A NOVEL ANION-EXCHANGE RESIN SUITABLE FOR BOTH DISCOVERY RESEARCH AND CLINICAL MANUFACTURING PURPOSES

Strong ion-exchange protein chromatography is one of the most powerful and most common steps for protein purification in both discovery research and manufacturing. However, the demands on protein purification of early drug discovery and later stage manufacturing are quite different. In order to shorten the time of developing a purification process for new protein drug candidates, there is a need for a strong ion-exchange resin that will be optimum for both stages. This article details a novel anion-exchange resin suitable for research, as well as for clinical manufacturing. In this study, a novel Q resin anion-exchange prototype was evaluated and compared to the GE Healthcare Q Sepharose® Fast Flow (QFF) and Q Sepharose® High Performance (QHP) resins. This study specifically focused on the following: resolution, dynamic binding capacity, flow rate, back pressure, and scale up. The evaluation was performed in both small- and large-scale experiments. From all the comparable data, the prototype resin is adaptable for both discovery research and manufacturing. Its wide-range operation suitability could potentially shorten the time required to develop conventional purification protocols for clinical manufacturing.     

Improved purification of recombinant adenoviral vector by metal affinity membrane chromatography

The increasing importance of adenoviral vectors for gene therapy clinical trials necessitates the development of processes suitable for large-scale and commercial production of adenovirus. Here, we evaluated a novel purification process combining an anion-exchange chromatography and an immobilized metal affinity membrane chromatography for the purification of recombinant adenovirus. Adenovirus was initially purified from clarified infectious lysate by anion-exchange chromatography using Q Sepharose XL resin and further polished using a Sartobind IDA membrane unit charged with Zn²⁺ ions as affinity ligands. The metal affinity membrane chromatography efficiently removed residual host cell impurities that co-eluted with adenovirus during the previous anion-exchange chromatography step. The metal affinity membrane chromatography also separated defective adenovirus particles from the infectious adenovirus fraction. Furthermore, the metal affinity membrane chromatography showed an improved yield, when compared with a conventional bead-based metal affinity chromatography. The purity and specific activity of the adenovirus prepared using this two-step chromatography was comparable to those of adenovirus produced by the conventional CsCl density centrifugation. Therefore, our data provide an improved method for the purification of adenoviral vectors for clinical applications.     

Isolation and purification of plastocyanin from spinach stored frozen using hydrophobic interaction and ion-exchange chromatography

A new simple three-day procedure for preparative isolation and purification of plastocyanin from spinach stored in the frozen state is described. This procedure is based on batch adsorption on ion-exchange resin, ammonium sulphate precipitation, and purification on a Phenyl-Sepharose hydrophobic interaction column and a single Q Sepharose High Performance ion-exchange column. Approximately 100 mg of plastocyanin with an absorbance ratio A₂₇₈/A₅₉₇ of 1.10±0.02 in the oxidized state was typically obtained from 12 kg of spinach leaves. The purified spinach plastocyanin is shown to be homogeneous to the resolution of free solution capillary electrophoresis.Abbreviations MES 2(N-morpholino)ethanesulfonic acid - Tris Tris(hydroxymethyl)aminomethane - FSCE free solution capillary electrophoresis     

Expression, purification, and molecular analysis of the Necator americanus glutathione S-transferase 1 (Na-GST-1): a production process developed for a lead candidate recombinant hookworm vaccine antigen

The enzyme Necator americanus glutathione S-transferase 1 (Na-GST-1) belongs to a unique Nu class of GSTs and is a lead candidate antigen in a bivalent human hookworm vaccine. Here we describe the expression of Na-GST-1 in the yeast Pichia pastoris at the 20 L manufacturing scale and its purification process performed by three chromatographic steps, comprised of a Q Sepharose XL anion exchange column, followed by a Butyl Sepharose HP hydrophobic affinity column and a Superdex 75 size-exclusion column. Approximately 1.5 g of recombinant protein was recovered at an overall process yield of 51%, with a purity grade of 98% and the absence of detectable host cell protein. By mass spectrometry the recombinant protein exhibits a mass of 23,676Da, which closely matches the predicted molecular mass of the protein. The expression and purification methods described here are suitable for further scale-up product development and for its use to design formulation processes suitable to generate a vaccine for clinical testing.     

