Recovery of a monoclonal antibody from hybridoma culture supernatant by affinity precipitation with Eudragit S-100

An IgG₁ monoclonal antibody (MAB) was isolated from hybridoma culture supernatant by affinity precipitation with an Eudragit S-100-based heterobifunctional ligand. Affinity binding was performed in a homogeneous aqueous phase at pH 7.5 followed by precipitation of the bound affinity complex by lowering the pH to 4.8. After two washing steps, elution of specifically bound MAB was achieved by incubating the precipitate with 0.1 M glycine.HCl pH 2.5. The influence of elution volume and time on the recovery of active MAB and the overall purification factor were studied. The best conditions enabled the recovery of 50.2% of active MAB with a purification factor of 6.2. A further dialysis against 50 mM Tris.HCl pH 8.0 increased the activity yield and the purification factor to 68.4% and 8.3, respectively. This result showed that part of the antibody activity loss during affinity precipitation was due to a reversible inactivation process, being easily recovered after a refining dialysis step.     

Purification of recombinant protein A by aqueous two-phase extraction integrated with affinity precipitation

Aqueous two-phase extraction incorporated affinity precipitation was examined as a technique for protein purification. An enteric coating polymer, Eudragit S100, was employed as a ligand carrier. Eudragit was specifically partitioned to the top phase in the aqueous two-phase systems. For application of this method to purification of recombinant protein A using human IgG coupled to Eudragit in an aqueous two-phase system, 80% of protein A added was recovered with 81% purity. The purity was enhanced 26-fold by thid method. The IgG-Eudragit could be used repeatedly for the purification process. This seperation method should be applicable to industrial-scale purification as a new purification procedure combining the advantages and compensating for the disadvantages of the aqueous two-phase method and affinity precipitation method. (c) 1992 John Wiley & Sons, Inc.     

Eudragit S-100对人转化生长因子β1（TGF-β1）复性的促进作用及其机制

本研究主要是考察一种对pH较为敏感的多聚化合物聚丙烯酸树脂Eudragit S-100是否对人转化生长因子β1（Transforwing growth factor,TGF-β1）复性具有促进作用. 将以包涵体形式存在TGF-β1进行变性,并将变性蛋白直接加入到含有不同浓度Eudragit的蛋白复性缓冲液中,采用MTT法、荧光分光光度法、圆二色谱以及高效液相色谱法等方法来比较分析不同浓度Eudragit S-100对变性TGF-β1的复性促进作用.实验结果表明,在Eudragit S-100作用下TGF-β1的复性产率比普通稀释复性法显著增高且最高达到53%,研究还表明Eudragit S-100的促进蛋白复性的作用是基于Eudragit S-100与TGF-β1发生了特异性的离子结合反应.通过这一反应,Eudragit S-100遮蔽了蛋白多肽间的疏水基团,有效的抑制了蛋白的聚集进而发挥其促复性功能.     

Interfacing Pichia pastoris cultivation with expanded bed adsorption

For improved interfacing of the Pichia pastoris fed-batch cultivation process with expanded bed adsorption (EBA) technique, a modified cultivation technique was developed. The modification included the reduction of the medium salt concentration, which was then kept constant by regulating the medium conductivity at low value (about 8 mS/cm) by salt feeding. Before loading, the low conductivity culture broth was diluted only to reduce viscosity, caused by high cell density. The concept was applied to a one-step recovery and purification procedure for a fusion protein composed of a cellulose-binding module (CBM) from Neocallimastix patriciarum cellulase 6A fused to lipase B from Candida antarctica (CALB). The modified cultivation technique resulted in lower cell death and consequently lower concentration of proteases and other contaminating proteins in the culture broth. Flow cytometry analysis showed 1% dead (propidium-stained) cells compared to 3.5% in the reference process. During the whole process of cultivation and recovery, no proteolysis was detected and in the end of the cultivation, the product constituted 87% of the total supernatant protein. The lipase activity in the culture supernatant increased at an almost constant rate up to a value corresponding to 2.2 g/L of CBM-CALB. In the EBA process, no cell-adsorbent interaction was detected but the cell density had to be reduced by a two-times dilution to keep a proper bed expansion. At flow velocity of 400 cm/h, the breakthrough capacity was 12.4 g/L, the product yield 98%, the concentration factor 3.6 times, the purity about 90%, and the productivity 2.1 g/L x h.     

