Downstream processing of human antibodies integrating an extraction capture step and cation exchange chromatography

In this paper we explore an alternative process for the purification of human antibodies from a Chinese hamster ovary (CHO) cell supernatant comprising a ligand-enhanced extraction capture step and cation exchange chromatography (CEX). The extraction of human antibodies was performed in an aqueous two-phase system (ATPS) composed of dextran and polyethylene glycol (PEG), in which the terminal hydroxyl groups of the PEG molecule were modified with an amino acid mimetic ligand in order to enhance the partition of the antibodies to the PEG-rich phase. This capture step was optimized using a design of experiments and a central composite design allowed the determination of the conditions that favor the partition of the antibodies to the phase containing the PEG diglutaric acid (PEG-GA) polymer, in terms of system composition. Accordingly, higher recovery yields were obtained for higher concentrations of PEG-GA and lower concentrations of dextran. The highest yield experimentally obtained was observed for an ATPS composed of 5.17% (w/w) dextran and 8% (w/w) PEG-GA. Higher purities were however predicted for higher concentrations of both polymers. A compromise between yield and purity was achieved using 5% dextran and 10% PEG-GA, which allowed the recovery of 82% of the antibodies with a protein purity of 96% and a total purity of 63%, determined by size-exclusion chromatography. ATPS top phases were further purified by cation exchange chromatography and it was observed that the most adequate cation exchange ligand was carboxymethyl, as the sulfopropyl ligand induced the formation of multi-aggregates or denatured forms. This column allowed the elution of 89% of the antibodies present in the top phase, with a protein purity of 100% and a total purity of 91%. The overall process containing a ligand-enhanced extraction step and a cation exchange chromatography step had an overall yield of 73%.     

Purification Process for the Preparation and Characterizations of Hen Egg White Ovalbumin,Lysozyme, Ovotransferrin,and Ovomucoid

Abstract

In this study, four major egg white proteins were purified by two step ion exchange chromatography followed by precipitation. Lysozyme and ovalbumin were separated with Q Sepharose Fast Flow anion exchange chromatography in the first step, resulting in two peaks of lysozyme and three peaks of ovalbumin with 87% and 70% purity by HPLC, respectively. Ovotransferrin was separated with CM-Toyopearl 650 M cation exchange chromatography in the second step, giving 80% purity. Ovomucoid was precipitated from the partial purified protein fraction from the first two steps, and concentrated in the final step to yield 90% purity. Protein recoveries were estimated to be 55, 21, 54, and 21% for lysozyme, ovotransferrin, ovalbumin, and ovomuciod, respectively. Lysozyme was identified from the purified peaks using zymogram refolding gel, whereas ovalbumin was identified by western blotting. Purified ovotransferrin and ovomucoid was identified by mass spectrometry. The results indicate that this purification process is adequate for preparation of lysozyme, ovalbumin, ovotransferrin, and ovomucoid, at least on a laboratory scale.     

Method for rapid separation of liposome-associated doxorubicin from free doxorubicin in plasma

To understand and predict the efficacy and/or toxicity of liposomal drugs in vivo, it is essential to have rapid, reliable methods of separating and quantitating both the free and the liposomal forms of the drug. A method using solid-phase extraction chromatography columns was developed to separate and quantitate unencapsulated doxorubicin and liposome-associated doxorubicin in plasma following the intravenous injection of liposomal doxorubicin. The method facilitated the recovery and quantitation of free and liposomal drug. The separation and recovery of doxorubicin were linear across the entire range of possible mixtures (0 to 100%) of the two forms of the drug in plasma. Free drug and liposomal drug were readily separated for liposomal doxorubicin systems varying in size (0.1-1.0 microns) and lipid composition (egg yolk phosphatidylcholine/cholesterol and distearylphosphatidylcholine/cholesterol). The method is rapid and allows for multiple samples to be processed simultaneously.     

