A simplified procedure for synthesizing large quantities of highly purified uridine [beta-32P]diphospho-N-acetylglucosamine

A simplified procedure for the synthesis of [beta-32P]UDP-N-acetylglucosamine is described. This novel method utilizes commercially available enzymes, chemical acetylation, and preparative thin-layer chromatography and can be used to synthesize millicurie quantities of the sugar nucleotide at an extremely high specific activity and purity.     

Simultaneous purification and immobilization of soybean hull peroxidase with a dye attached to chitosan mini-spheres

Soybean hull peroxidase (EC 1.11.1.7, SBP) was simultaneously purified and immobilized by dye affinity chromatography with Reactive Blue 4 attached to chitosan mini-spheres. Under optimized conditions, 96% of SBP was adsorbed to the matrix. Under the most stringent condition, only 49% was desorbed, whereas 2 M NaCl failed to desorb a significant amount of SBP. This behaviour allowed proposing the dye matrix as a support to immobilize SBP from a crude extract. The pH of maximum activity shifted from 7 to 3–5. SBP gained thermostability after immobilization: after 5?h at 85?°C, the remaining activity was 54%, whereas that of the free enzyme was 31%. The optimum temperature for the immobilized SBP was 75?°C, whereas that of the free enzyme was 55?°C. After two months at 4?°C, the activity loss of the immobilized SBP was only 3%. Immobilized SBP removed 80% of 2-bromophenol from wastewater in 180?min and, after five cycles of use, the activity loss was only 12.8%.     

Medium format enhancement: design of an immobilized heparin affinity media for industrial bioprocessing

Affinity chromatography is one of the most powerful and selective separation methods available. Recently, affinity methods are being incorporated into industrial processes with some frequency. One of the reasons for this is that affinity media robust enough for industrial bioprocessing are now available. By robust is meant that the media meet stringent requirements for cleanability, sanitization, physical and chemical stability, regulatory and technical support, batch-to-batch reproducibility and reliability of supply. This paper describes a medium format enhancement program to adapt a widely known group-specific affinity medium, Heparin Sepharose( CL6B, to the requirements for industrial bioprocessing. The new medium, Heparin Sepharose( 6 Fast Flow was designed for the recovery of antithrombin 3 (AT3) at industrial scale. The medium is based upon a highly cross-linked 6% agarose, which is produced in very large scale and is familiar to regulatory agencies. The ligand, heparin, is attached to the matrix by a reductive amination chemistry. The resulting linkage is stable in 0.1 N NaOH for 150 h, showing no decrease in AT3 binding affinity at that time. Heparin has a broad biological functionality and thus is useful chromatographically for the purification of a number of proteins which have an affinity for heparin. Heparin, as a complex sugar, is also a highly charged polyanion and thus has interesting ion-exchange properties. Because of its broad applicability to a number of purification problems, immobilized heparin is a useful case study in medium format enhancement. © 1997 John Wiley & Sons, Ltd.     

Temperature-triggered purification of antibodies

In this article the unique capability of elastin-like protein (ELP) to reversibly precipitate was combined with the high affinity and specificity of antibody-binding domains such as Protein G, Protein L, or Protein LG as a general method for antibody purification that combines in a unique manner the simplicity and robustness of temperature-triggered precipitation with the selectivity of affinity interactions. In a single precipitation step, antibodies derived from different sources (animal sera or hybridoma cell cultures) were selectively recovered by a simple temperature trigger. Due to the versatility of the binding ligands toward different classes of antibodies, we believe that this technology will be useful as an economical, highly efficient, and universal platform for the purification of antibodies.     

Dye-ligand affinity adsorbents for enzyme purification

Affinity chromatography is widely employed in laboratory and large-scale for the purification of biotherapeutics and diagnostics. Some of the most widely used ligands in affinity chromatography have been several reactive chlorotriazine dyes. In particular, immobilized anthraquinone dyes have found a plethora of applications in affinity chromatography because they are inexpensive, are resistant to chemical and biological degradation, are sterilizable and cleanable in situ, and are readily immobilized to generate affinity absorbents which display high binding capacity for a broad spectrum of proteins. This article provides detailed protocols on the preparation of a dye-ligand affinity adsorbent. Also, detailed protocols for effective application of these media, emphasizing binding and elution conditions are presented.     

