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.     

Enhanced recovery of antitumor ganoderic acid T from Ganoderma lucidum mycelia by novel chemical conversion strategy

The removal of analog impurities with a very small sample size presents a major challenge in the purification of high-valued biochemicals such as those derived from fermentation or herbs. Ganoderic acid T (GA-T), an antitumor drug candidate, is very difficult to purify from the mycelia of medicinal mushroom Ganoderma lucidum due to co-purifying analog impurities. A novel pretreatment process with three consecutive chemical conversion steps, namely hydrolysis-acetylation-hydrolysis, was developed to convert two key analog impurities (7-O-ethyl GA-O and GA-Mk) to GA-T. It increased the GA-T amount in the 100 g dried mycelia from the initial 0.444 g to 1.621 g after the pretreatment, representing an apparent yield of 365% for the pretreatment. If the yield basis were the initial GA-T amount plus the GA-T amount from 100% conversion of 7-O-ethyl GA-O and GA-Mk in the crude extract, the yield, termed adjusted yield for the pretreatment in this work, would still reach 90.8%. Furthermore, the subsequent RP-HPLC purification was considerably enhanced due to the conversion of the analog impurities. This game-changer strategy achieved a daily GA-T throughput of 2.9 g with 95% purity (mass based). Even at the laboratory scale, it is now possible to produce a sufficient amount of GA-T for small-scale pharmacological and clinical evaluations. The approach of converting analog impurities that are otherwise difficult to remove to the product in a bioseparation process may be useful to achieve enhanced recovery of other medicinally useful natural products.     

An immunoperoxidase technique for demonstrating antilymphocytic globulin on cell surfaces

Summary An immunoperoxidase technique is described, for detecting horse IgG on human lymphocytes incubated with equine antilymphocytic globulin (ALG). Using this method, horse IgG was demonstrated on lymphocytes which had been incubated with ALG in dilutions of up to approximately 1:1,500.     

IDA型固定化镍离子金属螯合亲和膜色谱对人血清白蛋白的分离纯化

采用自制的固定化镍离子亚氨二乙酸(IDA)型复合纤维素金属螯合膜色谱对药用人血清白蛋白的进一步纯化进行了研究。考察了Ph对HAS吸附效果的影响。经一步纯化,商品药用HAS中的许多杂蛋白可被除去,经毛细管电泳分析,纯度与Sigma公司的电泳纯HAS相当,回收率可达85%以上。纯化蛋白液中的镍离子经过自制的N,N,N′-三羧甲基乙二胺(TED)型螯合柱处理后可较好地除去。     

Adsorption of human serum proteins onto TREN-agarose: Purification of human IgG by negative chromatography

Tris(2-aminoethyl)amine (TREN) – a chelating agent used in IMAC – immobilized onto agarose gel was evaluated for the purification of IgG from human serum by negative chromatography. A one-step purification process allowed the recovery of 73.3% of the loaded IgG in the nonretained fractions with purity of 90–95% (based on total protein concentration and nephelometric analysis of albumin, transferrin, and immunoglobulins A, G, and M). The binding capacity was relatively high (66.63 mg of human serum protein/mL). These results suggest that this negative chromatography is a potential technique for purification of IgG from human serum.     

Simultaneous ultrafiltration and affinity sorptive separation of proteins in a hollow fiber membrane module

A protein separation scheme combining affinity or ion exchange sorption with hollow fiber cross-flow filtration is described. Sorptive gel particles were loaded into the shell side of a hollow fiber membrane module. In the adsorption step, crude protein mixtures were passed through the lumen and permeating proteins passed through the membrane to bind on the gel particles in the shell. During elution, a buffer of adequate ionic strength to desorb the bound proteins was passed through the lumen and permeated through the shell. The eluant was then collected at the outlet to the shell of the hollow fiber module. The concept is illustrated by two examples: the purification of butyrylcholinesterase (EC 3.1.1.7) from raw horse serum using the affinity gel procainamide-Sepharose as the packing and the separation of carboxylesterase (EC 3.1.1.1) from beef liver homogenate using DEAE-Sephadex as the packing. The technique has the advantage of high volumetric throughputs typical of hollow fiber membrane modules as well as the high capacity characteristic of chromatographic packings. In addition, cross-flow filtration of particulates, agglomerates, and debris in passing protein from lumen to shell side can help eliminate the need for extensive pretreatment.     