抗金黄色葡萄球菌卵黄抗体的制备及活性研究

目的:制备金黄色葡萄球菌特异性卵黄抗体并考察其活性。方法:采用灭活的金黄色葡萄球菌免疫产蛋母鸡,通过水稀释法、硫酸铵和硫酸钠盐析及凝胶过滤法分离、纯化抗体。抗体效价测定及体外抑菌试验分别采用酶联免疫吸附法(ELISA)和液体培养基比浊法。结果:纯化所得抗体纯度达95.10%,回收率为20.08%。抗体对金黄色葡萄球菌具有特异性,效价最高可达1:6400。体外抑菌试验表明,抗体抑菌活随IgY浓度的增加而增强,当特异性IgY的浓度为10mg/ml时,能完全抑制细菌生长。结论:抗体制备及纯化所述方法简便、可行,所制抗体具有特异性和抑菌活性。     

The purification of IgY from chicken egg yolk by preparative electrophoresis

Chicken IgY has been purified from egg yolk by preparative electrophoresis on the Gradiflow, a system which has been employed for the purification of a wide range of proteins with high recovery and biological activity. Protein purification on the Gradiflow utilises electrophoresis with selected combinations of porous membranes and buffers. The purification of IgY was achieved by initial PEG lipid precipitation, then a single step Gradiflow run by a strategy based on the relatively high pI range of IgY compared to other egg yolk proteins. The IgY yields obtained from the delipidised supernatant are consistently greater than 80% by immunoassay. The purity of the IgY fraction compared favourably with IgY prepared using three commercial products.     

On-line casein micelle disruption for downstream purification of recombinant human myelin basic protein produced in the milk of transgenic cows

Downstream purification of a model recombinant protein (human myelin basic protein) from milk of transgenic cows is described. The recombinant protein was expressed as a His tagged fusion protein in the milk of transgenic cows and was found associated with the casein micellar phase. While difficulties in obtaining good recoveries were found when employing conventional micelle disruption procedures, direct capture using the cation exchanger SP Sepharose Big Beads? was found successful in the extraction of the recombinant protein. Early breakthrough suggested a slow release of the recombinant protein from the micelles and dictated micelle disruption in order to obtain good yields. A new approach for deconstruction of the calcium core of the casein micelles, employing the interaction between the micellar calcium and the active sites of the cation exchanger resin was developed. Milk samples were loaded to the column in aliquots with a column washing step after each aliquot. This sequential loading approach successfully liberated the recombinant protein from the micelles and was found superior to the conventional sample loading approach. It increased the recovery by more than 25%, reduced fouling due to milk components and improved the column hydrodynamic properties as compared to the conventional sample loading approach. Hardware and software modifications to the chromatography system were necessary in order to keep the whole process automated. A second purification step using a Ni²⁺ affinity column was used to isolate the recombinant protein at purity more than 90% and a recovery percentage of 78%.     

A large-scale purification of paclitaxel from cell cultures of Taxus chinensis

A large-scale purification method was developed for producing paclitaxel, to guarantee high purity and yield from plant cell cultures. The complete method for mass production was a simple and efficient procedure, for the isolation and purification of paclitaxel from the biomass of Taxus chinensis, consisting of solvent extraction, synthetic adsorbent treatment, and two steps of precipitation, followed by two steps of high performance liquid chromatography (HPLC). The organic solvent extraction of biomass obtained crude extract containing paclitaxel. The use of synthetic adsorbent treatment and precipitation in the prepurification process allows for rapid and efficient separation of paclitaxel from interfering compounds and dramatically increases the yield and purity of crude paclitaxel for HPLC purification steps compared to alternative processes. This prepurification process serves to minimise solvent usage, size, and complexity of the HPLC operations for paclitaxel purification. The paclitaxel of over 99.5% purity can be simply obtained with high yield from crude paclitaxel by HPLC using reverse-phase separation on C18 as the first step and normal-phase separation on silica as the second step.     

