Polymer displacement in dye-affinity chromatography

Displacement of lactate dehydrogenase from dye-affinity matrices with poly(ethyleneimine) (PEI) was shown to be an effective elution strategy. It resulted in better recoveries and sharper elution profiles than traditional non-specific elution while the purification factors were unchanged. The elution is assumed to proceed via displacement of bound protein by PEI when the polymer binds to the dye-ligands. Complete elution of bound protein is a characteristic feature of such a mechanism. Hence displacement with PEI may be a promising strategy for eluting proteins with reported low recoveries in dye-affinity chromatography protocols.     

Presence of imidazole in loading buffer prevents formation of free radical in immobilized metal affinity chromatography and dramatically improves the recovery of herpes simplex virus type 1 gene therapy vectors

We have recently shown that immobilized metal affinity chromatography (IMAC) is an effective technique for purification of herpes simplex virus type 1 (HSV-1) gene vector engineered to display cobalt affinity tag on the envelope. However, the tagged HSV-1 viruses were severely inactivated by oxidative hydroxyl free radicals when crude HSV-1 supernatant was applied on an immobilized cobalt column and eluted by a low pH buffer. Furthermore, we have reported that virus inactivation could be prevented by inclusion of high concentration of ascorbate in chromatographic mobile phase. In this paper we report that when elution of bound virus was attempted by inclusion of imidazole in elution buffer, rather than lowering the pH of elution buffer, similar inactivation was also observed. The results also demonstrated that virus inactivation was dramatically reduced by inclusion of 20mM imidazole in the loading buffer. Electron spin resonance (ESR) experiments suggest that imidazole prevents hydroxyl free radical generation from the cobalt complexes. This is the first report describing the role of imidazole in preventing free radical formation in an IMAC column. From a practical stand point, our results imply that inclusion of appropriate amount of imidazole in the loading buffer is an effective strategy for improving the recovery yield of active products and for enhancing product quality during IMAC purification.     

Impact of double cryogelation process on a macroporous dye-affinity hydrogel

Cryogels with interconnected channels allow high flow-through properties and mass transfer when dealing with complex mixtures such as non-clarified crude extracts. However, their mechanical strength can be challenged due to a large void volume inside the polymeric network. We have addressed this problem by forming a double-layer cryogel applied as a dye-affinity chromatography gel. In this study, poly(acrylamide-co-allyl glycidyl ether) cryogel was prepared at sub-zero temperature. The second layer was then prepared inside the primary cryogel under the same conditions to form a double-layer network. Cibacron Blue F3GA, a dye molecule, was immobilized on the surface of the cryogels. Bovine serum albumin was used as a model molecule to study the adsorption/elution procedure in batch and continuous modes. The maximum batch binding capacity and the dynamic binding capacity for the single-layer cryogel were 18 and 0.11, and for the double-layer cryogel were 7.5 and 0.9 mg/g of gel, respectively. However, the mechanical stability of the double-layer cryogel increased 7-fold (144 kPa). It was found that the kinetic and adsorption isotherms follow pseudo-second-order and Freundlich models, respectively. The regeneration of the columns after adsorption/elution cycles was evaluated, and no significant loss of capacity was observed after 10 cycles.     

Solution‐blown nylon 6–chitosan core–shell nanofiber for highly efficient affinity adsorption

A facile spinning‐based strategy was developed to fabricate chitosan (CS) surface nanofiber‐based affinity membranes for protein adsorption. The core–shell nanofiber mat of nylon 6–CS was prepared via coaxial solution blowing process. The nanofibers have a diameter range of 60–300 nm. The core–shell structure was confirmed by transmission electron microscopy, and CS was observed as a thin layer that uniformly adhered to the core. The dye ligand of cibacron blue F3GA (CB F3GA) was further covalently immobilized on the nanofibers with a content of 425 µmol/g. The pristine and CB F3GA‐attached mats were studied in protein adsorption. High bovine serum albumin adsorption capacities of 91.9 and 219.6 mg/g were obtained for pristine and CB F3GA‐attached mats, respectively. Given its properties of high flux rate and low pressure drop, CB F3GA‐attached nylon 6–CS nanofiber mat meets the requirements of highly effective affinity membrane chromatography. Copyright © 2016 John Wiley & Sons, Ltd.     