用膨胀床金属亲和层析从淡菜匀浆液中分离纯化纤维素酶

研究了一种新的膨胀床金属亲和层析技术,即将金属亲和层析结合膨胀床层析,直接从淡菜(Blue mussel)匀浆液中纯化纤维素酶。研究了金属亲和配基种类、pH、离子强度及流速对酶吸附和解吸的影响,确定了酶洗脱条件和介质再生条件。一步可纯化纤维素酶194倍,酶收率达82%。本方法不需要预先去除细胞碎片,而且处理速率比传统层析技术高3～4倍。     

Free polymeric bioligands in aqueous two-phase affinity extractions of microbial xylanases and pullulanase

Two reversibly soluble-insoluble polymers (viz. Eudragit S-100 and alginate) were used as free macroaffinity bioligands in polyethylene glycol (PEG)/salt two-phase systems for separation of enzymes. Incorporation of Eudragit S-100 and alginate in the PEG phase led to considerable selectivity in separation of microbial xylanases and pullulanase, respectively. Xylanase from Aspergillus niger was recovered 93% with 56-fold purification, whereas the enzyme from Trichoderma reesei and Bacillus amyloliquefaciens was obtained with 93% activity recovery (31-fold purification) and 90% activity recovery (32-fold purification), respectively. From Bacillus acidopullulyticus pullulanase, 85% enzyme activity recovery with 44-fold purification was obtained. The approach described here shows the potential of developing into a general approach for use of reversibly soluble-insoluble macroaffinity ligand in two-phase affinity extraction.     

Selective precipitation-assisted recovery of immunoglobulins from bovine serum using controlled-fouling crossflow membrane microfiltration

Efficient and economic recovery of immunoglobulins (Igs) from complex biological fluids such as serum, cell culture supernatant or fermentation cell lysate or supernatant, represents a substantial challenge in biotechnology. Methods such as protein A affinity chromatography and anion exchange chromatography are limited by cost and selectivity, respectively, while membrane chromatography is limited by low adsorptive area, flow distribution problems and scale-up difficulties. By combining the traditional salt-assisted precipitation process for selective removal of Igs from serum followed by constant-permeate flux membrane microfiltration for low fouling, we demonstrate an exciting new, efficient and economic hybrid method. The high selectivity of an ammonium sulfate-induced precipitation step was used to precipitate the Igs leaving the major undesirable impurity, the bovine serum albumin (BSA), in solution. Crossflow membrane microfiltration in diafiltration mode was then employed to retain the precipitate, while using axial flow rates to optimize removal of residual soluble BSA to the permeate. The selectivity between immunoglobulin G (IgG) and BSA obtained from the precipitation step was approximately 36, with 97% removal of the BSA with diafiltration in 5 diavolumes with resulting purity of the IgG of approximately 93% after the membrane microfiltration step. Complete resolubilization of the IgG was obtained without any aggregation at the concentrations of ammonium sulfate employed in this work. Further, membrane pore size and axial Reynolds number (recirculation rate) were shown to be important for minimizing fouling and loss of protein precipitate.     

Chromatography on DEAE ion-exchange and Protein G affinity columns in tandem for the separation and purification of proteins.

A high-performance liquid-chromatographic method based on coupled DEAE anion-exchange and Protein G affinity columns has been developed for the simultaneous separation and purification of immunoglobulin G and albumin from mouse serum. The diluted mouse serum was injected directly into this system, and the proteins were eluted separately from the DEAE and Protein G columns, coupled in series, by the column-switching technique. The advantages of this method are that IgG and albumin can be separated and purified simultaneously, the expensive affinity column is protected from contamination by the impurities in the mouse serum, and it is fast, selective, robust, and reproducible.     

