Aqueous two-phase separation enables selective purification of mono-PEGylated human serum albumin: influence of process parameters and reagent size

Evaluation of poly(ethylene glycol)/hydroxypropyl starch aqueous two-phase system for immunoglobulin G extraction

Aqueous two-phase (polyethylene glycol + sodium sulfate) system for caffeine extraction: Equilibrium diagrams and partitioning study

Recombinant bispecific antibodies such as tandem scFv molecules (taFv), diabodies (Db), or single chain diabodies (scDb) have shown to be able to retarget T lymphocytes to tumor cells, leading to their destruction. However, therapeutic efficacy is hampered by a short serum half-life of these small molecules having molecule masses of 50-60 kDa. Thus, improvement of the pharmacokinetic properties of small bispecific antibody formats is required to enhance efficacy in vivo. In this study, we generated several recombinant bispecific antibody-albumin fusion proteins and analyzed these molecules for biological activity and pharmacokinetic properties. Three recombinant antibody formats were produced by fusing two different scFv molecules, bispecific scDb or taFv molecules, respectively, to human serum albumin (HSA). These constructs (scFv(2)-HSA, scDb-HSA, taFv-HSA), directed against the tumor antigen carcinoembryonic antigen (CEA) and the T cell receptor complex molecule CD3, retained full binding capacity to both antigens compared with unfused scFv, scDb, and taFv molecules. Tumor antigen-specific retargeting and activation of T cells as monitored by interleukin-2 release was observed for scDb, scDb-HSA, taFv-HSA, and to a lesser extent for scFv(2)-HSA. T cell activation could be further enhanced by a target cell-specific costimulatory signal provided by a B7-DbCEA fusion protein. Furthermore, we could demonstrate that fusion to serum albumin strongly increases circulation time of recombinant bispecific antibodies. In addition, our comparative study indicates that single chain diabody-albumin fusion proteins seem to be the most promising format for further studying cytotoxic activities in vitro and in vivo.

This study examined the effect of third components (low-molecular-weight saccharides and polymers) on the crystallization of poly(ethylene) glycol (PEG) in frozen solutions, focusing on the relationship between their crystallization-inhibiting ability and molecular compatibility. Effects of sugars and polymers on the crystallization of PEG 3000 in frozen solution were monitored by differential scanning calorimetry (DSC). Pulsed-NMR was employed to monitor the molecular mobility of water and solutes in the frozen solutions. Miscibility between PEG and third components in aqueous solution was estimated from the lowering of cloud point of PEG 20,000. Thermal analysis of frozen solutions containing some non-crystallizing solutes was used to examine the possibility of phase separation in frozen solutions. Some sugars and polymers inhibited the crystallization of PEG and formed practically stable amorphous phases among ice crystals. The mobility of solute molecules in the amorphous phase increased above the softening temperature of maximally concentrated solutions (Ts), whereas that of water molecules appeared at a lower temperature. Mono- and disaccharides that are relatively less miscible with PEG in solution inhibit PEG crystallization to a lesser degree. Two Ts regions were observed in frozen solutions containing both polyvinylpyrrolidone (PVP) and dextran, at much lower concentrations than those causing aqueous two-phase separation at ambient temperatures. Ice crystallization raises the concentration of solutes in the remaining solution, which can lead to phase separation in the amorphous phase. Molecular compatibility between components is an important factor determining their propensity to phase separate and crystallize.

Rotavirus-like particles primary recovery from insect cells in aqueous two-phase systems☆

Macroscopic structures of gel fibers have been prepared by control of the polymer solution properties and by design of the nozzle and flow path of the microfluidic device. In this research, we investigated a method to simultaneously fabricate hundreds to thousands of gel filaments simply by flowing the polymer solution inside the capillary without spinneret. An aqueous two-phase separation (ATPS) can be induced by adjusting their concentration in certain combinations of two polymers. The respective polymer concentration in each phase can be determined from the phase diagram, whereas an assembly of heterogeneous polymers generate in each phase. Hydrodynamic properties of pre-gel solution can be controlled by inducing such heterogeneous polymer assemblies. A co-axial flow double capillary was used to fabricate gel filaments, where an inner capillary (inner diameter 0.7 mm) was fixed at the insert position of an outer capillary. To induce ATPS, an ionic strength for the aqueous solution of sodium alginate (Alg) / polyethylene glycol (PEG) mixture was controlled by NaCl addition. The pre-gel Alg/PEG solution was flown as an inner flow of glass double capillaries, where a crosslinker solution (Ca2+ soln.) was flown as a sheath flow. The obtained gel was composed of multiple parallel gel filaments with a diameter of several micrometers, while a single gel without filament structure was obtained from the homogeneous solution without NaCl addition. In aqueous solution, the Alg chain has a structure with few entanglements because of its rigidity. The rigid assembly of alginate is mainly caused by guluronic acid block, that is stabilized by diaxial linkages via intramolecular hydrogen bonds. The shear stress generated by flowing the aqueous Alg solution inside the capillary cannot induce deformation of its rigid assembly, results in the single thick gel filament. By complexation with PEG, destruction of regular hydrogen bond was responsible for breaking the rigid structure of Alg. Thus, deformation of Alg/PEG assembly was enabled to elongate as the fibrous structure by the shear stress, followed by gelation in contact with Ca2+ ions at the outlet of the inner capillary. Such shear-induced deformation of the Alg/PEG assembly was studied by measuring viscoelastic properties with a spindle viscometer. Besides, Alg/PEG assembly generation in each phase was determined by size-exclusion chromatography with a multi angle light scattering detector. This presentation will discuss a simple technique for preparing multiple gel filaments simply by passing a polymer solution through a capillary.

