Evaluation of activation methods with cellulose beads for immunosorbent purification of immunoglobulins

Attempts were made to evaluate the chemical properties of cross-linked cellulose beads in order to utilize them as a support material for the large scale purification of specific immunoglobulins via immunosorbent chromatography with goat anti-human IgG serving as the model affinity ligand. Since these cellulose beads have sufficient mechanical strength to sustain a high flow rate of viscous fluids, they are ideal for rapid purification of large fluid volumes. The beads were activated with cyanogen bromide, tosyl chloride, cyanuric chloride or oxidation reagents such as chromium trioxide, sodium periodate and dimethylsulfoxide-carbodiimide before the antibodies were immobilized under mild conditions. The inert hydroxyl groups were thus converted into more active cyanate ester, tosylate, reactive acyl-like chlorines, and carbonyl groups which readily react with amino groups of antibodies. Antibodies were immobilized on the activated cellulose beads under mild conditions with an average yield of 42.3%. Every immobilization method had disadvantages. The binding activity of the immobilized antibody depended on its concentration. Very high binding efficiency was achieved when the concentration was less than 0.2 mg/ml; however, the efficiency was only about 5% when the concentration was greater than 2 mg/ml. The binding activity of immobilized antibodies was affected by the steric factors imposed by the support material but not affected by the immobilization methods. Although some non-specific interaction between plasma components and the cellulose bead immunosorbent occurred, specific immunoglobulin could be purified from plasma in a single step.     

Influence of the conditions of trypsin immobilization onto Spherosil on coupling efficiency

Summary The effect of several parameters (pH, time of reaction, temperature, enzyme concentration) on trypsin immobilization onto glutaraldehyde-activated amine-Spherosil was investigated. This activated support could be stored over long periods of time without any important loss of capacity for trypsin coupling. When increasing the amount of trypsin bound to the carrier, enzymatic activity shows an optimal value, beyond which an augmentation of Spherosil enzyme content results in a lowered activity. The influence of the number of available reactive aldehyde groups on silica was investigated by coupling L-lysine to activated support either prior to or simulataneously with trypsin immobilization. In both cases, the activity of trypsin derivatives is decreased when L-lysine concentration is increased, yet the activity of trypsin derivatives is never equal to zero, even in presence of a large excess of L-lysine. This suggests the presence of two types of reactive groups on the activated support.     

Design and study of peptide-ligand affinity chromatography adsorbents: application to the case of trypsin purification from bovine pancreas

The purification of trypsin from bovine pancreas was employed in a case study concerning the design and optimization of peptide-ligand adsorbents for affinity chromatography. Four purpose-designed tripeptide-ligands were chemically synthesized (>95% pure), exhibiting an Arg residue as their C-terminal (site P(1)) for trypsin bio-recognition, a Pro or Ala in site P(2), and a Thr or Val in site P(3). Each tripeptide-ligand was immobilized via its N-terminal amino group on Ultrogel A6R agarose gel, which was previously activated with low concentrations of cyanuric chloride (10.5 to 42.5 mumol/g gel). Well over 90% of the peptide used was immobilized. Three different concentrations were investigated for every immobilized tripeptide-ligand, 3.5, 7.0, and 14 mumol/g gel. The K(D) values of immobilized tripeptide-trypsin complexes were determined as well as the purifying performance and the trypsin-binding capacity of the affinity adsorbents. The K(D) values determined were in good agreement with the trypsin purification performance of the respective affinity adsorbents. The tripeptide sequence H-TPR-OH displayed the highest affinity for trypsin (K(D) 8.7 muM), whereas the sequence H-TAR-OH displayed the lowest (K(D) 38 muM). Dipeptide-ligands have failed to bind trypsin. When the ligand H-TPR-OH was immobilized via its N-terminal on agarose, at a concentration of 14 mumol/g gel, it produced the most effective affinity chromatography adsorbent. This adsorbent exhibited high trypsin-binding capacity (approximately 310,000 BAEE units/mL of adsorbent); furthermore, it purified trypsin from pancreatic crude extract to a specific activity of 15,200 BAEE units/mg (tenfold purification), and 82% yield. (c) 1997 John Wiley & Sons, Inc.     