IgY‐binding peptide screened from a random peptide library as a ligand for IgY purification

Chicken egg yolk immunoglobulin (IgY) is a functional substitute for mammalian IgG for antigen detection. Traditional IgY purification methods involve multi‐step procedures resulting in low purity and recovery of IgY. In this study, we developed a simple IgY purification system using IgY‐specific peptides identified by T7 phage display technology. From disulfide‐constrained random peptide libraries constructed on a T7 phage, we identified three specific binding clones (Y4‐4, Y5‐14, and Y5‐55) through repeated biopanning. The synthetic peptides showed high binding specificity to IgY‐Fc and moderate affinity for IgY‐Fc (K_d: Y4‐4 = 7.3 ± 0.2 μM and Y5‐55 = 4.4 ± 0.1 μM) by surface plasmon resonance analysis. To evaluate the ability to purify IgY, we performed immunoprecipitation and affinity high‐performance liquid chromatography using IgY‐binding peptides; the result indicated that these peptides can be used as affinity ligands for IgY purification. We then used a peptide‐conjugated column to purify IgY from egg yolks pre‐treated using an optimized delipidation technique. Here, we report the construction of a cost‐effective, one‐step IgY purification system, with high purity and recovery. © 2017 The Authors. Journal of Peptide Science published by European Peptide Society and John Wiley & Sons Ltd.     

Extraction of monoclonal antibodies (IgG1) using anionic and anionic/nonionic reverse micelles

Purification schemes for antibody production based on affinity chromatography are trying to keep pace with increases in cell culture expression levels and many current research initiatives are focused on finding alternatives to chromatography for the purification of Monoclonal antibodies (MAbs). In this article, we have investigated an alternative separation technique based on liquid–liquid extraction called the reverse micellar extraction. We extracted MAb (IgG1) using reverse micelles of an anionic surfactant, sodium bis 2‐ethyl‐hexyl sulfosuccinate (AOT) and a combination of anionic (AOT) and nonionic surfactants (Brij‐30, Tween‐85, Span‐85) using isooctane as the solvent system. The extraction efficiency of IgG1 was studied by varying parameters, such as pH of the aqueous phase, cation concentration, and type and surfactant concentration. Using the AOT/Isooctane reverse micellar system, we could achieve good overall extraction of IgG1 (between 80 and 90%), but only 30% of the bioactivity of IgG1 could be recovered at the end of the extraction by using its binding to affinity chromatography columns as a surrogate measure of activity. As anionic surfactants were suspected as being one of the reasons for the reduced activity, we decided to combine a nonionic surfactant with an anionic surfactant and then study its effect on the extraction efficiency and bioactivity. The best results were obtained using an AOT/Brij‐30/Isooctane reverse micellar system, which gave an overall extraction above 90 and 59% overall activity recovery. An AOT/Tween‐85/Isooctane reverse micellar system gave an overall extraction of between 75 and 80% and overall activity recovery of around 40–45%. The results showed that the activity recovery of IgG1 can be significantly enhanced using different surfactant combination systems, and if the recovery of IgG1 can be further enhanced, the technique shows considerable promise for the downstream purification of MAbs. © 2010 American Institute of Chemical Engineers Biotechnol. Prog., 2010     

Affinity purification of immunoglobulins from chicken egg yolk using a new synthetic ligand

Due to the peculiar composition of the egg yolk and the lack of specific affinity ligands, Y immunoglobulins are normally purified using complex and time consuming procedures involving a combination of precipitation and chromatographic steps first to extract and capture and then to polish IgY. In this study, we have examined the applicability for IgY affinity purification of TG19318, a synthetic ligand for immunoglobulin, obtained from the screening of combinatorial libraries, and already characterized for its capability to purify immunoglobulins of class G, M, E and A. Soluble proteins were separated from the lipidic fraction of egg yolk by the water dilution method and loaded on to TG19318 affinity columns prepared by immobilizing the ligand on the commercially available support Emphaze™. In a single chromatographic step TG19318 affinity columns led to an efficient capture of IgY directly from crude samples, and with a purity degree higher than 90%, as determined by densitometric scanning of SDS–PAGE analysis of bound fractions, and with full recovery of antibody activity, as determined by ELISA assay. Higher recovery and purity of IgY was obtained by using loading buffers at pH close to 6.5. Column capacity, determined by applying 4× excess IgY to 1 ml bed volume column, and eluting the retained immunoglobulins, was close to 65 mg of IgY per ml of resin. Chemical and chromatographic stability of TG19318/Emphaze was tested before and after various treatments. The derivatized matrix was found to be very stable, in terms of ligand leakage and maintenance of IgY binding capacity, under conditions of normal column usage, cleaning and storage.     

