Purification of ascitic fluid-derived murine monoclonal antibodies by anion-exchange and size-exclusion high-performance liquid chromatography

Ascitic fluid-derived murine monoclonal antibodies (MoAbs) of immunoglobulin (Ig) M and IgG isotypes (IgG1 and IgG2a subisotypes) were previously prepared against an isolate of Actinobacillus sp (CAs8C) for the purpose of identifying and characterizing outer membrane antigens on this bacterium. An attempt was made to purify these MoAbs by anion-exchange and size exclusion high-performance liquid chromatography (HPLC). Hybridomas producing the IgG1 and IgG2a MoAbs posed unique difficulties in that they also secreted irrelevant IgG2b MoAbs that were present in the ascitic fluids. Anion-exchange chromatography (Protein-Pak DEAE-5PW column), with a simultaneous change in gradients of pH and ionic strength, was used to purify IgG and as a first step in the purification of IgM. There was good separation of IgG2b from IgG2a, but not from IgG1. Size-exclusion chromatography (Protein-Pak 300 SW column) was required to complete the purification of IgM. The presence of MoAbs in the HPLC fractions was confirmed by discontinuous gradient polyacrylamide gel electrophoresis (denatured and either reduced or non-reduced conditions) and the enzyme-linked immunosorbent assay. HPLC-purified MoAbs were free from transferrin and albumin and retained their specificity for As8C.     

High-performance liquid affinity chromatography for the purification of immunoglobulin A from human serum using jacalin

A high-performance liquid affinity chromatographic method for the purification of serum immunoglobulin A (IgA) using a jacalin column is described. The automated procedure takes about 2 with minimal manipulation. The yields of the isolated IgA and of its IgG and IgM contamination were studied by enzyme-linked immunosorbent assay (ELISA) of 30 sera. Purity was assured by immunoelectrophoresis. The ratio of IgA1 to total IgA was unchanged after purification, as verified by ELISA. The results showed that greater than 90% IgA could be recovered with less than 0.5% total IgG and greater than 2.0% total IgM remaining in the fractions containing purified IgA.     

Selectivity of monolithic supports under overloading conditions and their use for separation of human plasma and isolation of low abundance proteins

Human serum albumin (HSA) and immunoglobulin G (IgG) represent over 75% of all proteins present in human plasma. These two proteins frequently interfere with detection, determination and purification of low abundance proteins that can be potential biomarkers and biomarker candidates for various diseases. Some low abundance plasma proteins such as clotting factors and inhibitors are also important therapeutic agents. In this paper, the characterization of ion-exchange monolithic supports under overloading conditions was performed by use of sample displacement chromatography (SDC). If these supports were used for separation of human plasma, the composition of bound and eluted proteins in both anion- and cation-exchange mode is dependent on column loading. Under overloading conditions, the weakly bound proteins such as HSA in anion-exchange and IgG in cation-exchange mode are displaced by stronger binding proteins, and this phenomenon was not dependent on column size. Consequently, small monolithic columns with a column volume of 100 and 200 μL are ideal supports for high-throughput screening in order to develop new methods for separation of complex mixtures, and for sample preparation in proteomic technology.     

Automated flow immunoassay for detection of food allergen using anion-exchange resin and alkaline phosphatase conjugated immunoglobulin G

A novel automated flow immunoassay system is developed for the detection of wheat protein as a food allergen. A polyclonal immunoglobulin G (IgG) antibody was isolated from serum of a rat with a wheat allergy, then reductively treated using dithiothreitol and covalently coupled to alkaline phosphatase. This conjugate was used in a non-competitive binding assay. The automated system was equipped with an immunoreaction column, an anion-exchange column, a luminescent reaction column and a photodetector. Antibody–antigen complexes were separated from their free conjugate on the basis of a difference in isoelectric point (pI) by an anion-exchange column. This simple technique permits the assay of wheat-protein allergen in 25 min with a reliable detection limit of 5 μg/ml. The anion-exchange column was regenerated by occasional elution with N-methylpiperazine buffer (pH 5.0) containing 0.5 M NaCl, to remove free conjugate. Free conjugate recovered in this manner could be reused up to four times without significant decrease in sensitivity of the immunoassay.     