Optimization of alkyl beta-D-galactopyranoside synthesis from lactose using commercially available beta-galactosidases

Commercially available lactase (beta-D-galactoside galactohydrolase, EC 3.2.1.23) enzymes produced from Kluyveromyces fragilis and Kluyveromyces lactis were accessed as catalysts for use in the production of beta-galactopyranosides of various alcohols using lactose as galactosyl donor. The yield of galactoside was enhanced by using the highest practical concentrations of both lactose and alcohol acceptor. The concentrations and thus yield, were limited by the solubility of the substrates. The increase in galactoside yield with increasing lactose concentration appeared to be specific to the lactose substrate and not due to water activity alterations, because addition of maltose to a fixed concentration of lactose had no effect. During the course of the reaction, the yield of galactoside peaked after around 70% to 80% of the lactose was consumed, due to hydrolysis of the product by the enzyme. A wide variety of compounds with primary or secondary hydroxyl groups could act as acceptors, the essential requirement being at least some water solubility. Addition of organic cosolvents had little effect on galactoside yield except when it increased the water solubility of sparingly soluble alcohols. Some galactosides were synthesized on a gram scale to determine practical product recoveries and improve purification methods for large-scale synthesis. Initial purification by hydrophobic chromatography (for galactosides of hydrophobic alcohols) or strong anion-exchange chromatography (for galactosides of hydrophilic alcohols) separated galactosides, galactobiosides, and higher oligomers from reducing sugars. A facile separation of the galactoside and galactobioside could then be effected by flash chromatography on silica gel. (c) 1993 John Wiley & Sons, Inc.     

交联琼脂糖珠固定化蛋白酶在纯化牛肺Kunitz抑制剂中的应用

本文介绍了珠状交联琼脂糖及以此作为载体,经氯代环氧丙烷活化后与蛋白酶(胰蛋白酶或糜蛋白酶)结合,制成固定化蛋白酶亲和吸附剂,进而用以亲和层析牛肺提取液中的Kunitz抑制剂的方法。纯化出的抑制剂在SDS-聚丙烯酰胺凝胶电泳上呈现单一条带,与参照物Trasytol(商品Kunitz抑制剂)具有相对应的电泳迁移率,其分子量也相符。纯化产品每毫克蛋白的抑制活力相当于16 000胰蛋白酶BAEE单位。纯化效果为90倍,收率约85％。     

用于MALDI-TOF MS分析的毛细管层析柱制备方法研究

研究了一种用于MALDI-TOF MS分析中样品预处理毛细管亲和层析柱的制备方法。首先采用硫酸和双氧水氧化法将羟基引入到石英毛细管内表面,进一步使用氨基丙基三乙氧基硅烷（APTES）对毛细管进行修饰以将氨基偶联到毛细管内表面;采用1,4-丁二醇二缩水甘油醚（BDDE）将魔芋葡甘聚糖（KGM）进行活化,将活化后的KGM与毛细管上的氨基进行了偶联,在此基础上将模型蛋白（胰蛋白酶）偶联到毛细管内KGM,成功制备出毛细管亲和层析柱,考察了KGM和环氧基含量对模型蛋白偶联量及其样品预处理效果的影响。结果表明,KGM分子量是影响毛细管层析柱上蛋白偶联量的关键因素,以胰蛋白酶抑制剂为目标物结合MALDI-TOF MS对亲和层析柱的分离效果进行了评价,证明了偶联胰蛋白酶的毛细管层析柱可有效实现胰蛋白酶抑制剂的分离和浓缩。基于表面处理和KGM衍生的毛细管亲和层析柱制备技术具有可行性,并可用于MALDI-TOF MS分析的样品预处理。     