Low density lipoproteins extracted from hen egg yolk by an easy method: cryoprotective effect on frozen-thawed bull semen

Hen egg yolk is widely used as a cryoprotective agent in semen freezing extenders in order to protect the spermatozoa against cold shock. The protective action of yolk is largely presumed to be due to low density lipoproteins (LDL). In recent years, arguments concerning the presence of cryoprotective antagonists in egg yolk, have reinforced interest in the use of only the LDL extracted from egg yolk in the extenders. However, current methods of LDL purification do not support the use of LDL in commercial extenders because they offer a poor recovery rate. Consequently, we have developed an easy method to extract LDL from egg yolk. Several concentrations of purified LDL (between 2.5 and 20%, w/v) were tested in freezing extenders for bull semen, and compared with commercial extenders. Our extraction method reached 97% purity and about 67% yield, and is easily reproducible on an industrial scale. Analysis of sperm motility showed that the motility and characteristics of spermatozoa movement were improved with LDL in the extender, as compared to a commercial extender containing egg yolk. The optimum LDL concentration in the extender was 8%. In conclusion, we propose that an extender containing LDL extracted from egg yolk could be used as cryoprotective media with a better efficiency than present commercial extenders.     

Simplified NaCl Based (68)Ga Concentration and Labeling Procedure for Rapid Synthesis of (68)Ga Radiopharmaceuticals in High Radiochemical Purity

A simple sodium chloride (NaCl) based (68)Ga eluate concentration and labeling method that enables rapid, high-efficiency labeling of DOTA conjugated peptides in high radiochemical purity is described. The method utilizes relatively few reagents and comprises minimal procedural steps. It is particularly well-suited for routine automated synthesis of clinical radiopharmaceuticals. For the (68)Ga generator eluate concentration step, commercially available cation-exchange cartridges and (68)Ga generators were used. The (68)Ga generator eluate was collected by use of a strong cation exchange cartridge. 98% of the total activity of (68)Ga was then eluted from the cation exchange cartridge with 0.5 mL of 5 M NaCl solution containing a small amount of 5.5 M HCl. After buffering with ammonium acetate, the eluate was used directly for radiolabeling of DOTATOC and DOTATATE. The (68)Ga-labeled peptides were obtained in higher radiochemical purity compared to other commonly used procedures, with radiochemical yields greater than 80%. The presence of (68)Ge could not be detected in the final product. The new method obviates the need for organic solvents, which eliminates the required quality control of the final product by gas chromatography, thereby reducing postsynthesis analytical effort significantly. The (68)Ga-labeled products were used directly, with no subsequent purification steps, such as solid-phase extraction. The NaCl method was further evaluated using an automated fluid handling system and it routinely facilitates radiochemical yields in excess of 65% in less than 15 min, with radiochemical purity consistently greater than 99% for the preparation of (68)Ga-DOTATOC.     

Application of microwave‐assisted extraction coupled with high‐speed counter‐current chromatography for separation and purification of Dehydrocavidine from Corydalis saxicola Bunting

Introduction – Dehydrocavidine is a major component of Corydalis saxicola Bunting with sedative, analgesic, anticonvulsive and antibacterial activities. Conventional methods have disadvantages in extracting, separating and purifying dehydrocavidine from C. saxicola. Hence, an efficient method should be established. Objective – To develop a suitable preparative method in order to isolate dehydrocavidine from a complex C. saxicola extract by preparative HSCCC. Methodology – The methanol extract of C. saxicola was prepared by optimised microwave‐assisted extraction (MAE). The analytical HSCCC was used for the exploration of suitable solvent systems and the preparative HSCCC was used for larger scale separation and purification. Dehydrocavidine was analysed by high‐performance liquid chromatography (HPLC) and further identified by ESI‐MS and 1H NMR. Results – The optimised MAE experimental conditions were as follows: extraction temperature, 60°C; ratio of liquid to solid, 20; extraction time, 15 min; and microwave power, 700 W. In less than 4 h, 42.1 mg of dehydrocavidine (98.9% purity) was obtained from 900 mg crude extract in a one‐step separation, using a two‐phase solvent system composed of chloroform–methanol–0.3 m hydrochloric acid (4 : 0.5 : 2, v/v/v). Conclusion – Microwave‐assisted extraction coupled with high‐speed counter‐current chromatography is a powerful tool for extraction, separation and purification of dehydrocavidine from C. saxicola. Copyright © 2009 John Wiley & Sons, Ltd.     