Simultaneous refolding/purification of xylanase with a microwave treated smart polymer

Affinity precipitation with a smart polymer, Eudragit S-100 (a methyl methacrylate polymer), was exploited for simultaneous refolding and purification of xylanase. Affinity precipitation consisted of this reversibly soluble-insoluble polymer-binding xylanase selectively. The complex was precipitated by lowering the pH and xylanase was eluted off the polymer using 1 M NaCl. For refolding experiments, the commercial preparation of Aspergillus niger xylanase was denatured with 8 M urea. Addition of microwave irradiated Eudragit S-100 and affinity precipitation led to recovery of 96% enzyme activity by refolding. Simultaneously, the enzyme was purified 45 times. Thermally inactivated preparation, when subjected to similar steps, led to 95% recovery of enzyme activity with 42-fold purification. The strategy has the potential for recovering pure proteins in active forms from overexpressed proteins, which generally form inclusion bodies in E. coli.     

Lipase from Pseudomonas fragi. I. Purification of the Enzyme

The experimental conditions required to isolate a lipase from Pseudomonas fragi were determined. The organism was grown in a buffered tryptone medium for 4 to 5 days at 20 C. The lipase in the culture supernatant fluid was isolated by fractionation with ammonium sulfate at 60% saturation, followed by acetone precipitation at 30-60% concentration. Further purification was made by using Sephadex G-200 gel-filtration and diethylaminoethyl cellulose chromatography. Electrophoretic analysis of the purified lipolytic fraction showed apparent homogeneity by both cellulose polyacetate and disc electrophoresis. The specific activity of the purified enzyme was about 100 times that of the starting culture filtrate, and the yield was about 1.8% of the original activity.     

Optimisation of aqueous two-phase extraction of human antibodies

The purification of human antibodies in an aqueous two-phase system (ATPS) composed of polyethylene glycol (PEG) 6000 and phosphate was optimised by surface response methodology. A central composite design was used to evaluate the influence of phosphate, PEG and NaCl concentration and of the pH on the purity and extraction yield of IgG from a simulated serum medium. The conditions that maximise the partition of IgG into the upper phase were determined to be high concentrations of NaCl and PEG, low concentrations of phosphate and low pH values. An ATPS composed of 12% PEG, 10% phosphate, 15% NaCl at pH 6 was further used to purify human monoclonal antibodies from a Chinese Hamster Ovary (CHO) concentrated cell culture supernatant with a recovery yield of 88% in the upper PEG-rich phase and a purification factor of 4.3. This ATPS was also successfully used to purify antibodies from a hybridoma cell culture supernatant with a recovery yield of 90% and a purification factor of 4.1.     

Capture of human monoclonal antibodies from cell culture supernatant by ion exchange media exhibiting high charge density

A shortcut purification sequence for therapeutic proteins should consist of three steps: capture, purification, and polishing. Special emphasis has been put on direct capture of human monoclonal antibodies from culture supernatants with ion-exchangers avoiding pretreatment steps such as desalting, dilution, and other means to reduce the ionic strength. CM-HyperD, a cation-exchanger composed of an inorganic macroporous support filled with a viscoelastic gel with a high charge density was used. Capture of monoclonal antibodies from clarified hybridoma cell culture grown in media supplemented with fetal calf serum was investigated. Screening of different pH conditions and buffers for the load step showed that monoclonal antibodies were efficiently bound by CM-HyperD at pH 4.0 and 5.0 at an ionic strength equivalent to culture supernatant. Combination of negative purification with Q-Sepharose FF and capturing with CM-HyperD gave sufficient yield and resolution. Implementation of wash steps with higher conductivity did not improve the purity, but decreased the yield. Interestingly, high flow rates improved the purity. When antibodies were captured from serumfree culture supernatant the antibody could be eluted in a single peak with substantial reduction of contaminants. Capturing of antibodies by ion-exchange sorbents from culture supernatant is possible despite the high salt content.     