Biocatalytic synthesis of fluorinated polyesters

The biocatalytic synthesis of fluorinated polyesters from activated diesters and fluorinated diols has been investigated. The effects of time, continuous enzyme addition, enzyme concentration, and diol chain length were studied to determine the factors that would limit chain extension, such as enzyme inactivation, enzyme specificity, the equilibrium position for the reaction, hydrolytic side reactions, and polymer precipitation. An enzyme screen demonstrated that only Novozym 435, an immobilized lipase from Candida antarctica, was effective in producing the fluorinated polyester. Molecular weight and polydispersity analyses were performed by means of gel permeation chromatography. End group analysis was accomplished through the use of matrix-assisted laser desorption/ionization time-of-flight mass spectroscopy. Polymer molecular weight steadily increased and then leveled off after approximately 30 h, with a weight average molecular weight of approximately 1773. The majority of the polymer chains were terminated with either hydroxyl or vinyl groups. Polymers that were synthesized from bulk monomers had higher molecular weights, but high enzyme concentrations were required. Enzyme specificity toward shorter chain fluorinated diols appeared to be the governing factor in limiting chain growth. However, polymer molecular weight increased further (M(w) = 8094) when a fluorinated diol that contained an additional methylene spacer between the fluorine atoms and hydroxyl groups was used.     

A continuous affinity ultrafiltration process for trypsin purification

A continuous process has been devised and tested for purification of a crude trypsin preparation from pig pancreas. The development was based on the principles of affinity chromatography and Ultrafiltration. Trypsin was selectively attracted by a water-soluble high molecular weight (>100,000) polymer, bearing a potent and specific trypsin inhibitor, m-aminobenzamidine. The trypsin-macroligand complex was then retained by using an appropriate Ultrafiltration membrane, while impurities could pass through. The bound trypsin was eluted by either arginine or benzamidine. The process also featured provision for recirculation of the eluant as well as the macroligand. It was demonstrated that this purification process could purify trypsin from the crude preparation with a yield of 77%, contaminated with only 3% of impurities. For the first time, a serious attempt has been made toward continuous purification of enzymes by the affinity Ultrafiltration technique. Besides a substantial increase in productivity, the affinity polymer could be easily reconditioned and expected to possess a long operative life. Such characteristics undoubtedly will play an important role in reducing the cost of trypsin purification.     

Homogeneous phase synthesis of cellulose carbamate silica hybrid materials using 1-n-butyl-3-methylimidazolium chloride ionic liquid medium

Cellulose carbamate silica hybrid materials can be prepared in 78–84% yield using the homogeneous phase reaction of 3-(triethoxysilyl)propyl isocyanate with cellulose dissolved in 1-n-butyl-3-methylimidazolium chloride ionic liquid and then using NH₄OH catalyzed hydrolysis of triethoxysilyl groups and the sol–gel process. New cellulose carbamate silica hybrid materials produced were characterized by elemental analysis, FT-IR, and TG-DTA. The hydrophilic affinity of these materials is shown to decrease with the degree of substitution of the cellulose hydroxyl groups with carbamate groups.     

An activated medium with high durability and low nonspecific adsorption: application to protein A chromatography

Activated media allow the user to easily synthesize a variety of affinity media. We have developed a novel activated medium based on porous silica modified with phosphorylcholine (PC) and N-hydroxysuccinimide (NHS) groups for the purpose of high-throughput purification and reducing nonspecific protein adsorption. The PC groups function as suppressors of nonspecific protein adsorption, whereas the NHS groups are able to covalently bind to the primary amino groups of ligands. Because protein A affinity medium is the most frequently used affinity medium, we prepared protein A media in which a recombinant protein A was bound to the NHS groups of the activated media and evaluated its utility. After optimizing various factors in the synthetic process, the resultant protein A medium showed improved durability at a high flow rate over 300 purification cycles and reduced nonspecific protein adsorption compared with commercially available protein A media.     