Extension of the selection of protein chromatography and the rate model to affinity chromatography

The rational selection of optimal protein purification sequences, as well as mathematical models that simulate and allow optimization of chromatographic protein purification processes have been developed for purification procedures such as ion-exchange, hydrophobic interaction and gel filtration chromatography. This paper investigates the extension of such analysis to affinity chromatography both in the selection of chromatographic processes and in the use of the rate model for mathematical modelling and simulation. Two affinity systems were used: Blue Sepharose and Protein A. The extension of the theory developed previously for ion-exchange and HIC chromatography to affinity separations is analyzed in this paper. For the selection of operations two algorithms are used. In the first, the value of η, which corresponds to the efficiency (resolution) of the actual chromatography and, Σ, which determines the amount of a particular contaminant eliminated after each separation step, which determines the purity, have to be determined. It was found that the value of both these parameters is not generic for affinity separations but will depend on the type of affinity system used and will have to be determined on a case by case basis. With Blue Sepharose a salt gradient was used and with Protein A, a pH gradient. Parameters were determined with individual proteins and simulations of the protein mixtures were done. This approach allows investigation of chromatographic protein purification in a holistic manner that includes ion-exchange, HIC, gel filtration and affinity separations for the first time.     

Affinity purification of recombinant protein-tyrosine phosphatase 1B using a highly selective inhibitor

Our structure-based drug discovery program within the field of protein-tyrosine phosphatases (PTPs) demands delivery of significant amounts of protein with extraordinary purity specifications over prolonged time periods. Hence, replacement of classical, multi-step, low-yield protein purifications with efficient affinity techniques would be desirable. For this purpose, the highly selective PTP1B inhibitor 2-(oxalyl-amino)-4,5,6,7-tetrahydro-thieno[2,3-c]pyridine-3-carboxylic acid (OTP) was coupled to epoxy-activated Sepharose 6B (OTP Sepharose) and used for one-step affinity purification of tag-free PTP1B. The elution was performed with a combined pH and salt gradient. Importantly, since OTP Sepharose binds PTP1B with an intact active site only, the method ensures that the purified enzyme is fully active, a feature that might be particularly important in PTP research.     

Purification of a full-length recombinant glucocorticoid receptor

We described a novel purification method for a recombinant glucocorticoid receptor (GR) in detail. The purification procedure consists of sequential chromatographies using common ion-exchange columns (Mono Q and Mono S). This procedure is based upon a new finding that the activated GR binds both to a Mono Q column and to a Mono S column at the same pH. The entire chromatographies took about 3 h and GR represented 97% of the purified protein sample. This purification protocol will be applicable to the purification of native GR, point-mutated recombinant GR and other nuclear receptors.     

Behaviour of vanadate and vanadium-transferrin complex on different anion-exchange columns. Application to in vivo 48V-labelled rat serum

The behaviour of free [48V]vanadate and [48V]vanadium-transferrin complex was investigated on five different anion-exchange columns (Mono Q 5/5 HR, Hitrap Q HP, Sepharose Q FF, Sepharose DEAE FF and Hitrap Q XL). The recovery of both V-compounds was quantitative. The peak shape and retention time of vanadate varied according to the type of column. The vanadium-transferrin complex also showed different elution patterns depending on the type of column. Especially in case of the Sepharose Q FF, Mono Q 5/5 HR and Hitrap Q XL columns the vanadium-transferrin binding was degraded during elution on the column. The results clearly prove that care should be taken as to the choice of column for speciation purposes of vanadium compounds in order to prevent various artefacts showing up in the chromatograms. A Hitrap Q HP column was used to fractionate different vanadium compounds in rat serum.     

