Rongyue Zhang

Preparation of poly(N-isopropylacrylamide)-grafted polymer monolith for hydrophobic interaction chromatography of proteins

Poly(N-isopropylacrylamide)-grafted polymer monolith has been achieved using a surface-initiated atom transfer radical polymerization grafting polymerization within the pores of poly(chloromethylstyrene-divinylbenzene) macroporous monolith contained in a 100 mm x 4.6mm I.D. stainless steel column. The grafted-poly(N-isopropylacrylamide) on the surface of the grafted monolith that was used as chromatographic stationary phase showed a response to the variation of temperatures and/or salt concentrations. This study focus on its salt concentration responsive property and it has been revealed that the hydrophobicity of the grafted monolith can be adjusted by changing salt concentrations in the range of 0.05-2.0 mol/L. A variety of salts including sodium sulfate, ammonium sulfate and sodium chloride exhibited different effects on the alteration of hydrophobicity of the grafted monolith, and the effect of the salts was in the order of sodium sulfate>ammonium sulfate>sodium chloride. Based on this response to salt concentrations, the grafted monolith was applied in hydrophobic interaction chromatography of proteins, and the base-line separation of a six proteins mixture consisting of cytochrome c, myoglobin, ribonuclease A, bovine serum albumin, ovalbumin and thyroglobulin bovine was achieved by a salt gradient elution.

Hydrophilic modification gigaporous resins with poly(ethylenimine) for high-throughput proteins ion-exchange chromatography.

High hydrophilicity of gigaporous microspheres based on a copolymer of poly(glycidyl methacrylate)-co-divinyl benzene (PGMA-DVB) was successfully realized through coating the branched polyethyleneimine (PEI) in PGMA-DVB microspheres. PEI with various molecules weights and different branching agents were identified in terms of protein recovery as evaluation approach. For this evaluation, PEI600 (Mw=600) and poly (ethylene glycol) diglycidyl ether (PEGDE, Mw=400) were used as modification agent and branching agent, respectively. The modified microspheres showed good permeability and revealed a certain mechanical strength. After modification, the protein recovery increased from 40% to >90%. The protein recovery increased with the branched generations and the first and second generations could give the protein recovery of 93% and 96%, respectively. Meanwhile, the ionic capacity also showed a rising trend in the range of 0.11-0.32mmol/mL with the branched generations. But the dynamic binding capacity of protein (bovine serum albumin, BSA as the model protein) increased at first and then decreased. Analysis of the dry microspheres structure by mercury intrusion method as well as observation of the branched PEI on PGMA-DVB membrane in aqueous solution indicated that excess PEI chains with the extended state in the second generation would block the small pores and decrease the accessible surface area. Therefore, the protein capacity on the second generation, on the contrary, was lower than that on the first generation. Meanwhile, it was found that the PEI chains in the modified microspheres changed their construction from the extended to the collapsed state with increase of NaCl concentration. And the corresponding pore size of the modified microspheres increased with salt concentration through low-field nuclear magnetic resonance. Dynamic binding capacity of proteins on the modified supports did not significantly change with increase of the flow rate. The media showed good performance for separation three model proteins at high flow rate of 1084cm/h. This modified gigaporous microspheres had a large potential in application for rapid separation of biomolecules.

Efficient decolorization and deproteinization using uniform polymer microspheres in the succinic acid biorefinery from bio-waste cotton (Gossypium hirsutum L.) stalks.

Bio-waste cotton (Gossypium hirsutum L.) stalks were converted into succinic acid by simultaneous saccharification and fermentation (SSF) using Actinobacillus succinogenes 130Z. After 54 h SSF at 40 °C and pH 7.0, the production of succinic acid was 63 g/L, with 1.17 g/L/h productivity and 64% conversion yield. After SSF, a simple method for the decolorization and deproteinization of crude SSF broth was developed through adsorption tests of polystyrene (PSt) microspheres. Under optimized conditions (5% PSt loading (w/v), pH 4.0, 60 °C and adsorption time of 40 min), the ratios of decolorization, deproteinization and succinic acid loss ratios were 96.6, 84.5 and 4.1%, respectively. The method developed will provide a potential approach for large-scale production of succinic acid from the biomass waste.