Chemically modified porous silica gel as a bioadsorbent and a biocatalyst.

Aminopropyl silica gel was prepared from porous silica gel by reaction with γ-aminopropyltrimethoxysilane in toluene and was used for immobilizing chymotrypsin (EC 3.4.4.5) and human serum albumin. Immobilized chymotrypsin was used for the resolution of N-acetyl-dl-phenylalanine and immobilized human serum albumin was used for the purification of goat anti-human serum albumin. Epoxy silica gel, prepared by reaction of porous silica gel with γ-glycidoxypropyltriethoxysilane, was coupled with m-aminobenzamidine and the resulting matrix was used for trypsin purification.     

Purification of recombinant aprotinin from transgenic corn germ fraction using ion exchange and hydrophobic interaction chromatography

Plants have attracted interest as hosts for protein expression because of the promise of a large production capacity and a low production cost. However, recovery costs remain a challenge as illustrated for recovery of recombinant aprotinin, a trypsin inhibitor, with removal of native corn trypsin inhibitor from transgenic corn (Azzoni et al. in Biotechnol Bioeng 80:268–276, 2002). When expression is targeted to corn grain fractions, dry milling can separate germ and endosperm fractions. Hence, only the product-containing fraction needs to be extracted, reducing the cost of extraction and the impurity level of the extract. Selective extraction conditions can reduce impurity levels to the point that low-cost adsorbents can result in relatively high purity levels. In this work, we attempted to achieve comparable purity with these lower cost methods. We replaced whole grain extraction and purification of recombinant aprotinin with sequential trypsin affinity and IMAC steps with an alternative of germ fraction extraction and purification with ion exchange and hydrophobic interaction chromatography (HIC). Using germ extraction at acidic pH supplemented with heat precipitation to remove additional host proteins resulted in a higher specific activity feed to the chromatographic steps. The cation exchange step provided 7.6× purification with 76.4% yield and no sodium dodecyl sulfate–polyacrylamide gel electrophoresis detectable native corn trypsin inhibitor. After the HIC step (2.7× step purification with 44.0% yield), the final product had a specific activity that was 75.3% of that of the affinity-purified aprotinin.     

Design of novel cationic ligands for the purification of trypsin-like proteases by affinity chromatography

A number on new cationic ligands have been designed and synthesized for the selective resolution an purification of the trypszin-like proteases. A series of ligands based on 4-[2′-methyl-4′-(2″,4″-dichloro-1″,3″,5″-triazin-6-ylamino) phenylazo]benzamidine were able to bind to trypsin and the trypsin-like proteases, thrombin and urokinase, but bound pancreatic kallikrein only weakly. Ligands possessing a second cationic group (either 4-aminophenyltrimethylammonium or 4-aminobenzamidine) substituted onto the triazine ring displayed higher affinities than the parent compound for trypsin in solution but bound the enzyme weakly or not at all after immobilization. In contrast, these bis-cationic ligands bound pancreatic kallikrein in solution ad following immobilization. The presence of the second cationic group was crucial, since its replacement by neutral or anionic groups led to loss of affinity for pancreatic kallikrein. One of the bis-cationic ligands was used to purify pancreatic kallikrein 9.5-fold from a crude pancreatic extract in 79% yield, to generate a product 99.9% free of contaminating trypsin activity.     