Application of mixed modal resin for purification of a fibrinolytic enzyme

Recent advances in purification technologies for therapeutic molecules have stirred the research consortium. Mixed mode chromatography, having multiple interactions with the solute molecule, has drawn significant attention due to its overall advantage over traditional ion-exchange and reverse-phase chromatography. Capto adhere, a mixed mode chromatography resin with strong anion-exchange and reverse-phase interaction with solutes, was explored for purification of fibrinolytic enzyme from Bacillus sphaericus MTCC 3672. Static and dynamic resin binding study revealed that 30°C temperature, pH 8, and 0.5 mL/min flow rate were optimum for maximum binding of fibrinolytic enzyme. Maximum static dynamic binding and breakthrough capacities for Capto adhere were 249 and 196 U/mL of resin, respectively. Final purification with Sephadex G 100 gel chromatography resulted in 38-fold purity of fibrinolytic enzyme with 39% enzyme recovery. Purified enzyme was further characterized by sodium dodecyl sulfate polyacrylamide gel electrophoresis (SDS-PAGE) analysis to homogeneity, and molecular mass was found to be around 55–70 kD. Like most of the serine alkaline proteases, purified fibrinolytic enzyme was stable in a temperature range of 25–40°C and pH range of 7–9. Offshoots of our research findings have revealed a broad application area of mixed mode chromatography.     

Purification and scale-up of a recombinant heavy chain fragment C of botulinum neurotoxin serotype E in Pichia pastoris GS115

A recombinant C-terminus heavy chain fragment from botulinum neurotoxin serotype E (BoNT/E) is proposed as a vaccine against the serotype E neurotoxin. This fragment, rBoNTE(Hc), was produced intracellular in Pichia pastoris GS115 by a three-step fermentation process, i.e., glycerol batch phase and a glycerol fed-batch phase to achieve high cell densities, followed by a methanol fed-batch induction phase. The rBoNTE(Hc) protein was purified from the soluble fraction of cell lysates using three ion-exchange chromatography steps (SP Sepharose Fast Flow, Q Sepharose Fast Flow, Sp Sepharose High Performance) and polished with a hydrophobic charge induction chromatography step (MEP HyperCel). Method development at the bench scale was achieved using 7-380 mL columns and the process was performed at the pilot scale using 0.5-3.1 L columns in preparation for technology transfer to cGMP manufacturing. The purification process resulted in greater than 98% pure rBoNTE(Hc) based on HPLC and yielded up to 1.01g of rBoNTE(Hc)/kg cells at the bench scale and 580mg vaccine/kg cells at the pilot scale. N-terminal sequencing showed that the purified rBoNTE(Hc) N-terminus is intact and was found to protect mice against a challenge of 1000 mouse intraperitoneal LD50's of BoNT/E.     

Investigation of Factors Affecting the Bioregeneration Process for Perchlorate-Laden Gel-Type Anion-Exchange Resin

Ion exchange is the most common process for perchlorate removal from waters. Selective ion-exchange resins are widely used for perchlorate removal from waters, but are incinerated after one-time use, making the ion-exchange process incomplete for perchlorate removal. As perchlorate ions are readily biodegradable, direct contact of spent ion-exchange resins with perchlorate-reducing bacteria for its regeneration has been studied recently. In this research, some factors affecting the bioregeneration of perchlorate-laden gel-type anion-exchange resin were investigated. Bioregeneration is a sustainable process when compared to one-time use of resin and disposal by incineration. Batch bioregeneration experiments were performed to determine (a) the effect of initial perchlorate load in the resin, (b) the effect of microbial concentration, and (c) the effect of nitrate load on the degradation of perchlorate in the resin bead. The results of the bioregeneration tests suggested that the bioregeneration process may be controlled by both kinetics and diffusion. Higher perchlorate load in the resin had a positive effect on perchlorate degradation rates, whereas varying microbial concentration did not have a significant effect on perchlorate degradation in gel-type resin. The presence of nitrate suppressed perchlorate degradation initially, but once all nitrate was utilized, perchlorate degradation took place.     

huGM-CSF(9-127)-IL-6(29-184)融合蛋白的复性及纯化研究

利用Q Sepharose H.P.离子交换柱层析在8mol/L尿素变性条件下对huGM-CSF(9-127)-IL-6(29-184）融合蛋白进行初步纯化,然后再利用Sephacryl S-200分子筛柱层析复性及纯化后获得目的蛋白,其纯度达到95％以上。该纯化方案成功地解决了稀释复性或透析复性产物在进行Q Sepharose H.P.离子交换柱层析时目的蛋白不稳定而沉积于柱上的问题,获得了较好的复性效果,复性率达到80％以上。使用该纯化方案,1天内便可基本完成重组蛋白的复性及纯化过程,而且也便于扩大。     