Detailed exploration of structure formation of an epoxy-based monolith with three-dimensional bicontinuous structure

To explore a clear formation mechanism of a three-dimensional (3D) bicontinuous skeleton and control the structure of an epoxy-based monolith, we have prepared the monolith using a mixture of good and poor solvents. The influences of reaction and phase separation parameters, such as molecular weights and content of porogenic poor solvents, porogenic good solvent concentration, equivalent ratio of epoxy group to amine and reaction temperature on the final morphology are systematically studied by monitoring the reaction process with differential scanning calorimetry (DSC) and observing the cloud points (CP). Depending on the above parameters, the resultant morphology can be varied ranging from closed pore structure to globules aggregated structure, which was controlled by the competitive kinetics between the domain coarsening and the structure freezing. The optimized monoliths with uniform and controllable pores have great potential for application in chromatographic separation, membrane filters, and membrane emulsification.

Efficient fabrication of high‐capacity immobilized metal ion affinity chromatographic media: The role of the dextran‐grafting process and its manipulation

Novel high-capacity Ni(2+) immobilized metal ion affinity chromatographic media were prepared through the dextran-grafting process. Dextran was grafted to an allyl-activated agarose-based matrix followed by functionalization for the immobilized metal ion affinity chromatographic media. With elaborate regulation of the allylation degree, dextran was completely or partly grafted to agarose microspheres, namely, completely dextran-grafted agarose microspheres and partly dextran-grafted ones, respectively. Confocal laser scanning microscope results demonstrated that a good adjustment of dextran-grafting degree was achieved, and dextran was distributed uniformly in whole completely dextran-grafted microspheres, while just distributed around the outside of the partly dextran-grafted ones. Flow hydrodynamic properties were improved greatly after the dextran-grafting process, and the flow velocity increased by about 30% compared with that of a commercial chromatographic medium (Ni Sepharose FF). A significant improvement of protein binding performance was also achieved by the dextran-grafting process, and partly dextran-grafted Ni(2+) chelating medium had a maximum binding capacity for His-tagged lactate dehydrogenase about 2.5 times higher than that of Ni Sepharose FF. The results indicated that this novel chromatographic medium is promising for applications in high-efficiency and large-scale protein purification.

A novel gigaporous GSH affinity medium for high-speed affinity chromatography of GST-tagged proteins

Novel GSH-AP (phenoxyl agarose coated gigaporous polystyrene, Agap-co-PSt) microspheres were successfully prepared by introducing GSH ligand into hydrophilic AP microspheres pre-activated with 1,4-butanediol diglycidyl ether. The gigaporous structure and chromatographic properties of GSH-AP medium were evaluated and compared with commercial GSH Sepharose FF (GSH-FF) medium. The macropores (100-500nm) of gigaporous PSt microspheres were well maintained after coating with agarose and functionalized with GSH ligand. Hydrodynamic experiments showed that GSH-AP column had less backpressure and plate height than those of GSH-FF column at high flow velocity, which was beneficial for its use in high-speed chromatography. The presence of flow-through pores in GSH-AP microspheres also accelerated the mass transfer rate of biomolecules induced by convective flow, leading to high protein resolution and high dynamic binding capacity (DBC) of glutathione S-transferase (GST) at high flow velocity. High purity of GST and GST-tagged recombinant human interleukin-1 receptor antagonist (rhIL-1RA) were obtained from crude extract with an acceptable recovery yield within 1.5min at a velocity up to 1400cm/h. GSH-AP medium is promising for high-speed affinity chromatography for the purification of GST and GST-tagged proteins.