Photochemical synthesis of simple organic free radicals on simulated planetary surfaces—An ESR study

Electron spin resonance spectroscopy provided evidence for formation of hydroxyl radicals during ultraviolet photolysis (254 nm) at −170°C of H₂O adsorbed on silica gel or of silica gel alone. The carboxyl radical was observed when CO or CO₂ or a mixture of CO and CO₂ adsorbed on silica gel at −170°C was irradiated. The ESR signals of these radicals slowly disappeared when the irradiated samples were warmed to room temperature. However, re-irradiation of CO or CO₂, or the mixture CO and CO₂ on silica gel at room temperature then produced a new species, the carbon dioxide anion radical, which slowly decayed and which was identical with that produced by direct photolysis of formic acid adsorbed on silica gel. The primary photochemical process may involve formation of hydrogen and hydroxyl radicals by means of (1) photodissociation of H₂O physically adsorbed on the silica gel, or (2) absorption of the excitation energy by the silica gel surface with subsequent cleavage of the silanol bonds, or (3) dissociation of H₂O molecules through photosensitization by the surfaces or a combination of (1) to (3). Subsequent reactions of these radicals with adsorbed CO or CO₂ or both yield carboxyl radicals, CO₂H, the precursors of formic acid. Our results confirm the formation of formic acid under simulated. Martian conditions and provide a mechanistic basis for gauging the potential importance of gas-solid photochemistry for chemical evolution on other extraterrestrial bodies, on the primitive earth and on dust grains in the interstellar medium.     

Rechargeable biocidal cellulose: Synthesis and application of 3-(2,3-dihydroxypropyl)-5,5-dimethylimidazolidine-2,4-dione

An N-halamine precursor containing two hydroxyl groups (diol) has been synthesized. The N-halamine diol precursor was coated onto cotton fabrics with the assistance of the cross-linking agent BTCA. The surface of the coated cotton could be rendered biocidal by exposure to dilute hypochlorite solutions. Syntheses routes, characterization data, and antimicrobial test results will be presented. The durability and rechargeability of chlorine on the coated cotton was determined according to an AATCC standard washing test. The chlorinated cotton swatches were challenged with Staphylococcus aureus (ATCC 6538) and Escherichia coli O157:H7 (ATCC 43895) and showed excellent efficacy against these two bacterial species within a brief time of contact. Over 70% of the chlorine lost after repeated washing or UVA irradiation could be regained upon rechlorination.     

Synthesis and characterization of a water-soluble affinity polymer for trypsin purification

A specific ligand bound polymer has been synthesized for the purpose of purification and stabilization of trypsin, an easily autodigestible enzyme. The affinity polymer was formed by copolymerizing N-acryloyl-m-aminobenzamidine, a strong trypsin inhibitor, and acrylamide in the absence of oxygen. Kinetic studies on the trypsin inhibition revealed that there was a strong binding between this enzyme and the polymer and the mechanism was of a competitive manner with an inhibition constant of 0.6 x 10(-3)M. Such an affinity polymer was also very effective in preventing trypsin from auto-digestion at 4 degrees C.Based on this finding and the principle of cross flow filtration, a new process has been developed for purification of trypsin from a solution containing chymotrypsin. The experimental data indicated that trypsin was bound to the polymer (MW > 10(5)) and remained in the retentate while unbound chymotrypsin was collected in the filtrate. This purification process has a capability of recovering 98% pure trypsin at 90% yield.     

Stereoselectivity of microsomal epoxide hydrolase toward diol epoxides and tetrahydroepoxides derived from benz[a]anthracene