High Performance Liquid Chromatography of Mouse Monoclonal Antibodies on Spherical Hydroxyapatite Beads

Abstract

High performance liquid chromatography (HPLC) on newly developed spherical beads of hydroxyapatite was applied for the simple purification of monoclonal antibodies (mAbs) secreted into mouse ascitic fluid. Sixteen mAbs including all four subclasses of IgG and IgM were separated successfully from serum albumin a major contaminant in the crude mAb preparation by a 30 min-linear gradient of phosphate ion concentration from 0.01M-0.3M at pH 7.2. Not only IgG mAbs but also IgM mAbs were quantitatively eluted from the column. Each antibody had a different retention time (apparent capacity factor of 2.24–4.14) in the chromatography and no relation was found between the retention time and the type of immunoglobulin (class or subclass). A monomeric form of IgM was also resolved successfully from IgM (pentamer) after its reduction with dithiothreitol; the monomer form of IgM was eluted from the column by a lower concentration of phosphate ion than was the pentamer. These results indicate that HPLC on the hydroxylapatite beads will be useful for the purification and characterization of mouse mAbs.     

Engineering of a two-step purification strategy for a panel of monoclonal immunoglobulin M directed against undifferentiated human embryonic stem cells

A two-step purification strategy comprising of polyethylene glycol (PEG) precipitation and anion-exchange chromatography was developed for a panel of monoclonal immunoglobulin M (IgM) (pI 5.5–7.7) produced from hybridoma cultures. PEG precipitation was optimized with regards to concentration, pH and mixing. For anion-exchange chromatography, different resins were screened of which Fractogel EMD, a polymer grafted porous resin had the highest capacity. Despite its significantly slower mass transfer, the binding capacity was still higher compared to a convection driven resin (monolith). This purification strategy was successfully demonstrated for all 9 IgMs in the panel. In small scale most antibodies could be purified to >95% purity with the exception of two which gave a lower final purity (46% and 85%). The yield was dependent on the different antibodies ranging from 28% to 84%. Further improvement of recovery and purity was obtained by the digestion of DNA present in the hybridoma supernatant using an endonuclease, benzonase. So far this strategy has been applied for the purification of up to 2 l hybridoma supernatants.     

Effects of peptide density and elution pH on affinity chromatographic purification of human immunoglobulins A and M

A family of linear hexamer peptide ligands HWRGWV, HYFKFD and HFRRHL, initially identified for their affinity to the Fc portion of human immunoglobulin G (hIgG), also have potential for use in the purification of human immunoglobulins A (hIgA) and M (hIgM). HWRGWV demonstrated the strongest binding affinity to hIgM, followed by hIgA and hIgG respectively. The effects of N-terminal acetylation of the peptide, as well as elution buffer pH, on the chromatographic elution of human IgG, IgA and IgM from HWRGWV resins at various peptide densities (0.04-0.55 meq/g) were investigated. Over 80% recovery and 90% purity were achieved for human IgG and IgA isolation from complete minimum essential medium (cMEM) using HWRGWV resin at optimum peptide densities. For human IgM, 75.7% recovery and 86.0% purity were achieved by using HWRGWV at a low peptide density of 0.04 meq/g. Although HYFKFD and HFRRHL exhibited their ability for isolation of human IgG, IgA and IgM from cMEM as well, HWRGWV is the best option among them for large-scale purification of human IgG, IgA and IgM based on conditions tested.     