Prevalence of antibodies to Neospora sp. in horses from Alabama and characterisation of an isolate recovered from a naturally infected horse [corrected

An IFAT was used to determine the prevalence of Neospora-specific IgG antibodies in serum from Alabama horses. Serum samples (n = 536) were from asymptomatic horses routinely submitted for equine infectious anaemia virus infection testing. We also subjected a 13-year-old horse with CNS disease to necropsy examination for isolation and in vitro cultivation of protozoal organisms. In antemortem tests, this horse was positive for antibodies to Neospora sp. in the IFAT and western immunoblot. Results of the prevalence survey indicated that IgG antibodies to Neospora were present in 62 (11.5%) of the 536 serum samples. Endpoint titres for the positive samples were 1:50 (35/6.5%), 1:100 (19/3.5%), 1:200 (7/1.3%) and 1:1600 (1/0.2%). Tachyzoites were first seen in cultured bovine turbinate cells 32 days after inoculation with spinal cord homogenates from the horse with CNS disease. Tachyzoites reacted with known N. caninum-positive serum from horses, cows, dogs and mice, but did not react with murine anti-Toxoplasma gondii or equine anti-Sarcocystis neurona serum. Ultrastructural features of tachyzoites and results of comparison of tachyzoite immunodominant proteins revealed that they were identical to those of N. hughesi, a species described recently from a naturally infected horse. The isolate recovered from the naturally infected horse in the present study (designated NA1) is thought to be an isolate of N. hughesi, although confirmation of this awaits additional molecular characterisation. These results provide some additional evidence that N. hughesi is a valid species and that Neospora infections in horses may occur in widely separated geographic regions of the United States.     

Purification of equine chorionic gonadotropin (eCG) using magnetic ion exchange adsorbents in combination with high‐gradient magnetic separation

Current purification of the glycoprotein equine chorionic gonadotropin (eCG) from horse serum includes consecutive precipitation steps beginning with metaphosphoric acid pH fractionation, two ethanol precipitation steps, and dialysis followed by a numerous of fixed‐bed chromatography steps up to the specific activity required. A promising procedure for a more economic purification procedure represents a simplified precipitation process requiring only onethird of the solvent, followed by the usage of magnetic ion exchange adsorbents employed together with a newly designed ‘rotor‐stator’ type High Gradient Magnetic Fishing (HGMF) system for large‐scale application, currently up to 100 g of magnetic adsorbents. Initially, the separation process design was optimized for binding and elution conditions for the target protein in mL scale. Subsequently, the magnetic filter for particle separation was characterized. Based on these results, a purification process for eCG was designed consisting of (i) pretreatment of the horse serum; (ii) binding of the target protein to magnetic ion exchange adsorbents in a batch reactor; (iii) recovery of loaded functionalized adsorbents from the pretreated solution using HGMF; (iv) washing of loaded adsorbents to remove unbound proteins; (v) elution of the target protein. Finally, the complete HGMF process was automated and conducted with either multiple single‐cycles or multicycle operation of four sequential cycles, using batches of pretreated serum of up to 20 L. eCG purification with yields of approximately 53% from single HGMF cycles and up to 80% from multicycle experiments were reached, with purification and concentration factors of around 2,500 and 6.7, respectively. © 2014 American Institute of Chemical Engineers Biotechnol. Prog., 31:78–89, 2015     

Construction of a medium-density horse gene map

A medium-density map of the horse genome (Equus caballus) was constructed using genes evenly distributed over the human genome. Three hundred and twenty-three exonic primer pairs were used to screen the INRA and the CHORI-241 equine BAC libraries by polymerase chain reaction and by filter hybridization respectively. Two hundred and thirty-seven BACs containing equine gene orthologues, confirmed by sequencing, were isolated. The BACs were localized to horse chromosomes by fluorescent in situ hybridization (FISH). Overall, 165 genes were assigned to the equine genomic map by radiation hybrid (RH) (using an equine RH(5000) panel) and/or by FISH mapping. A comparison of localizations of 713 genes mapped on the horse genome and on the human genome revealed 59 homologous segments and 131 conserved segments. Two of these homologies (ECA27/HSA8 and ECA12p/HSA11p) had not been previously identified. An enhanced resolution of conserved and rearranged chromosomal segments presented in this study provides clarification of chromosome evolution history.     