Preparative affinity electrophoresis: application to human erythrocyte carbonic anhydrase

A modification of affinity electrophoresis for preparative purposes is described. This method has been applied to the purification of human erythrocyte carbonic anhydrases B and C. During conventional affinity chromatography some hemoglobin contamination occurs. By introduction of an electrophoretic purification step after the immobilization of carbonic anhydrase to the affinity gel, the hemoglobin impurity is reduced about eight and two times in the preparations of the B and C enzymes, respectively, compared to the enzymes purified by affinity chromatography.     

Affinity gel electrophoresis as a predictive technique in the fractionation of transgenic sheep milk proteins by affinity aqueous two-phase partitioning

Affinity electrophoresis in the presence of various triazine dyes of sheep milk proteins, including transgenically-introduced human ₁-antitrypsin, has been evaluated as a predictive technique for possible large scale affinity-driven aqueous two-phase purifications. The success of the approach suggested it has potential as a general method for the rapid screening of ligands using only g amounts of sample, that could be applied to many complex mixtures before embarking on more costly and time-consuming two-phase partitioning experiments.     

Biomimetic-dye affinity adsorbents for enzyme purification: application to the one-step purification of Candida boidinii formate dehydrogenase

Formate dehydrogenase (FDH, EC 1.2.1.2) was purified from Candida boidinii cells in a single step by biomimetic-dye affinity chromatography. For this purpose, seven' biomimetic analogues of the monochlorotriazine dye, Cibacron(R) Blue 3GA (CB3GA), and parent dichloro-triazine dye, Vilmafix((R)) Blue A-R (VBAR), bearing a car-boxylated structure as their terminal biomimetic moiety, were immobilized on crosslinked agarose gel, Ultrogel((R)) A6R. The corresponding new biomimetic-dye adsorbents, along with nonbiomimetic adsorbents bearing CB3GA and VBAR, were evaluated for their ability to purify FDH from extracts obtained after press-disintegration of C. boidinii cells. Optimal conditions for maximizing specific activity of FDH in starting extracts (1.8 U/mg) were realized when cell growth was performed on 4% methanol, and press disintegration proceeded in four consecutive passages before the homogenate was left to stand for 1 h (4 degrees C). When compared to nonbiomimetic adsorbents, biomimetic adsorbents exhibited higher purifying ability. Furthermore, one immobilized biomimetic dye, bearing as its terminal biomimetic moiety mercap-topyruvic acid linked on the chlorotriazine ring (BM6), displayed the highest purifying ability. Adsorption equilibrium data which were obtained for the BM6 adsorbent in a batch system corresponded well to the Langmuir isotherm and, in addition, breakthrough curves were taken for protein and FDH adsorption in a fixed bed of BM6 adsorbent. The dissociation constant ( K(D)) of the complex between immobilized BM6 and FDH was found to equal 0.05 muM. Adsorbent BM6 was employed in the purification of FDH from a 18-L culture of C. boidinii in a single step (60% overall yield of FDH). The purified FDH afforded a single-band on sodium dodecyl sulphate poly-acrylamide gel electrophoresis, and a specific activity of 7,0 U/mg (30 degrees C). (c) 1995 John Wiley & Sons, Inc.     

Weak partitioning chromatography for anion exchange purification of monoclonal antibodies

Weak partitioning chromatography (WPC) is an isocratic chromatographic protein separation method performed under mobile phase conditions where a significant amount of the product protein binds to the resin, well in excess of typical flowthrough operations. The more stringent load and wash conditions lead to improved removal of more tightly binding impurities, although at the cost of a reduction in step yield. The step yield can be restored by extending the column load and incorporating a short wash at the end of the load stage. The use of WPC with anion exchange resins enables a two-column cGMP purification platform to be used for many different mAbs. The operating window for WPC can be easily established using high throughput batch-binding screens. Under conditions that favor very strong product binding, competitive effects from product binding can give rise to a reduction in column loading capacity. Robust performance of WPC anion exchange chromatography has been demonstrated in multiple cGMP mAb purification processes. Excellent clearance of host cell proteins, leached Protein A, DNA, high molecular weight species, and model virus has been achieved.     