A new affinity-HPLC packing for protein separation: Cibacron blue attached uniform porous poly(HEMA-<Emphasis Type="Italic">co</Emphasis>-EDM) beads

In this study, a new affinity high-performance liquid chromatography (HPLC) stationary phase suitable for protein separation was synthesized. In the first stage of the synthesis, uniform porous poly(2-hydroxyethyl methacrylate-co-ethylene dimethacrylate), poly(HEMA-co-EDM), beads 6.2 μm in size were obtained. Homogeneous distribution of hydroxyl groups in the bead interior was confirmed by confocal laser scanning microscopy. The plain poly(HEMA-co-EDM) particles gave very low non-specific protein adsorption with albumin. The selected dye ligand Cibacron blue F3G-A (CB F3G-A) was covalently linked onto the beads via hydroxyl groups. In the batch experiments, albumin adsorption up to 60 mg BSA/g particles was obtained with the CB F3G-A carrying poly(HEMA-co-EDM) beads. The affinity-HPLC of selected proteins (albumin and lysozyme) was investigated in a 25 mm×4.0-mm inner diameter column packed with CB F3G-A carrying beads and both proteins were successfully resolved. By a single injection, 200 μg of protein was loaded and quantitatively eluted from the column. The protein recovery increased with increasing flow rate and salt concentration of the elution buffer and decreased with the increasing protein feed concentration. During the albumin elution, theoretical plate numbers up to 30,000 plates/m were achieved by increasing the salt concentration.     

Purification of IgG from Sera of Rabbit and Guinea Pig by Flow-Through Mode Ion-Exchange Chromatography using DEAE Sepharose Fast Flow Column

A one-step purification process using flow-through mode ion-exchange chromatography (Ft-IEC) was evaluated for the purification of Immunoglobulin G (IgG) from rabbit and guinea pig serum. A simple protein precipitation with saturated ammonium sulfate was used to pretreated plasma samples. Chromatographic separation was carried out on DEAE Sepharose Fast Flow (F.F.) column at a flow rate of 1 mL min^?1. Ft-IEC using Tris?CHCl buffer at pH 7.0 allowed the recovery of 22% of the loaded IgG with purity of 95% existed in flowthrough and washing effluents but not in elution effluents. To be compared, bind-elute mode IEC using Tris?CHCl buffer at pH 8.5 based on the routine protocol showed that the recovery of 15% of the loaded IgG with purity of 80% existed in elution effluents. These results indicate that the Ft-IEC is an effective method for purifying IgG from sera of rabbit and guinea pig and may also be suitable for other animal sera by adjusting pH at equilibrium buffer for chromatography column.     

Recovery of actinorhodin from fermentation broth

In the present work, a new method of purification for actinorhodin was developed using an expanded bed chromatography technique in which antibiotic capture, feedstock clarification, centrifugation, dialysis and concentration are done in one step. The cation-exchanger (P-11) resulted in 26% adsorption and 2% recovery whereas the anion-exchanger (DE-52) resulted in 99% adsorption and 56% recovery of adsorbed antibiotic using methanol buffer and 2 M NH4Cl as eluting agent. Streamline DEAE anion-exchanger, which is especially designed for EBA applications, yields 82% adsorption and 50% elution of actinorhodin fed into the chromatography column directly from the fermentation broth. Isocratic elution resulted in extremely efficient yield compared to linear gradient elution, i.e. 13.5-fold more recovery in the column with an aspect ratio (L:D) of 4. Expansion by 150% of settled bed resulted in the best recovery of actinorhodin among 100 and 200% expansions. A comparison of breakthrough profiles in packed and expanded bed adsorption showed that the performance of the expanded bed is better (by 33%) at allowing more volume of the fermentation broth to pass through the chromatography column.     

Enhanced performance of expanded bed chromatography on rigid superporous adsorbent matrix

Rigid spherical macroporous adsorbent beads with surface hydroxyl groups were prepared by cross-linking of cellulose. These beads had diameter in the range 100-200 microm and a mean pore size of about 3 microm with about 60% pore volume. The matrix (bulk density approximately 1600 kg m(-3)) could be expanded into a stable bed and used for protein chromatography. Chromatographic runs were performed on a 10 mm diameter column under non-retaining and retaining conditions on the prepared matrix (called Celbeads) and performance of the runs was measured in terms of the height equivalent to a theoretical plate (HETP). The HETP curves in both packed and expanded bed modes followed profiles typical of macroporous adsorbents, i.e. increasing and levelling with velocity. Unimpaired performance of the matrix at increasing flow-rates permitted expanded bed elution of adsorbed solutes without loss of efficiency in terms of purification factor and product concentration. As a model system, Celbeads was used to purify lactate dehydrogenase from porcine muscle homogenate by dye-affinity chromatography. The prepared matrix provided about 100 theoretical plates per meter for the enzyme system at a linear flow velocity of 1.27 cm x min(-1) in an expanded bed elution mode, and gave enzyme yields of 100% with a purification factor of 31 using an optimized procedure. The adsorbent could be cleaned in place with 5 M urea and used repeatedly without loss of performance.     