Studies on proteolytic activity in commercial myoglobin preparations

Commercial myoglobin preparations from horse skeletal muscle degraded casein. The maximum activity was at pH8-8.5. A muscle myofibril preparation was also attacked. The protease could be partly separated from the myoglobin by selective ultrafiltration through a membrane with an exclusion limit of mol.wt. 30000. A greater than 1000-fold purification of the proteolytic activity was achieved by affinity chromatography with soya-bean trypsin inhibitor bound to CM-cellulose. The enzyme preparation hydrolysed p-toluenesulphonyl-l-arginine methyl ester and N-benzyloxycarbonyl-l-tyrosine p-nitrophenyl ester. Its activity was inhibited strongly by soya-bean and ovomucoid trypsin inhibitors, serum and the soluble fraction of muscle homogenates. EDTA, p-chloromercuribenzoate and phenylmethylsulphonyl fluoride also caused some inhibition.     

Recent advances in bioprocessing application of membrane chromatography

Compared to traditional chromatography using resins in packed-bed columns, membrane chromatography is a relatively new and immature bioseparation technology based on the integration of membrane filtration and liquid chromatography into a single-stage operation. Over the past decades, advances in membrane chemistry have yielded novel membrane devices with high binding capacities and improved mass transfer properties, significantly increasing the bioprocessing efficiency for purification of biomolecules. Due to the disposable nature, low buffer consumption, and reduced equipment costs, membrane chromatography can significantly reduce downstream bioprocessing costs. In this review, we discuss technological merits and disadvantages associated with membrane chromatography as well as recent bioseparation applications with a particular attention on purification of large biomolecules.     

Integrated fragmentation of human IgG and purification of Fab using a reactant adsorptive membrane bioreactor separator system

This article discusses an integrated separation–reaction–separation scheme for producing Fab fragment directly from human immunoglobulin G (hIgG) present in serum feed. The novel reactant adsorptive membrane bioreactor separator (or RAMBS) system used in the current study consisted of a stack of microporous adsorptive membranes held within a temperature controlled module. The membrane stack, in the presence of salt, selectively and reversibly adsorbed hIgG by hydrophobic interaction while allowing most other serum proteins to flow through. The bound hIgG was then fragmented by pumping a solution of papain through the reactor at controlled temperature and flow rate. The salt concentration and pH for reaction and separation were systematically optimized using pure hIgG as reactant. The Fab fragment was separated from undigested hIgG and other byproducts such as Fc fragment based on their differences in hydrophobicity. Under optimal conditions, Fab was obtained in the reaction flow through while the other proteins remained bound to the membrane, these being subsequently eluted by lowering the salt concentration. The RAMBS system in addition to being convenient from process integration and intensification points of view also showed higher catalytic efficiency of papain in comparison to that in liquid phase reactions. Biotechnol. Bioeng. 2009; 104: 152–161 © 2009 Wiley Periodicals, Inc.     

Purification of human IgG by negative chromatography on ω-aminohexyl-agarose

The ω-aminohexyl diamine immobilized as ligand on CNBr- and bisoxirane-activated agarose gel was evaluated for the purification of human immunoglobulin G (IgG) from serum and plasma by negative affinity chromatography. The effects of matrix activation, buffer system, and feedstream on recovery and purity of IgG were studied. A one-step purification process using Hepes buffer at pH 6.8 allowed a similar recovery (69–76%) of the loaded IgG in the nonretained fractions for both matrices, but the purity was higher for epoxy-activated gel (electrophoretically homogeneous protein with a 6.5-fold purification). The IgG and human serum albumin (HSA) adsorption equilibrium studies showed that the adsorption isotherms of IgG and HSA obeyed the Langmuir–Freundlich and Langmuir models, respectively. The binding capacity of HSA was high (210.4 mg mL^?1 of gel) and a positive cooperativity was observed for IgG binding. These results indicate that immobilizing ω-aminohexyl using bisoxirane as coupling agent is a useful strategy for rapid purification of IgG from human serum and plasma.     