Application of calcium phosphate flocculation in high-density cell culture fluid with high product titer of monoclonal antibody

The calcium phosphate [Ca₃(PO4)₂] precipitation was used for improving the clarification efficiency in harvest process of the monoclonal antibody (mAb) containing cell culture fluid (CCF) with high turbidity and product titer. The flocculation conditions (concentration, addition order of flocculants, pH, and operation time), and the effect of flocculants on the mAb physical chemical properties (such as distribution of charge variants and aggregates) and process-related impurities removal (such as DNA and CHOP) were evaluated in this study. The results showed that the turbidity of CCF supernatant was significantly reduced at pH 7, 120 min with addition of phosphate ions first, while a high mAb recovery yield was kept in the CCF supernatant after flocculation. Addition of calcium ions at 15–60 mM was sufficient for flocculation in this study. A relationship between turbidity/mAb recovery yield and the concentration of calcium ions was established. More than 85% DNA in the CCF were effectively removed by the addition of optimal concentration of flocculants. Flocculation process of Ca₃(PO4)₂ is an effective pretreatment method in purification processes of mAbs from the CCF with high turbidity and product titer.

     

Isolation and Purification of Staphylococcal Lipase

An extracellular lipase was isolated from the cell-free supernatant fluid of a 24-hr culture of Staphylococcus aureus grown in Trypticase Soy Broth at 37 C with continuous agitation. The purification was achieved by precipitation with alcohol followed by differential precipitation at pH 8.6 and 4.3. Subsequent purification with Sephadex G 200 and BioGel 300 yielded a preparation which showed a 350- to 450-fold increase in specific activity over the original cell-free supernatant fluid. The purified lipase was homogeneous over a BioGel 300 column and showed a single peak on electrophoresis in a Veronal buffer (pH 8.6, Γ/2 = 0.1). The electrophoretic mobility was -7.78 × 10^-5 cm² per v per sec.     

Purification and characterization of monoclonal antibodies against the free α-subunit of human chorionic gonadotrophin

Monoclonal antibodies (Mabs) against human chorionic gonadotropin hormone (hCG) were raised by hybridoma technology using Sp2/0 myeloma cells as fusion partner. Sixty-five percent of the total culture wells exhibited hybrid growth and 8% of the total wells (13 culture wells) contained anti-hCG secreting hybrids. A positive hybrid cell line secreting antibodies against the free alpha-subunit of hCG was cloned twice by limiting dilution method and eighty four clones were obtained that secreted monoclonal antibodies anti-alpha hCG. One of these hybridoma clones (1C4) secreting monoclonal antibodies against the free alpha-subunit of hCG was selected for purification and characterization purposes. This hybridoma cell line secreted monoclonal antibodies of IgG1 subclass, which were purified by affinity chromatography on Protein A Sepharose CL-4B column with a final relative recovery of antibody activity of 75% and a purification factor of about 12. The purified preparation was analyzed by SDS-PAGE, native PAGE, and IEF. Specificity studies of this Mab revealed that it recognized specifically an epitope on the free alpha-subunits of hCG, FSH, LH, and TSH as determined by enzyme immunoassays. On the other hand, this Mab exhibited crossreactivity with other pituitary hormones either as free subunits or intact molecules as follows: alpha hCG 100%; intact hCG 1.8%; beta hCG 0.14%; alpha FSH 24.5%; intact FSH 0.8%; beta FSH 0.09%; alpha LH 20.5%; intact LH 0.9%; beta LH 0.08%; alpha TSH 50.5%; intact TSH 3.7%; beta TSH 0.07%; The affinity constant (K) of this Mab with respect to free alpha-subunit of hCG was found to be 1.5 x 10(7) I/mol as determined by the simple antibody dilution analysis method.     

Caprylic acid precipitation method for impurity reduction: An alternative to conventional chromatography for monoclonal antibody purification