Affinity precipitation of proteins by polyligands

A novel technique for affinity precipitation has been developed in which multimeric target proteins are precipitated as a result of network formation by polymer-conjugated ligands (polyligands). A polyligand precipitant for avidin was synthesized by conjugation of biotin to a polyacrylamide-based backbone. The effects of mixing conditions, ligand substitution frequency, and molecular weight on affinity precipitation were examined using the biotin-PAAm precipitant. Biotin was replaced by iminobiotin to study the effect of the ligand-protein dissociation constant o affinity precipitation. The iminobiotin-PAAm precipitant was also used to examine the reversibility of the precipitation and recovery of the target protein after precipitation. (c) 1993 Wiley & Sons, Inc.     

Affinity purification of fibrinogen using a ligand from a peptide library.

An affinity resin containing the peptide ligand Phe-Leu-Leu-Val-Pro-Leu (FLLVPL) has been developed for the purification of fibrinogen. The ligand was identified by screening a solid-phase combinatorial peptide library using an immunostaining technique. The specific binding of fibrinogen to the ligand has been characterized by isothermal calorimetry and adsorption isotherms and is dominated by both hydrophobic interactions and ionic interactions with the N-terminal free amino group. The effective association constant of fibrinogen was substantially higher when the peptide was immobilized on the resin than in solution; moreover, it increased with increasing peptide density, suggesting a cooperative binding effect. A low ionic strength buffer at pH 4 was used successfully to elute adsorbed fibrinogen from the column with high purity, retention of factor XIII crosslinking activity, and minimal, if any, loss of biological function. This general approach to ligand selection and characterization can be used to develop peptide ligands for the affinity purification of diverse proteins on a large scale.     

Advective hydrogel membrane chromatography for monoclonal antibody purification in bioprocessing

Protein A chromatography is widely employed for the capture and purification of monoclonal antibodies (mAbs). Because of the high cost of protein A resins, there is a significant economic driving force to seek new downstream processing strategies. Membrane chromatography has emerged as a promising alternative to conventional resin based column chromatography. However, to date, the application has been limited to mostly ion exchange flow through (FT) mode. Recently, significant advances in Natrix hydrogel membrane has resulted in increased dynamic binding capacities for proteins, which makes membrane chromatography much more attractive for bind/elute operations. The dominantly advective mass transport property of the hydrogel membrane has also enabled Natrix membrane to be run at faster volumetric flow rates with high dynamic binding capacities. In this work, the potential of using Natrix weak cation exchange membrane as a mAb capture step is assessed. A series of cycle studies was also performed in the pilot scale device (> 30 cycles) with good reproducibility in terms of yield and product purities, suggesting potential for improved manufacturing flexibility and productivity. In addition, anion exchange (AEX) hydrogel membranes were also evaluated with multiple mAb programs in FT mode. Significantly higher binding capacity for impurities (support mAb loads up to 10Kg/L) and 40X faster processing speed were observed compared with traditional AEX column chromatography. A proposed protein A free mAb purification process platform could meet the demand of a downstream purification process with high purity, yield, and throughput. © 2015 American Institute of Chemical Engineers Biotechnol. Prog., 31:974–982, 2015     

工程菌产霍乱肠毒素B亚单位的纯化

 本实验室使霍乱肠毒素(CT)B亚单位基因在大肠杆菌中获得表达,并能分泌到胞外。将该菌株培养物上清经过超滤浓缩后,用偶联上霍乱毒素IgG的CNBr-Sepharose 4B进行亲和层析,得到表达产物霍乱毒素B亚单位纯蛋白。经PA-GE、HPLC及琼脂免疫扩散等方法鉴定证明该蛋白与天然霍乱肠毒素B亚单位完全相同。     

Immunoaffinity chromatography

The basic procedure of immunoaffinity chromatography (IAC) is described. The insoluble support matrices available for IAC and their activation chemistries, including some of the most recently introduced, are reviewed. Means of selecting the most appropriate monoclonal antibody (MAb) are described, although an empirical approach is still required for the final choice of antibody. Precise methods of runing IAC columns are surveyed including the binding, washing, and elution stages, although no precise recommendations can be made particularly for the elution step since this is unique to a particular MAb and antigen. All IAC sorbents lose activity with time through a combination of MAb inactivation and ligand leakage. The relative importance of the two phenomena is discussed, and suggestions are made to minimize the problem along with an indication of the relative stabilities of a range of coupling chemistries. A sample of the proteins purified by IAC is given together with pointers to the future of the technique.     