Use of proteomics for design of a tailored host cell for highly efficient protein purification

After some initial optimization, a downstream process comprised of one or several chromatography steps removes the majority of the host proteins and achieves a reasonable degree of purification. The separation of remaining contaminant proteins from the target protein could become very difficult and costly due to their similar physicochemical properties. In this paper we describe a highly efficient strategy, based on proteomic analysis and elution chromatography, by which a protein of interest may be isolated from copurifying contaminants. Mutant strains of Escherichia coli were prepared that are deficient in three prevalent host proteins found in a strategic fraction of an elution profile of nickel immobilized affinity chromatography. Recombinant green fluorescent protein (GFPuv) served as a model protein and its elution was directed to this optimized fraction with an N-terminus hexahistidine tag (his₆), thereby easing its recovery. We demonstrate that proteomic data can facilitate the rational engineering of host cell expressing the target protein and the design of an efficient process for its purification.     

High-performance liquid chromatography of proteins: purification of alpha-fetoprotein from fetal calf serum

High-performance liquid chromatography was utilized for the purification of bovine alpha-fetoprotein (BAFP) from fetal calf serum (FCS). An initial step in the purification involved absorption of charcoal delipidated FCS on Cibacron Blue F3GA gel. The Cibacron Blue pre-purified FCS was then chromatographed on a Polyanion SI weak anion-exchange column. The BAFP isolated had a purity of greater than 93% with an overall yield of 48% from FCS. The procedure was applicable for semi-preparative scale purification of BAFP.     

Refolding and simultaneous purification of recombinant human proinsulin from inclusion bodies on protein‐folding liquid‐chromatography columns

Protein‐folding liquid chromatography (PFLC) is an effective and scalable method for protein renaturation with simultaneous purification. However, it has been a challenge to fully refold inclusion bodies in a PFLC column. In this work, refolding with simultaneous purification of recombinant human proinsulin (rhPI) from inclusion bodies from Escherichia coli were investigated using the surface of stationary phases in immobilized metal ion affinity chromatography (IMAC) and high‐performance size‐exclusion chromatography (HPSEC). The results indicated that both the ligand structure on the surface of the stationary phase and the composition of the mobile phase (elution buffer) influenced refolding of rhPI. Under optimized chromatographic conditions, the mass recoveries of IMAC column and HPSEC column were 77.8 and 56.8% with purifies of 97.6 and 93.7%, respectively. These results also indicated that the IMAC column fails to refold rhPI, and the HPSEC column enables efficient refolding of rhPI with a low‐urea gradient‐elution method. The refolded rhPI was characterized by circular dichroism spectroscopy. The molecular weight of the converted human insulin was further confirmed with SDS–18% PAGE, Matrix‐Assisted Laser Desorption/ Ionization Time of Flight Mass Spectrometry (MALDI‐TOF‐MS) and the biological activity assay by HP‐RPLC. Copyright © 2014 John Wiley & Sons, Ltd.     

开管毛细管亲和液相色谱初探

 提出了一种新的亲和色谱模式开管毛细管亲和液相色谱。在内径为 5 0 μm的毛细管内表面键合一层三嗪染料配体 ,利用毛细管电泳仪的压力系统进行亲和色谱实验。采用流动相切换洗脱技术 ,牛血清白蛋白和溶菌酶获得了有效的分离。连续运行 10次 ,溶菌酶的出峰时间、峰面积和峰高的相对标准偏差分别为0 1% ,4 3% ,3 7%。在 8 6ng～ 2 8 7ng范围内 ,溶菌酶的进样量与峰面积和峰高都呈线性关系 ,其相关系数分别为 0 9946和 0 9988。     

Rapid method for the fractionation of nuclear proteins and their complexes by batch elution from hydroxyapatite

A new procedure for the separation and purification of nuclear proteins and their complexes by batch elution from hydroxyapatite is presented. This method allows to isolate such proteins with different basic character faster and more efficiently than procedures using column chromatography, while showing high selectivity, sensitivity, simplicity, mild conditions of purification, reproducibility and protein stability.     