Evaluation of a novel agarose-based synthetic ligand adsorbent for the recovery of antibodies from ovine serum

This paper evaluates a prototype agarose-based affinity adsorbent utilizing a bound synthetic ligand designed to replace Protein A as an IgG-affinity capture resin and compares its purification characteristics with four commercially available matrices for the recovery of polyclonal antibodies from crude hyperimmune ovine serum. The novel adsorbent was found to show the highest dynamic capacity (29.2 mg/mL) of all matrices under evaluation--30% higher than the other commercial adsorbents evaluated. When using a post-load caprylic acid wash, IgG yields of over 85% and purities of over 90% were achieved consistently over multiple loading cycles. To evaluate bead diffusion, inverted confocal microscopy was used to visualise fluorescent antibody binding on to individual adsorbent beads in real time. The results indicate that the binding characteristics of the prototype adsorbent are similar to those obtained with Protein G Sepharose. This study indicates that the high-capacity prototype matrix is a feasible and potentially cost-effective alternative for the direct capture of antibodies from crude ovine serum and may therefore also be applicable to the purification of other complex industrial feedstocks such as transgenic milk or monoclonal antibodies expressed using recombinant technologies.     

Use of anion-exchange high-performance liquid chromatography for the study of smooth muscle myosin light-chain kinase and its catalytic domain

Avian myosin light-chain kinase from smooth muscle of the gizzard and its catalytic domain, derived from the intact enzyme by trypsin digestion, was purified within 30–40 min by both analytical and preparative anion-exchange high-performance liquid chromatography. The proteins obtained were more than 95% pure and retained their biological activity. The high-performance anion-exchange chromatography protocols represent a significant decrease in purification time when compared with conventional ion-exchange chromatography.     

Large-scale purification of plasmid DNA by fast protein liquid chromatography using a Hi-Load Q Sepharose column.

The large-scale purification of plasmid DNA was achieved using fast protein liquid chromatography on a Hi-Load Q Sepharose column. This method allows for the purification of plasmids starting from crude plasmid DNA, prepared by a simple alkaline lysis procedure, to pure DNA in less than 5 h. In contrast to the previously described plasmid purification methods of CsCl gradient centrifugation or high-pressure liquid chromatography, this method does not require the use of any hazardous or expensive chemicals. More than 100 plasmids varying in size from 3 to 15 kb have been purified using this procedure. A Mono Q Sepharose column was initially used to purify plasmids smaller than 8.0 kb; however, a Hi-Load Q Sepharose column proved more effective with plasmids larger than 8 kb. The loading of plasmids larger than 8 kb on the Mono Q column resulted in a high back pressure and the plasmid DNA could not be eluted from the column. Thus, for routine purification we utilize the Hi-Load Q Sepharose column. Plasmids purified by this method had purity, yield, and transfection efficiency in mammalian cells similar to those of plasmids purified by CsCl density gradient centrifugation.     

A protocol for the purification of bovine serum albumin free of deoxyribonuclease activity

Bovine serum albumin, free of deoxyribonuclease activity, was obtained in our laboratory using ion-exchange chromatography followed by acetylation. Chromatography on four different resins (DEAE-52, P-11, hydroxylapatite and Q Sepharose fast-flow) was examined. Fractions from Q Sepharose chromatography, eluted with a linear gradient 0-1.0 M NaCl and subsequently acetylated, proved to be the most effective method for obtaining deoxyribonuclease-free bovine serum albumin.     

Affinity purification of the voltage-sensitive sodium channel from electroplax with resins selective for sialic acid

The voltage-sensitive sodium channel present in the eel (Electrophorus electricus) has an unusually high content of sialic acid, including alpha-(2----8)-linked polysialic acid, not found in other electroplax membrane glycopeptides. Lectins from Limax flavus (LFA) and wheat germ (WGA) proved the most effective of 11 lectin resins tried. The most selective resin was prepared from IgM antibodies against Neisseria meningitidis alpha-(2----8)-polysialic acid which were affinity purified and coupled to Sepharose 4B. The sodium channel was found to bind to WGA, LFA, and IgM resins and was readily eluted with the appropriate soluble carbohydrates. Experiments with LFA and IgM resins demonstrated binding and unbinding rates and displacement kinetics, which suggest highly specific binding at multiple sites on the sodium channel protein. In preparative-scale purification of protein previously fractionated by anion-exchange chromatography, without stabilizing TTX, high yields were reproducibly obtained. Further, when detergent extracts were prepared from electroplax membranes fractionated by low-speed sedimentation, a single step over the IgM resin provided a 70-fold purification, yielding specific activities of 3200 pmol of [3H]TTX-binding sites/mg of protein and a single polypeptide of approximately 285,000 Da on SDS-acrylamide gels. No small peptides were observed after this 5-h isolation. We further describe a cation-dependent stabilization with millimolar levels of monovalent and micromolar levels of divalent species.     

