (NH₄)₂SO₄ (w/w, pH 5.0), plant-esterase was purified by a two-step extraction. Compared to the results obtained with the conventional salting-out method, this method had a comparable yield (83.16% versus the original yield of 80%), but produced plant-esterase that was 4.8 times as pure (18.46-fold). Integrating dialysis into the aqueous two-phase extraction removed (NH₄)₂SO₄ from the purified plant-esterase. Finally, plant-esterase was freeze-dried to convert the product to powder. This work offers a simple and more efficient process to purify and concentrate plant-esterase. Plant-esterase is used in applications such as organophosphorus compounds (OPs) detection and since our method makes this enzyme easier to isolate, it will enhance researchers’ ability to explore these applications.     

The biliprotein C-phycocyanin modulates the early radiation response: A pilot study

This study analyzed the effects of biliprotein C-phycocyanin (C-PC) on the enzymatic antioxidant defence system in lymphocytes of nuclear power-plant workers and non-exposed controls. Changes in the protein levels of manganese super oxide dismutase (MnSOD), catalase and glutathione-S-transferase (GST) were used as markers for early biological effects of a single in vitro exposure of cells to: (i) 2 Gy gamma rays; (ii) 5 μM C-PC; and (iii) a combination of C-PC plus irradiation with 2 Gy. The results showed that C-PC selectively stimulated the lymphocyte antioxidant defence system of occupationally exposed subjects. The activation of the antioxidant protective mechanisms as part of the early radiation response was probably related to the chronic low-dose occupational exposure. The modulating capacity of C-PC at the molecular level may be of interest for the protection of occupationally exposed persons.     

Scaling-up of a B-phycoerythrin production and purification bioprocess involving aqueous two-phase systems: Practical experiences

One of the most attractive segments in food and cosmetic industries is that of natural pigments. Since some synthetic pigments have been reported to be hazardous for humans, natural pigments obtained through biotechnological processes represent an attractive alternative. Our research group has previously worked on the development of an aqueous two-phase system (ATPS)-based prototype process for the recovery of B-phycoerythrin (BPE), a natural high-value pigment obtained from Porphyridium cruentum. Detailed studies describing the scaling up of ATPS processes from bench scale to pilot plant facilities are not common. In this paper experiences derived from the scale-up of a previously developed process for production and recovery of highly purified (purity defined as the absorbance ratio A₅₄₅/A₂₈₀ > 4) BPE are described, where a scale-up factor of 850× was implemented. Characterization of cell disruption with a pilot-scale bead mill allowed efficient BPE release at 2900 rpm, 10% (w/v) sample load, 60% (v/v) bead load and 0.5 mm glass beads and 22 min of residence time with a yield of 1.35 mg BPE/g of wet biomass. BPE was recovered and purified using a strategy comprising isoelectric precipitation, aqueous two-phase fractionation and ultrafiltration. A 54% global BPE recovery yield, with final purity of 4.1, was achieved under optimal process conditions. Considering total costs for raw materials and energy expenditures for one batch, it was determined that the production cost of BPE was of $1.17 USD/mg, which is underneath the commercial price of a BPE standard (>$30 USD/mg).     

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.     

Production of a key chiral intermediate of Betahistine with a newly isolated Kluyveromyces sp. in an aqueous two-phase system

(S)-(4-Chlorophenyl)-(pyridin-2-yl)methanol [(S)-CPMA] is an important chiral intermediate of anti-allergic drug Betahistine. Carbonyl reductase-producing microorganisms were isolated from soil samples for the stereoselective reduction of (4-chlorophenyl)-(pyridin-2-yl)methanone (CPMK) to (S)-CPMA. Among over 400 microorganisms isolated, one strain exhibiting the highest activity was selected and identified as Kluyveromyces sp. After optimization, the biotransformation reaction catalyzed by Kluyveromyces sp. CCTCC M2011385 whole-cell gave product (S)-CPMA in 81.5% ee and 87.8% yield at substrate concentration of 2 g/L in aqueous phase. Using an aqueous two-phase system (ATPs) consisted of PEG4000 (20%, w/w) and Na₂HPO₄ (14%, w/w), the product reached 86.7% ee and 92.1% yield at a higher substrate concentration of 6 g/L. The substrate tolerance and biocompatibility of microbial cells are greatly improved in ATPs by accumulating substrate/product in the upper PEG solution. This study, for the first time, reports the production of (S)-CPMA catalyzed by microbial cells.     

Separation and purification of laccases from two different fungi using aqueous two-phase extraction

Selective purification still poses a challenge in the downstream processing of biomolecules such as proteins and especially enzymes. In this study a polyethylene glycol 3000 (PEG 3000)–phosphate aqueous two-phase system at 25 °C and pH 7 was successfully used for laccase purification and separation. Initially, the effect of phase forming components on enzyme activities in homogenous systems was studied. In the course of the extraction experiments tie lines, enzyme source, initial enzyme activities, phase ratio and sodium chloride concentrations were varied and their influence on the activity partitioning was determined. Partitioning results were validated using clear-native-PAGE and isoelectric focusing. Based on these results, the separation of laccases from Trametes versicolor and Pleurotus sapidus was investigated using the principle of superposition. Sodium chloride was used to adjust laccase partitioning in the applied aqueous two-phase system (ATPS). Finally, two modes of operation are proposed depending on the aim of the purification task. One mode with 0.133 g g⁻¹ of PEG3000, 0.063 g g⁻¹ of phosphate and without sodium chloride separates P. sapidus laccases from T. versicolor laccases with clearance factors of 5.23 and 6.45, respectively. The other mode of operation with 0.124 g g⁻¹ of PEG3000, 0.063 g g⁻¹ of phosphate and 0.013 g g⁻¹ of sodium chloride enables a partitioning of both laccases into the bottom phase of the ATPS resulting in a purification factor of 2.74 and 96% activity recovery.     

Interference of some aqueous two-phase system phase-forming components in protein determination by the Bradford method

The interference of some specific aqueous two-phase system (ATPS) phase-forming components in bovine serum albumin (BSA) determination by the Bradford method was investigated. For this purpose, calibration curves were obtained for BSA in the presence of different concentrations of salts and polymers. A total of 19 salts [Na₂SO₄, (NH₄)₂SO₄, MgSO₄, LiSO₄, Na₂HPO₄, sodium phosphate buffer (pH 7.0), NaH₂PO₄, K₂HPO₄, potassium phosphate buffer (pH 7.0), KH₂PO₄, C₆H₈O₇, Na₃C₆H₅O₇, KCHO₂, NaCHO₂, NaCO₃, NaHCO₃, C₂H₄O₂, sodium acetate buffer (pH 4.5), and NaC₂H₃O₂] and 7 polymers [PEG 4000, PEG 8000, PEG 20000, UCON 3900, Ficoll 70000, PES 100000, and PVP 40000] were tested, and each calibration curve was compared with the one obtained for BSA in water. Some concentrations of salts and polymers had considerable effect in the BSA calibration curve. Carbonate salts were responsible for the highest salt interference, whereas citric and acetic acids did not produce interference even in the maximum concentration level tested (5 wt%). Among the polymers, UCON gave the highest interference, whereas Ficoll did not produce interference when used in concentrations up to 10 wt%. It was concluded that a convenient dilution of the samples prior to the protein quantification is needed to ensure no significant interference from ATPS phase-forming constituents.