Separation of isomeric 2-aminopyridine derivatized N-glycans and N-glycopeptides of human serum immunoglobulin G by using a zwitterionic type of hydrophilic-interaction chromatography

Isomeric oligosaccharides and isomeric glycopeptides are sometimes difficult to separate on normal-phase (NP) and reversed-phase (RP) columns. A zwitterionic type of hydrophilic-interaction chromatography column with sulfobetaine groups (called ZIC-HILIC column) was first applied to the separation of 2-aminopyridine derivatized (PA) N-glycans and tryptic peptides of human serum immunoglobulin G (IgG). It is shown that the ZIC-HILIC column has high capability for structural recognition of isomeric N-glycans as well as high selectivity for glycopeptides. The former feature (i.e., structural recognition) was proven by sufficient separation of neutral PA N-glycan isomers, which are usually difficult to separate on NP and RP columns. In addition, it is noteworthy that IgG glycopeptides consisting of isomeric N-glycans and the same peptide sequences can be sufficiently separated on a ZIC-HILIC column. The latter feature (i.e., selectivity) was also demonstrated by easily separating two peptide groups with/without N-glycans. Thus, we note that the ZIC-HILIC column is highly promising for a simple analysis of N-glycans and N-glycopeptide samples.     

Adsorptive voltammetric behaviour of immunoglobulin M

The adsorptive voltammetric behaviour of immunoglobulin M (IgM) has been investigated at the static mercury drop electrode. The stripping process yields an analytically useful signal and the detection limit is 1.2 x 10(-10)M. The adsorptive voltammetric behaviour of IgM has been compared with that of IgG and streptavidin.     

Surfactant-aided size-exclusion chromatography for the purification of immunoglobulin G

In the production of monoclonal antibodies, separate chains of the antibody are often present in the product mixture as well as other contaminating proteins. These fragments should be removed from the whole antibodies. This paper shows the purification of monoclonal immunoglobulin G (IgG) from its heavy chain contaminant. The heavy chain fragment is simulated experimentally using bovine serum albumin (BSA), which has approximately the same molecular weight. The purification is performed using traditional size-exclusion chromatography (SEC) and using surfactant-aided SEC (SASEC), testing two different surfactants (C(12)E(23) and Tween20) and two different gels (Sephacryl S200HR and Sephacryl S300 HR). Pulse experiments show that with SASEC both BSA and IgG are more distributed towards the solid phase than compared to using SEC. This effect is larger on IgG, the largest component than on BSA. As a consequence, azeotropes will be formed at a specific surfactant concentration. Above this concentration the selectivity is reversed and increased to values higher than obtained with conventional SEC. At 7.5% (w/w) of C(12)E(23), BSA actually elutes before IgG. These experiments further show that when using SASEC larger productivity, higher yields and lower solvent consumption can be achieved without loss of purity of IgG when compared to conventional SEC. Mathematical simulation of the separation of BSA and IgG using simulated moving bed (SMB) chromatography indicates a large increase in productivity when applying a surfactant gradient in SASEC SMB compared to conventional isocratic SEC-SMB. Furthermore, solvent consumption reductions with a factor 15 prove possible as well as concentrating the IgG by a factor 2.     

Monitoring of mouse immunoglobulin G by flow-injection analytical affinity chromatography

A flow-injection analytical affinity chromatographic (FIAAC) system was developed for the on-line monitoring of mouse immunoglobulin G (IgG). Protein A or anti-mouse IgG antibodies immobilized on oxirane beads were filled in a miniature column. The IgG-containing samples and standards were passed through the column and detected fluorimetrically after elution with citrate buffer (pH 3 or 2.5). The on-line monitoring of mouse IgG 2a during a 7-day cultivation of hybridoma cells in a perfusion reactor by FIAAC is presented. A chemical barrier was used to prevent contamination of the reactor from the FIAAC.     

Radiochemical purification of microgram and sub-microgram amounts of beryllium

A method is presented for the separation and radiochemical purification of microgram and tracer amounts of beryllium from solutions. It is a four-stage ion-exchange procedure consisting of (1) selective adsorption of the beryllium onto NaDAP resin and its elution with ammonium fluoride, (2) adsorption of the fluoroberyllate complex onto an anion-exchange column and elution of the beryllium with hydrochloric acid, (3) adsorption and selective elution of the beryllium on a cation-exchange column and (4) a pass through an anion-exchange column in concentrated hydrochloric acid. The method is quantitative and requires no carrier. Decontamination factors from most radionuclides tested were greater than 10,000. The method can be used to determine beryllium-10 in environmental materials.     