We report the use of caprylic acid based impurity precipitation as (1) an alternative method to polishing chromatography techniques commonly used for monoclonal antibody purification and (2) an impurity reduction step prior to harvesting the bioreactor. This impurity reduction method was tested with protein A purified antibodies and with cell culture fluid. First, the operational parameters influencing precipitation of host cell proteins and high molecular weight aggregate in protein A pools were investigated. When used as a polishing step, the primary factor affecting purification and yield was determined to be pH. Caprylic acid precipitation was comparable to polishing IEX chromatography in reducing host cell protein and aggregate levels. A virus reduction study showed complete clearance of a model retrovirus during caprylic acid precipitation of protein A purified antibody. Caprylic acid mediated impurity precipitation in cell culture showed that the impurity clearance was generally insensitive to pH and caprylic acid concentration whereas yield was a function of caprylic acid concentration. Protein A purification of caprylic acid precipitated cell culture fluid generated less turbid product pool with reduced levels of host cell proteins and high molecular weight aggregate. The results of this study show caprylic acid precipitation to be an effective purification method that can be incorporated into a production facility with minimal cost as it utilizes existing tanks and process flow. Eliminating flow through chromatography polishing step can provide process intensification by avoiding the process tank volume constraints for high titer processes. Biotechnol. Bioeng. 2012; 109: 2589–2598. © 2012 Wiley Periodicals, Inc.     

Using precipitation by polyamines as an alternative to chromatographic separation in antibody purification processes

Polyamine precipitation conditions for removing host cell protein impurities from the cell culture fluid containing monoclonal antibody were studied. We examined the impact of polyamine concentration, size, structure, cell culture fluid pH and ionic strength. A 96-well microtiter plate based high throughput screening method was developed and used for evaluating different polyamines. Polyallylamine, polyvinylamine, branched polyethyleneimine and poly(dimethylamine-co-epichlorohydrin-ethylenediamine) were identified as efficient precipitants in removing host cell protein impurities. Leveraging from the screening results, we incorporated a polyamine precipitation step into a monoclonal antibody purification process to replace the Protein A chromatography step. The optimization of the overall purification process was performed by taking the mechanisms of both precipitation and chromatographic separation into account. The precipitation-containing process removed a similar amount of process-related impurities, including host cell proteins, DNA, insulin and gentamicin and maintained similar product quality in respect of size and charge variants to chromatography based purification. Overall recovery yield was comparable to the typical Protein A affinity chromatography based antibody purification process.     

Towards protein crystallization as a process step in downstream processing of therapeutic antibodies: screening and optimization at microbatch scale

Crystallization conditions of an intact monoclonal IgG4 (immunoglobulin G, subclass 4) antibody were established in vapor diffusion mode by sparse matrix screening and subsequent optimization. The procedure was transferred to microbatch conditions and a phase diagram was built showing surprisingly low solubility of the antibody at equilibrium. With up-scaling to process scale in mind, purification efficiency of the crystallization step was investigated. Added model protein contaminants were excluded from the crystals to more than 95%. No measurable loss of Fc-binding activity was observed in the crystallized and redissolved antibody. Conditions could be adapted to crystallize the antibody directly from concentrated and diafiltrated cell culture supernatant, showing purification efficiency similar to that of Protein A chromatography. We conclude that crystallization has the potential to be included in downstream processing as a low-cost purification or formulation step.     

Mechanism of pH‐sensitive polymer‐assisted protein refolding and its application in TGF‐β1 and KGF‐2

Refolding of proteins at high concentrations often results in non‐productive aggregation. This study, through a unique combination of spectroscopic and chromatographic analyzes, provides biomolecular evidence to demonstrate the ability of Eudragit S‐100, a pH‐responsive polymer, to enhance refolding of denatured‐reduced lysozyme at high concentrations. The addition of Eudragit in the refolding buffer significantly increases lysozyme refolding yield to 75%, when dilution refolding was conducted at 1 mg/mL lysozyme. This study shows evidence of an electrostatic interaction between oppositely charged lysozyme and the Eudragit polymer during refolding. This ionic complexing of Eudragit and lysozyme appears to shield exposed hydrophobic residues of the lysozyme refolding intermediates, thus minimizing hydrophobic‐driven aggregation of the molecules. Importantly, results from this study show that the Eudragit‐lysozyme bioconjugation does not compromise refolded protein structure, and that the polymer can be readily dissociated from the protein by ion exchange chromatography. The strategy was also applied to refolding of TGF‐β1 and KGF‐2. © 2009 American Institute of Chemical Engineers Biotechnol. Prog. 2009     

Effect of polymer concentration on recovery of the target proteins in precipitation methods

Summary The effect of polymer (Eudragit S-100) concentrations on the recovery of proteins was studied in the affinity precipitation experiments. Proteins/enzymes were precipitated quantitatively at all polymer concentrations used (0.05 – 1%). The polymer concentrations used had remarkable effect on the recovery of the precipitated proteins.     