Polyethylene glycol (PEG) has been widely used as a serum half-life extender of therapeutic proteins. However, due to immune responses and low degradability of PEG, developing serum half-life extender alternatives to PEG is required. Human serum albumin (HSA) has several beneficial features as a serum half-life extender, including a very long serum half-life, good degradability, and low immune responses. In order to further evaluate the efficacy of HSA, we compared the extent of serum half-life extension of a target protein, superfolder green fluorescent protein (sfGFP), upon HSA conjugation with PEG conjugation side-by-side. Combination of site-specific incorporation of p-azido-l-phenylalanine into sfGFP and copper-free click chemistry achieved the site-specific conjugation of a single HSA, 20 kDa PEG, or 30 kDa PEG to sfGFP. These sfGFP conjugates exhibited the fluorescence comparable to or even greater than that of wild-type sfGFP (sfGFP-WT). In mice, HSA-conjugation to sfGFP extended the serum half-life 9.0 times compared to that of unmodified sfGFP, which is comparable to those of PEG-conjugated sfGFPs (7.3 times for 20 kDa PEG and 9.5 times for 30 kDa PEG). These results clearly demonstrated that HSA was as effective as PEG in extending the serum half-life of a target protein. Therefore, with the additional favorable features, HSA is a good serum half-life extender of a (therapeutic) protein as an alternative to PEG.

Studies of protein partition in non conventional aqueous two-phase systems as method to purify trypsinogen and alpha-chymotrypsinogen from bovine pancreas

BACKGROUNDRoseoflavin (RoS) is a naturally occurring red color riboflavin analog compound, produced mainly by Streptomyces davaonensis, with a rising profile owing to its antibacterial potential. However, there is a lack of strategies for its downstream processing and the existing ones are limited to chromatographic techniques involving harmful reagents. The use of aqueous two‐phase systems (ATPS), a liquid–liquid extraction method, is explored in this work as an alternative strategy to recover and purify RoS from S. davaonensis cultures.RESULTSPolymer‐phosphate, alcohol‐phosphate and ionic liquid (IL)‐phosphate systems that varied in composition were tested, where polyethylene glycol (PEG), ethanol (EtOH) and 1‐ethyl‐3‐methylimidazolium acetate ([C2mim] [OAC]) represent the top phases, and phosphate the bottom phase. The partition behavior of either RoS alone or with contaminants was evaluated. In both cases, RoS showed a preference for top phase in all the systems tested. When cell‐free cultures were added to the systems, IL‐salt (13% and 30% w/w), EtOH‐phosphate [50% tie‐line length (TLL)] and PEG8000‐phosphate (35% w/w TLL) systems presented the highest RoS recovery (>95%), but separation of RoS and contaminants was not accomplished. The systems that demonstrated separation of RoS and contaminants were the PEG3350‐ and PEG8000‐salt systems, both with a 15% w/w TLL, as RoS and contaminants partitioned to top and bottom phases, respectively.CONCLUSIONThis is the first attempt at using ATPS to recover RoS from S. davaonensis cultures. It has been proven that RoS can be recovered directly from S. davaonensis cultures using biphasic systems. This strategy may represent a greener alternative to chromatographic techniques. © 2021 Society of Chemical Industry (SCI).

Plant suspension cell cultures are emerging as an alternative to mammalian cells for production of complex recombinant proteins. Plant cell cultures provide low production cost, intrinsic safety and adherence to current regulations, but low yields and costly purification technology hinder their commercialization. Fungal hydrophobins have been utilized as fusion tags to improve yields and facilitate efficient low-cost purification by surfactant-based aqueous two-phase separation (ATPS) in plant, fungal and insect cells. In this work, we report the utilization of hydrophobin fusion technology in tobacco bright yellow 2 (BY-2) suspension cell platform and the establishment of pilot-scale propagation and downstream processing including first-step purification by ATPS. Green fluorescent protein-hydrophobin fusion (GFP-HFBI) induced the formation of protein bodies in tobacco suspension cells, thus encapsulating the fusion protein into discrete compartments. Cultivation of the BY-2 suspension cells was scaled up in standard stirred tank bioreactors up to 600L production volume, with no apparent change in growth kinetics. Subsequently, ATPS was applied to selectively capture the GFP-HFBI product from crude cell lysate, resulting in threefold concentration, good purity and up to 60% recovery. The ATPS was scaled up to 20L volume, without loss off efficiency. This study provides the first proof of concept for large-scale hydrophobin-assisted production of recombinant proteins in tobacco BY-2 cell suspensions.

Expert consensus on the use of human serum albumin in critically ill patients.

Primary recovery of recombinant human serum albumin from transgenic Oryza sativa with a single-step aqueous biphasic system

Interfacial tension of polyethyleneglycol-dextran-water systems: influence of temperature and polymer molecular weight

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

Software Copyright: Software Copyright Law Third Edition by David I. Bainbridge, 1997, soft-cover, Butterworths, 32Opp., ISBN 0 406 89421 3.