Selective high-performance liquid chromatographic purification of bispecific monoclonal antibodies.

The recent development of improved production techniques for bispecific monoclonal antibodies (biMAbs) has significantly increased interest in specific purification procedures. In this investigation, a general high-performance liquid chromatographic (HPLC) purification method is proposed that allows highly purified biMAbs to be obtained from mouse ascites fluid containing a mixture of different antibodies, i.e., parental MAbs, active biMAb and a mixture of randomly assembled heavy and light chains. Proteins from ascites fluid were precipitated with ammonium sulphate and applied to a high-performance protein A column to separate the total immunoglobulin fraction. BiMAbs were isolated from other immunoglobulins by two subsequent passages through a high-performance hydroxyapatite (HPHT) column. This purification protocol combines specificity of protein A for immunoglobulin G (IgG) and high selectivity of hydroxyapatite for different IgG idiotypes. All purification steps were performed rapidly and reliably by HPLC. This method was applied to the purification of six different biMAbs with consistently high yields, purity and homogeneity. This general purification method may prove extremely valuable when highly pure preparation of biMAbs is required, as for in vivo use.     

Adaptation of hybridomas to protein-free media results in a simplified two-step immunoglobulin M purification process

An IgM antibody was purified from hybridoma supernatant containing serum using a three-step purification process comprising of tangential flow filtration, anion-exchange chromatography and size-exclusion chromatography. Recovery and purity were significantly improved upon adaptation of the hybridoma to serum-free media. The process could even be simplified by omitting the initial tangential flow filtration step. Even with a two-step purification process a purity of >98% and a recovery of >60% was obtained.     

Purification of human immunoglobulin G by thermoseparating aqueous two-phase systems

The purification of human immunoglobulin G (IgG) from a Chinese hamster ovary (CHO) cells supernatant was studied using an aqueous two-phase system (ATPS) composed of ethylene oxide/propylene oxide (UCON) and dextran. In UCON/dextran systems IgG partitions preferentially to the less hydrophobic dextran-rich phase (Kp<1). The addition of triethylene glycol-diglutaric acid (TEG-COOH) shifted the IgG partition into the upper phase showing significant improvements in both the recovery yields and purity. The purification of IgG from a CHO cell supernatant with UCON 2000/dextran/TEG-COOH system was optimised using a central composite design. Using an ATPS composed of 8% UCON, 6% dextran and 20% TEG-COOH, IgG was purified, in two steps, with a global yield of 85% and 88% purity. Statistical valid models were obtained to predict the effect of the experimental conditions on the IgG yield and purity, for both extraction and back-extraction steps. A system composed of 10% UCON, 5.5% dextran and 20% TEG-COOH was identified as the best compromise between final purity and yield.     

Characterization of metal chelate methacrylate monolithic disk for purification of polyclonal and monoclonal immunoglobulin G

Dynamic binding capacity (DBC) of commercial metal-chelate methacrylate monolith-convective interaction media (CIM) was performed with commercial human immunoglobulin G (IgG) (Cohn fraction II, III). Monoliths are an attractive stationary phase for purification of large biomolecules because they exhibit very low back pressure even at high flow rates and flow-unaffected binding properties. Adsorption of IgG onto CIM-IDA disk immobilized with Cu²⁺, Ni²⁺ and Zn²⁺ were studied with Tris-acetate (TA), phosphate-acetate (PA) and MMA (MES, MOPS and acetate) buffer systems at different flow rates. Adsorption and elution of IgG varied with different buffers and adsorption of IgG was maximum with MMA buffer. Adsorption of human IgG from Cohn fractions (II, III) was high when Cu²⁺ was used as ligand. CIM-IDA disk showed dynamic binding capacity in the range of 14–16 mg/ml with Cu²⁺ and 7–9 mg/ml with Ni²⁺ for human IgG with MMA buffer. In the case of CIM-IDA-Zn²⁺ column, the binding capacity was only about 0.5 mg/ml of support. Different desorption strategies like lowering of pH and increasing of competitive agent were also studied to achieve maximum recovery. Chromatographic runs with human serum and mouse ascites fluid were also carried out with metal chelate methacrylate monolithic disk and the results indicate the potential of this technique for polyclonal human IgG and monoclonal IgG purification from complex biological samples.     