Toward improving selectivity in affinity chromatography with PEGylated affinity ligands: The performance of PEGylated protein A

Chemical modification of macromolecular affinity chromatography ligands with polyethylene glycol chains or “PEGylation” can potentially improve selectivity by sterically suppressing non‐specific binding interactions without sacrificing binding capacity. For a commercial protein A affinity media and with yeast extract (YE) and fetal bovine serum (FBS) serving as mock contaminants, we found that the ligand accounted for more than 90% of the media‐associated non‐specific binding, demonstrating an opportunity for improvement. The IgG static binding affinity of protein A mono‐PEGylated with 5.0 and 20.7 kDa poly(ethylene glycol) chains was found to be preserved using a biomolecular interaction screening platform. Similar in situ PEGylations of the commercial protein A media were conducted and the modified media was functionally characterized with IgG solutions spiked with YE and FBS. Ligand PEGylation reduced the mass of media‐associated contaminants by a factor of two to three or more. Curiously, we also found an increase of up to 15% in the average recovery of IgG on elution after PEGylation. Combined, these effects produced an order of magnitude increase in the IgG selectivity on average when spiked with YE and a two‐ to three‐fold increase when spiked with FBS relative to the commercial media. Dynamic binding capacity and mass‐transfer resistance measurements revealed a reduction in dynamic capacity attributed to a decrease in IgG effective pore diffusivity and possibly slower IgG association kinetics for the PEGylated protein A ligands. Ligand PEGylation is a viable approach to improving selectivity in affinity chromatography with macromolecular ligands. © 2014 American Institute of Chemical Engineers Biotechnol. Prog., 30:1364–1379, 2014     

Single step immobilized metal ion affinity precipitation/chromatography based procedures for purification of concanavalin A and Cajanus cajan mannose-specific lectin

Concanavalin A and a mannose-specific lectin could be precipitated specifically from extracts of jack bean and Cajanus cajan seeds, respectively, using metal charged EGTA. Single step purification of the lectins was also possible using iminodiacetic acid-Sepharose charged with metal ions. Nondenaturing electrophoresis in polyacrylamide gel and that performed in presence of SDS ascertained homogeneity of the isolated lectins. The migration behavior of the purified lectins was comparable with those of the lectins purified using alternative procedures.     

Immobilized palladium(II) ion affinity chromatography for recovery of recombinant proteins with peptide tags containing histidine and cysteine

Fusion of peptide‐based tags to recombinant proteins is currently one of the most used tools for protein production. Also, immobilized metal ion affinity chromatography (IMAC) has a huge application in protein purification, especially in research labs. The combination of expression systems of recombinant tagged proteins with this robust chromatographic system has become an efficient and rapid tool to produce milligram‐range amounts of proteins. IMAC‐Ni(II) columns have become the natural partners of 6xHis‐tagged proteins. The Ni(II) ion is considered as the best compromise of selectivity and affinity for purification of a recombinant His‐tagged protein. The palladium(II) ion is also able to bind to side chains of amino acids and form ternary complexes with iminodiacetic acid and free amino acids and other sulfur‐containing molecules. In this work, we evaluated two different cysteine‐ and histidine‐containing six amino acid tags linked to the N‐terminal group of green fluorescent protein (GFP) and studied the adsorption and elution conditions using novel eluents. Both cysteine‐containing tagged GFPs were able to bind to IMAC‐Pd(II) matrices and eluted successfully using a low concentration of thiourea solution. The IMAC‐Ni(II) system reaches less than 20% recovery of the cysteine‐containing tagged GFP from a crude homogenate of recombinant Escherichia coli, meanwhile the IMAC‐Pd(II) yields a recovery of 45% with a purification factor of 13. Copyright © 2014 John Wiley & Sons, Ltd.