Hexadecanedionic acid-sepharose 4B: A new tool for preparation of albumin-depleted plasma

Serum and plasma are the major sources of human material for clinical molecular diagnostics and drug discovery. However, due to the high abundance of some proteins, of which serum albumin (SA) is most prominent, lower-abundance proteins often remain undetectable in proteomic analysis of these body fluids. We have used hexadecanedionic acid (HDA) immobilized to Sepharose 4B to develop an affinity resin that is effective in the removal of SA from plasma. Two-dimensional gel analysis of the SA-depleted samples shows a significant enhancement of the low-abundance proteins and highly specific capture of serum albumin. The HDA resin shows better performance in terms of specificity than dye-based resins.     

Purification of cell culture-derived human influenza A virus by size-exclusion and anion-exchange chromatography

A process comprising of size-exclusion chromatography (SEC) and anion-exchange chromatography (AEC) was investigated for downstream processing of cell culture-derived influenza A virus. Human influenza virus A/PR/8/34 (H1N1) was propagated in serum-free medium using MDCK cells as a host. Concentrates of the virus were prepared from clarified and inactivated cell culture supernatants by cross-flow ultrafiltration as described before. SEC on Sepharose 4 FF resulted in average product yields of 85% based on hemagglutination (HA) activity. Productivity was maximized to 0.15 column volumes (cv) of concentrate per hour yielding a reduction in total protein and host cell DNA (hcDNA) to 35 and 34%, respectively. AEC on Sepharose Q XL was used to separate hcDNA from virus at a salt concentration of 0.65 M sodium chloride. Product yields >80% were achieved for loads >160 kHAU/mL of resin. The reduction in hcDNA was 67-fold. Split peak elution and bimodal particle volume distributions suggested aggregation of virions. Co-elution with hcDNA and constant amounts of hcDNA per dose indiciated association of virions to hcDNA. An overall product yield of 52% was achieved. Total protein was reduced more than 19-fold; hcDNA more than 500-fold by the process. Estimation of the dose volume from HA activity predicted a protein content at the limit for human vaccines. Reduction of hcDNA was found insufficient (about 500 ng per dose) requiring further optimization of AEC or additional purification steps. All operations were selected to be scalable and independent of the virus strain rendering the process suitable for vaccine production.     

鲍曼不动杆菌烈性噬菌体的分离与纯化

利用柱层析方法,纯化鲍曼不动杆菌（Acinetobacter baumannii）烈性噬菌体AB1。首先采用聚乙二醇6000沉淀方法,初步分离裂解液中的噬菌体,噬菌体纯度由6.1×1010 pfu/mg提高到37×1010 pfu/mg,噬菌体回收率为58.8%,蛋白质去除率为90.6%;噬菌体粗提样品经Sepharose 4B凝胶过滤层析柱进一步纯化,纯度提高到73×1010 pfu/mg,噬菌体回收率为95.7%,蛋白质去除率为48.1%;收集的噬菌体样品最后经DEAE-52阴离子交换层析柱处理,噬菌体纯度为40×1010 pfu/mg,回收率为50.8%,蛋白去除率15.6%。内毒素分析结果显示,Sepharose 4B凝胶过滤层析纯化的噬菌体样品中,内毒素含量为443.8 EU/mg,而DEAE-52阴离子交换层析纯化的噬菌体样品中,内毒素含量为544.4 EU/mg。实验结果显示,PEG沉淀方法与Sepharose 4B凝胶过滤方法能够有效地提高噬菌体纯度,而DEAE-52阴离子交换层析则不能提高噬菌体的纯度,也无法有效地去除样品中的内毒素。