Studies on Complement-Fixation Reaction in Equine Infectious Anemia

The substances responsible for inhibiting complement-fixation (CF) reaction of the late-stage serum of an equine infectious anemia (EIA)-infected horse were investigated. It was found that the IgG and IgG(T) classes in the late-stage serum were responsible for the CF inhibition. IgA could not be detected in partially purified IgG(T) by an immunodiffusion test using rabbit anti-human IgA serum. Other serum components could not be demonstrated in purified IgG by immunoelectrophoresis using rabbit anti-horse serum. The IgG class simultaneously showed CF and CF-inhibiting (CFI) activities, whereas the IgG(T) class showed only CFI activity. The IgG(T) class could exert CFI activity only when it had been reacted with the EIA antigen before addition of the reference CF serum and complement. In contrast, the IgG class converted the CF-active reference serum into a non-CF-reactive one irrespective of whether it was simultaneously reacted with the EIA antigen and the reference CF serum, whether it was added to the reaction mixture of the EIA antigen and the reference CF serum, or whether it was sensitized with the EIA antigen before addition of the reference CF serum. Inhibitory activities of the IgG and IgG(T) classes seemed to be different from each other in their reaction pattern as far as tested under our experimental conditions. Their CFI activities seemed to be specific for EIA, being negative in CFI activity in reaction with other antigens.     

Studies on complement-fixation reaction in equine infectious anemia. II. Identification of complement-fixing inhibitors.

The substances responsible for inhibiting complement-fixation (CF) reaction of the late-stage serum of an equine infectious anemia (EIA)-infected horse were investigated. It was found that the IgG and IgG(T) classes in the late-stage serum were responsible for the CF inhibition. IgA could not be detected in partially purified IgG(T) by an immunodiffusion test using rabbit anti-human IgA serum. Other serum components could not be demonstrated in purified IgG by immunoelectrophoresis using rabbit anti-horse serum. The IgG class simultaneously showed CF and CF-inhibiting (CFI) activities, whereas the IgG(T) class showed only CFI activity. The IgG(T) class could exert CFI activity only when it had been reacted with the EIA antigen before addition of the reference CF serum and complement. In contrast, the IgG class converted the CF-active reference serum into a non-CF-reactive one irrespective of whether it was simultaneously reacted with the EIA antigen and the reference CF serum, whether it was added to the reaction mixture of the EIA antigen and the reference CF serum, or whether it was sensitized with the EIA antigen before addition of the reference CF serum. Inhibitory activities of the IgG and IgG(T) classes seemed to be different from each other in their reaction pattern as far as tested under our experimental conditions. Their CFI activities seemed to be specific for EIA, being negative in CFI activity in reaction with other antigens.     

Purification of lutropin and follitropin in high yield from horse pituitary glands

A method has been developed for the purification of equine lutropin (eLH) and equine follitropin (eFSH) from horse pituitary glands which attains high yields of both hormones in contrast to previous methods that were devoted to one or the other with inferior recovery of the hormones. Two-pass chromatography over CM-Sephadex was used to separate eLH from eFSH. Subsequent steps employing QAE (quaternary amino-ethyl)-Sephadex chromatography and gel filtration on Sephacryl S-200 produced highly purified hormone preparations. Yields of purified eLH and eFSH were 110 and 60 mg/kg of frozen pituitaries, respectively. Subunits were prepared by dissociation in 8 M guanidine HCl followed by either gel filtration (eLH) or gel filtration followed by QAE-Sephadex chromatography (eFSH). The hormones and their subunits were characterized by sodium dodecyl sulfate-gel electrophoresis, amino acid analysis, NH2-terminal analysis, and by LH and FSH radioligand receptor assays.