膜径向离子交换色谱分离凝血酶原复合物

 利用径向离子交换色谱法分离纯化了Nitschmann组分Ⅲ中的凝血酶原复合物 ( prothrombincomplexconcentrate ,PCC) ,流动相为pH 7.5的Tris HCl缓冲液 ,色谱柱为XK 1 6DEAEfastflowSepharose ( 0 .8cmi.d .× 5cm)及膜DEAE径向色谱柱 ( 3.0cmi.d .× 5.8cm)。通过改变不同上样流速及洗脱流速 ,研究了流速对所分离的凝血酶原复合物的蛋白质量浓度及凝固活性的影响 ,为今后在血浆蛋白分离纯化中进一步推广使用径向色谱技术和放大实验提供了依据。     

Study on the inclusion complexes of cryptotanshinone with beta-cyclodextrin and hydroxypropyl-beta-cyclodextrin

The inclusion complexes of beta-cyclodextrin (beta-CD) and HP-beta-cyclodextrin (HP-beta-CD) with a kind of tanshinone, cryptotanshinone (CTan) were investigated by using spectrophotometry. Stable inclusion complexes were established in solution and in solid state and were characterized by UV, IR and 1H NMR spectra, respectively. The optimum pH for inclusion is about 7.5. Stoichiometry of the inclusion complex is 1:1. The stabilities of beta-CD and HP-beta-CD to CTan were in the order: beta-CD相似文献   

一种从蛇毒中纯化神经生长因子的新工艺

为了能从中华眼镜蛇蛇毒中简单快速地分离纯化神经生长因子（一种治疗各种神经性损伤和神经退行疾病的药物,简称NGF）,采用不同的色谱柱联用的方式对NGF的纯化工艺进行了研究。结果表明,采用DEAE Sepharose F.F.和Sephadex G 50二步柱色谱工艺可以从蛇毒中快速分离得到神经生长因子。经十二烷基硫酸钠聚丙烯酰胺凝胶电泳和反相高效液相色谱分析, 证明所得到的NGF为单一组分,相对分子质量约为 29 000。对8　d龄鸡胚背根神经节采用体外培养法,结果证明,所得NGF具有明显的促进神经纤维     

Application of a chromatography model with linear gradient elution experimental data to the rapid scale-up in ion-exchange process chromatography of proteins

We applied the model described in our previous paper to the rapid scale-up in the ion exchange chromatography of proteins, in which linear flow velocity, column length and gradient slope were changed. We carried out linear gradient elution experiments, and obtained data for the peak salt concentration and peak width. From these data, the plate height (HETP) was calculated as a function of the mobile phase velocity and iso-resolution curve (the separation time and elution volume relationship for the same resolution) was calculated. The scale-up chromatography conditions were determined by the iso-resolution curve. The scale-up of the linear gradient elution from 5 to 100mL and 2.5L column sizes was performed both by the separation of beta-lactoglobulin A and beta-lactoglobulin B with anion-exchange chromatography and by the purification of a recombinant protein with cation-exchange chromatography. Resolution, recovery and purity were examined in order to verify the proposed method.     

Enantiomeric separation by capillary electrochromatography. I. Chiral separation of dansyl amino acids and organochlorine pesticides on a diol-silica dynamically coated with hydroxypropyl-beta-cyclodextrin

In this work, a commercially available diol-silica stationary phase was converted in situ to a chiral stationary phase by dynamically coating it with hydroxypropyl-beta-cyclodextrin (HP-beta-CD). This stationary phase was shown useful for the capillary electrochromatography (CEC) separation of neutral and anionic enantiomers such as some organochlorine pesticides and dansyl amino acids, respectively. The inclusion of HP-beta-CD in the mobile phase to produce the in situ chiral stationary phase allowed the rapid separation of the anionic dansyl amino acid enantiomers at relatively low electroosmotic flow (EOF). The formation of host-guest complexes between the dansyl amino acids and the neutral HP-beta-CD in the mobile phase lowered the actual charge-to-mass ratios of the anionic solutes, thus speeding up their transport by the EOF across the packed capillary column. Several parameters affecting enantioseparation were investigated, including the concentration of HP-beta-CD, ionic strength, pH, and organic modifier content of the mobile phase.     

Application of preparative reversed-phase high-performance liquid chromatography to the isolation of insulin-like growth factor II from human serum

Substantially purified insulin-like growth factor II (IGF-II) was prepared from human serum. Initial enrichment using ion-exchange chromatography on DEAE Sephadex A50, followed by gel permeation chromatography on Sephadex G-75 in 1% formic acid produced material suitable for application to a preparative reversed-phase high-performance liquid chromatographic (HPLC) column containing LiChroprep RP-18. The latter step gave about 90-fold purification with a recovery of about 70% IGF-II bio-activity. Finally, a small reversed-phase HPLC column achieved a 17-fold purification with similar yield of activity. Overall, the four steps gave IGF-II of about 90% purity in yield of 12%.