Evaluation of immobilized metal membrane affinity chromatography for purification of an immunoglobulin G1 monoclonal antibody

The large scale production of monoclonal antibodies (McAbs) has gaining increased relevance with the development of the hybridoma cell culture in bioreactors creating a need for specific efficient bioseparation techniques. Conventional fixed bead affinity adsorption commonly applied for McAbs purification has the drawback of low flow rates and colmatage. We developed and evaluated a immobilized metal affinity chromatographies (IMAC) affinity membrane for the purification of anti-TNP IgG(1) mouse McAbs. We immobilized metal ions on a poly(ethylene vinyl alcohol) hollow fiber membrane (Me(2+)-IDA-PEVA) and applied it for the purification of this McAbs from cell culture supernatant after precipitation with 50% saturation of ammonium sulphate. The purity of IgG(1) in the eluate fractions was high when eluted from Zn(2+) complex. The anti-TNP antibody could be eluted under conditions causing no loss of antigen binding capacity. The purification procedure can be considered as an alternative to the biospecific adsorbent commonly applied for mouse IgG(1) purification, the protein G-Sepharose.     

Establishment and validation of an immunoenzymatic assay to determine mouse IgG levels based on a rat monoclonal antibody

In this paper we describe an immunoenzymatic assay based on a rat monoclonal antibody (Ram kappa) developed to determine mouse IgG concentration, which is widely used for samples obtained on purification processes, like supernatant waste and the content of IgG in the vaccine (rHBsAg). This assay involves the use of a rat antibody-horseradish peroxidase-conjugated for the revealing of the antigen-antibody reaction. The rat antibody was produced in cell culture using a dialysis tube (DT). The immunoassay was standardized following several concepts, such as specificity, precision, and linearity. The result obtained permitted us to replace the use of polyclonal antibodies to determine the kappa light chain mouse antibodies by a rat monoclonal antibody of high sensibility and reproducibility. The assay permitted a reliable measurement of murine kappa Ig up to 0.68 ng/ml and was capable of quantifying 6.25 ng/ml. Due to the high frequency of the kappa light chain in mouse antibodies this system acquires a great application.     

Paper-PEG-based membranes for hydrophobic interaction chromatography: purification of monoclonal antibody

This article discusses the preparation of novel Paper-PEG interpenetrating polymer network-based membranes as inexpensive alternative to currently available adsorptive membranes. The Paper-PEG membranes were developed for carrying out hydrophobic interaction membrane chromatography (HIMC). PEG is normally very hydrophilic but can undergo phase separation and become hydrophobic in the presence of high antichaotropic salt concentrations. Two variants of the Paper-PEG membranes, Paper-PEG 1 and Paper-PEG 2 were prepared by grafting different amounts of the polymer on filter paper and these were tested for their hydraulic properties and antibody binding capacity. The better of the two membranes (Paper-PEG 1) was then used for purifying the monoclonal antibody hIgG1-CD4 from simulated mammalian cell culture supernatant. The processing conditions required for purification were systematically optimized. The dynamic antibody binding capacity of the Paper-PEG 1 membrane was about 9 mg/mL of bed volume. A single step membrane chromatographic process using Paper-PEG 1 membrane gave high monoclonal antibody purity and recovery. The hydraulic permeability of the paper-based membrane was high and was maintained even after many runs, indicating that membrane fouling was negligible and the membrane was largely incompressible.     

Preliminary application of light-pH sensitive recycling aqueous two-phase systems to purification of lipase

One key problem of aqueous two-phase systems (ATPS) is that phase-forming polymers could not be recycled efficiently. This results in high cost and environmental pollution. In this study, we introduced novel aqueous two-phase systems which are composed by pH-sensitive polymer P_ADB and light-sensitive polymer P_NNC. P_NNC is enriched in the top phase while P_ADB is found in the bottom phase. And recoveries of two-phase-forming polymers can both reach over 96%. This aqueous two-phase system was used for purification of lipase from its crude material. The influences of various process parameters such as concentration of the phase-forming polymer, system pH, different types and concentrations of neutral salts on partitioning of lipase are evaluated. It has been found that partition coefficient of pure lipase could reach 0.061 under optimized conditions. Lipase from crude material was purified with 83.7% recovery and a purification factor of approximately 18 folds.