Improved Stability of Emulsions in Preparation of Uniform Small-Sized Konjac Glucomanna (KGM) Microspheres with Epoxy-Based Polymer Membrane by Premix Membrane Emulsification

Uniform small-sized (<10 μm) Konjac glucomanna (KGM) microspheres have great application prospects in bio-separation, drug delivery and controlled release. Premix membrane emulsification is an effective method to prepare uniform small-sized KGM microspheres. However, since KGM solution bears strong alkalinity, it requires the membrane to have a hydrophobic surface resistant to alkali. In this study, uniform small-sized KGM microspheres were prepared with epoxy-based polymer membrane (EP) we developed by premix membrane emulsification. It was found that emulsion coalescence and flocculation occurred frequently due to the high interface energy and sedimentation velocity of KGM emulsions. Emulsion stability had a significant influence on the uniformity and dispersity of the final KGM microspheres. To improve the stability of the emulsions, the effects of the concentration of the emulsifier, the viscosity of the KGM solution, the oil phase composition and the feeding method of epoxy chloropropane (EC) on the preparation results were studied. Under optimal preparation conditions (emulsifier 5 wt % PO-5s, KGM III (145.6 mPa·s), weight ratio of liquid paraffin (LP) to petroleum ether (PE) 11:1), uniform and stable KGM emulsions (d = 7.47 μm, CV = 15.35%) were obtained and crosslinked without emulsion-instable phenomena.

Functional hydrophilic polystyrene beads with uniformly size and high cross-linking degree facilitated rapid separation of exenatide

A high cross-linking polystyrene(PSt)-based anion-exchange material with uniformly size, high ion exchange capacity, and high hydrophilicity was synthesized by a novel surface functionalization approach in this study. Uniformly sized PSt microspheres were prepared by the membrane emulsion polymerization strategy, and then modified by (1) conversing resid ual surface vinyl groups to epoxy groups followed by quaternization, and (2) decorating aromatic ring matrix including nitration, reduction and attachment of glycidyltrimethylammonium chloride. The 3-D morphology and porous features of microspheres were observed by scanning electron microscopy (SEM) and atomic force microscopy (AFM). The surface of the modified PSt became roughness but the particle size remained same. Meanwhile, FT-IR spectra and laser scanning confocal microscope (LCSM) indicated that the modification groups had been successfully covalently coated onto the PSt microspheres. Modified PSt microspheres showed greatly improved hydrophilicity and biocompatibility with 0.387mmol/mL ion exchange capacity (IEC). In the application evaluation procedure, exenatide can be purified from 42.9% (peptide crudes) to 88.6% by modified PSt column with 97.1% recovery yield. This modified PSt microspheres had a large potential in application for efficient separation of peptides.

A novel rProtein A chromatographic media for enhancing cleaning-in-place performance

Protein A chromatography has been a popular method for purification of therapeutic monoclonal antibodies (mAb). Protein A chromatographic media using alkali-resistant rProtein A ligands from site-directed coupling method have been pursued for both high dynamic capacities and excellent stabilities. However, the mechanism of rProtein A leaking under cleaning-in-place (CIP) conditions is not very clear and difficulties have been commonly encountered when improving the medias chromatographic performance. We investigated the chromatographic performance of site-directed coupled rProtein A chromatographic media during CIP procedure. Trace amount of ligands leaked during the chromatographic medias incubation in 0.5 M NaOH was detected, explaining for the decline of chromatographic medias CIP performance. Decrease of rProtein As concentration in 0.5 M NaOH was consistent with chromatographic medias binding capacity. A novel rProtein A chromatographic media were prepared by site-directed coupling a newly-constructed alkali-resistant rProtein A to highly cross-linked agarose-based matrix. The media had a dynamic binding capacity of 63.2 mg hIgG/mL higher than 48.1 mg hIgG/mL of the commercial one, and the CIP performance was improved greatly with the remained dynamic binding capacity increased from 86% to 95% of the initial value after 40 CIP cycles.