Isocratic separation of PTH-amino acids at picomole level by reverse-phase HPLC in the presence of sodium dodecylsulfate

The phenylthiohydantoin (PTH) derivatives of protein amino acids have been separated by reverse-phase high performance liquid chromatography (HPLC) on a fully end-capped C18 column using an isocratic solvent system. The developing solvent was 0.01 M sodium acetate buffer (pH 4.5) containing 39.5% acetonitrile and 0.02% sodium dodecylsulfate (SDS). With an automated liquid chromatography equipped with a dual-channel detector, operating at 254 and 313 nm, the present isocratic separation system was quite useful for routine microanalysis of PTH-amino acids released with a "gas-phase" sequencer. The time for one run was approximately 23 min and the limit of analysis approximately 2.5 pmol of a PTH-amino acid.     

High‐throughput process development of purification alternatives for the protein avidin

With an increased number of applications in the field of the avidin‐biotin technology, the resulting demand for highly‐purified protein avidin has drawn our attention to the purification process of avidin that naturally occurs in chicken egg white. The high‐throughput process development (HTPD) methodology was exploited, in order to evaluate purification process alternatives to commonly used ion‐exchange chromatography. In a high‐throughput format, process parameters for aqueous two‐phase extraction, selective precipitation with salts and polyethylene glycol, and hydrophobic interaction and mixed‐mode column chromatography experiments were performed. The HTPD strategy was complemented by a high‐throughput tandem high‐performance liquid chromatography assay for protein quantification. Suitable conditions for the separation of avidin from the major impurities ovalbumin, ovomucoid, ovotransferrin, and lysozyme were identified in the screening experiments. By combination of polyethylene glycol precipitation with subsequent resolubilization and separation in a polyethylene glycol/sulfate/sodium chloride two‐phase system an avidin purity of 77% was obtained with a yield >90% while at the same time achieving a significant reduction of the process volume. The two‐phase extraction and precipitation results were largely confirmed in larger scale with scale‐up factors of 230 and 133, respectively. Seamless processing of the avidin enriched bottom phase was found feasible by using mixed‐mode chromatography. By gradient elution a final avidin purity of at least 97% and yield >90% was obtained in the elution pool. The presented identification of a new and beneficial alternative for the purification of the high value protein thus represents a successful implementation of HTPD for an industrially relevant purification task. © 2015 American Institute of Chemical Engineers Biotechnol. Prog., 31:957–973, 2015     

Application of analytical and preparative high-speed counter-current chromatography for the separation of Z-ligustilide from a crude extract of Angelica sinensis

Z-Ligustilide was separated and purified from the traditional Chinese medicinal plant Angelica sinensis by high-speed counter-current chromatography (HSCCC). Analytical HSCCC was first used for the systematic selection of the two-phase solvent system. Preparative HSCCC separation was performed with a two-phase solvent system composed of petroleum ether (60-90 degrees C)-ethanol-water at an optimum volume ratio of 10:17:10 (v/v). A total of 38 mg Z-ligustilide at 98.8% purity was obtained in one step from 200 mg crude extract as determined by HPLC analysis. The structure of the target compound was identified by electron impact ionisation mass spectrometry.     

One-step purification of proteins from chicken egg white using counter-current chromatography

Proteins present in chicken egg white are separated by counter-current chromatography (CCC) in one step using a cross-axis coil planet centrifuge (X-axis CPC). The separation was performed with an aqueous polymer two-phase system composed of 16% (w/w) poly(ethylene glycol) 1000 and 12.5% (w/w) dibasic potassium phosphate by eluting the lower phase at a flow-rate of 1.0 ml/min. From about 20 g of the crude egg white solution, lysozyme, ovalbumin, and ovotransferrin were resolved within 5.5 h. Each component was identified by 12% SDS gel electrophoresis with Coomassie brilliant blue staining.     