Long-Term Cultured Hairy Roots of Chicory—A Rich Source of Hydroxycinnamates and 8-Deoxylactucin Glucoside

Foam fractionation is a promising method for separation and concentration of biochemicals. It is simple, easily scalable, inexpensive, and environment friendly. Foam fractionation thus represents an alternative to the traditional methods used for immunoglobulin enrichment. However, little, if any, literature exists documenting the utilization of foam fractionation in the enrichment of immunoglobulins. Milk were utilized as an immunoglobulin source to serve as examples of a real system in this study. The investigation examined the effects of varying five different process parameters: the initial pH value, the initial concentration of immunoglobulin, the nitrogen flow rate, the column height, and the foaming time. Experimental results demonstrated that immunoglobulin could effectively be enriched from milk by foam fractionation. The maximum enrichment ratio with pretreatment (using pH 4.6 precipitation) was 6.30 along with a more than 92 % recovery for IgG and an enrichment ratio of 5.1 with 85 % recovery for IgM.     

Affinity chromatographic purification of immunoglobulin M antibodies utilizing immobilized mannan binding protein.

A method is described for the rapid and efficient affinity chromatographic purification of murine monoclonal immunoglobulin M (IgM) which utilizes immobilized rabbit mannan binding protein (MBP). This solid-phase matrix is shown to bind IgM-class antibodies from a variety of species. Conditions reported show a binding capacity of IgM from murine ascites of nearly 1 mg/ml of immobilized MBP support. The prepared gel is shown to possess an ability to bind not only mouse IgM, but also human and bovine IgM, although with a lesser affinity. The matrix can be regenerated and reused at least ten times without any apparent loss of binding capacity or specificity. Mouse monoclonal IgM purified from ascites fluid using this method is greater than 95% pure as shown by high-performance liquid chromatography analysis.     

阴离子交换整体柱对蛋白质的分离与纯化

分别用乙二胺、二乙胺、三乙胺将自制的以甲基丙烯酸缩水甘油酯(GMA)为单体、乙二醇二甲基丙烯酸酯(EDMA)为交联剂的整体柱修饰为弱、强阴离子交换整体柱。考察了该整体柱的性能,选择出分离蛋白质(牛血清白蛋白、溶菌酶和谷胱甘肽)的最佳实验条件,并在最佳分离条件下考察了这些蛋白质在整体柱上的色谱行为和该整体柱对纤维素降解酶的分离纯化情况。实验结果表明,该整体柱性能良好,可以实现对纤维素降解酶的快速分离与纯化。同时,实验也证明采用梯度洗脱可以实现对某些蛋白质的分离纯化。     

离子交换色谱法分离纯化鸡卵黄免疫球蛋白

建立了高效、经济、大规模获得鸡卵黄免疫球蛋白(IgY)的生产方法。在对传统的水稀释法改良的基础上,结合聚乙二醇沉淀与离子交换色谱进行IgY的分离纯化。结果显示,用8倍无菌水稀释蛋黄液,用0.1 mol/L HCl调节pH为5.2,在4 ℃下静置8 h,于5000×g力离心可得上清粗IgY液,经测定回收率可达93.47%。然后用6%聚乙二醇沉淀后经DEAE-Toyopearl 650 M离子交换纯化,最佳的纯化条件: 0.05 mol/L磷酸盐缓冲液(PBS, pH 7)平衡上样,0.075 mol/L PBS(pH 7)洗脱。十二烷基硫酸钠-聚丙烯酰胺凝胶电泳(SDS-PAGE)分析结果显示所得的IgY的纯度为95.02%,活性保持率高达73.77%。本研究弥补了传统分离方法不能同时达到高纯度和高回收率的缺点,且可用于大规模生产。