Studies of the egg proteins of tropical lizards: purification and partial characterization of yolk proteins of Anolis pulchellus

An easy biochemical procedure for the isolation of lizard lipoprotein is presented as well as the partial characterization of several egg proteins from tropical lizards. In Anolis pulchellus the egg content which is very yolky is homogeneously distributed throughout the egg with no apparent presence of an egg-white. Nevertheless, after resuspension in 0.02 M glycine (pH 7.2), a yolk pellet and a fraction with soluble proteins were separated by low-speed centrifugation. By chromatography in Sephadex G-100, the major egg yolk protein (S-1) was highly purified. This protein was characterized as a glyco-lipo-phosphoprotein with a mol wt of 110,000-120,000 as shown by SDS PAGE. By DEAE cellulose chromatography two acidic proteins (D-5; D-6) were purified (Mr = 62,000-66,000), which do not seem to be components of the yolk granules. Protein D-5 was shown to be a Fe2+-binding protein. By immunochemistry, the liver was found to be the site of synthesis of S-1 and D-5; both proteins are female specific. It is also demonstrated that S-1 shares several chemical and structural properties with the lipovitellins from other oviparous animals.     

Preparation ofN-acetylneuraminic acid from delipidated egg yolk

Egg yolk, a large proportion of the egg, was studied for the preparation ofN-acetylneuraminic acid (Neu5Ac). The delipidated hen egg yolk (DEY; 500 kg containing 0.2% w/w, Neu5Ac) was hydrolysed with HCl (pH 1.4) at 80 °C and neutralized with NaOH (pH 6.0). The mixture was filtered and electrodialysed until the conductivity was 240 µS cm^–1. The filtrate was applied on a column of Dowex HCR-W2 (20–50 mesh), followed by a column of Dowex 1-X8 (200–400 mesh). The latter column was washed with water, and then eluted with a linear gradient of HCO₂H (0–2m). The eluates containing Neu5Ac were concentrated using a reverse osmosis membrane and, finally, rotary evaporated at 40 °C. The residue was then lyophilized to yield 500 g Neu5Ac. The purity of Neu5Ac was >98% (TBA method). HPLC, NMR spectroscopy and TLC chromatography of the product obtained from the DEY showed that Neu5Ac was the sole derivative present in egg yolk. The DEY, a byproduct from egg processing plants, was found to be an excellent source for the large-scale preparation of Neu5Ac.Abbreviations Neu5Ac N-acetylneuraminic acid - Neu5Gc N-glycolylneuraminic acid - DEY delipidated egg yolk - HPLC high performance liquid chromatography - TLC thin layer chromatography - NMR nuclear magnetic resonance - IR infrared spectroscopy Presented at the 11th International Symposium on Glycoconjugates, Toronto, Canada.     

Determination of benzimidazole residues using liquid chromatography and tandem mass spectrometry

The determination of residues of benzimidazole using liquid chromatography and tandem mass spectrometry (LC–MS–MS) with ion spray ionization is described. Swine muscle tissue was spiked with a mixture of fifteen benzimidazoles, including metabolites of fenbendazole and albendazole. As clean-up procedure, an ethyl acetate extraction followed by solid-phase extraction on styrol-divinyl-benzene cartridge was used. The evaluation was performed by selecting the characteristic product ions for the benzimidazoles and using multiple reaction mode. 2-n-Butylmercaptobenzimidazole was used as internal standard. Blank muscle samples were fortified in the concentration range of 1–22 μg/kg. The limits of detection were below 6 μg/kg and the limits of quantification for most benzimidazoles were below 10 μg/kg. The matrix effect was checked using spiked muscle tissues of cattle and sheep as well as liver of cattle. Practical application will be shown by incurred egg material from laying hens treated with flubendazole. The recovery of the clean-up was mostly above 50% in muscle tissue and 70% in egg yolk.