We have examined the selectivity of rat liver microsomal epoxide hydrolase (EC 3.3.2.3) toward all of the possible positional isomers of benzo-ring diol epoxides and tetrahydroepoxides of benz[a]anthracene, as well as the 1,2-diol 3,4-epoxides of triphenylene. This set includes compounds with no bay region in the vicinity of the benzo-ring, a bay-region diol group, a bay-region epoxide group, and (for the triphenylene derivatives) both a bay-region diol and a bay-region epoxide. In all cases where both the tetrahydroepoxides and the corresponding diol epoxides were examined, there is a large retarding effect of hydroxyl substitution on the rate of the enzyme-catalyzed hydration. When the tetrahydroepoxides are fair or poor substrates (epoxide group in the 1,2-, 8,9-, or 10,11-position), the additional retardation introduced by adjacent hydroxyl groups causes the enzyme-catalyzed hydrolysis of the corresponding diol epoxides to be insignificantly slow or nonexistent. In contrast, a benz[a]anthracene derivative with an epoxide group in the 3,4-position, (-)-tetrahydrobenz[a]anthracene (3R,4S)-epoxide, has been identified as the best substrate known for epoxide hydrolase, with a Vmax at 37 degrees C and pH 8.4 of 6800 nmol/min/mg of protein, and the two diastereomeric (+/-)-benz[a]anthracene 1,2-diol 3,4-epoxides, unlike all the other diol epoxides examined to date, are moderately good substrates for epoxide hydrolase. This novel observation is accounted for by the fact that the very high reactivity of the tetrahydrobenz[a]anthracene 3,4-epoxide system towards epoxide hydrolase is large enough to overcome a kinetically unfavorable effect of hydroxyl substitution. The enantioselectivity and positional selectivity of the enzyme have been determined for the tetrahydro-1,2- and -3,4-epoxides of benz[a]anthracene as well as the 1,2-diol 3,4-epoxides. When the epoxide is located in the 3,4-position, the benzylic carbon is the preferred site of attack, whereas for the enantiomers of the bay-region tetrahydro-1,2-epoxides, the chemically less reactive non-benzylic carbon is preferred. The regio- and enantioselectivity of epoxide hydrolase are discussed in terms of a possible model for the hydrophobic binding site of this enzyme.     

Separation of bioactive biflavonoids from Rheedia gardneriana using chitosan modified with benzaldehyde

This paper shows the influence of benzenic groups on the chitosan surface for the separation of bioactive biflavonoids from Rheedia gardneriana leaves The yield of the biflavonoids using chitin modified with benzaldehyde (CH-Bz) as adsorbent in column chromatography was higher than that achieved with silica gel and chitosan. The presence of benzenic groups decreases the polarity of chitosan and consequently the interaction of hydrogen bonding between phenolic hydroxyl (OH) of biflavonoids and amine groups of the adsorbent. Therefore, the separation of these compounds appears to be the result of hydrophobicity and pi-pi interaction among electrons from the aromatic ring in sorbent and biflavonoid molecules.     

N-hydroxysuccinimide carbonates and carbamates are useful reactive reagents for coupling ligands to lysines on proteins

Ligands containing amino or hydroxyl groups were converted to their corresponding activated N-hydroxysuccinimidyl carbamate and carbonate by reaction with disuccinimidyl carbonate (DSC). The latter reagents can be used for the group-specific modification of primary amines as an alternative to the widespread usage of N-hydroxysuccinimide esters. Biotin and 2,4-dinitrophenyl (DNP) derivatives were used as examples to demonstrate the approach. Biotin and DNP were each extended by attaching two different spacer arms, carrying either a hydroxyl group or a primary amine as terminal functions. The latter were then activated via their conversion to N-hydroxysuccinimide carbonates and carbamates, respectively. The usefulness of these reagents for protein modification was investigated. The modified proteins obtained exhibited similar stability and activity characteristics compared to those modified with active N-hydroxysuccinimdyl esters. The activation of hydroxy- or amino-terminating compounds with DSC represents a general method that can be applied to any ligand which contains these functional groups for its covalent coupling to amines.     

A novel downstream process for 1,3-propanediol from glycerol-based fermentation

In this paper, a downstream process for purification of 1,3-propanediol from glycerol-based fermentation broth was investigated. The purification of 1,3-propanediol from fermentation broth was achieved by a process combining microfiltration, charcoal treatment, vacuum distillation, and silica gel chromatography. The broth was first filtered through hollow fiber cartridge, wherein 98.7% of biomass was removed. Soluble proteins and other color impurities in the broth were removed by the use of activated charcoal at optimal concentration of 30 g l⁻¹ where the soluble proteins in the broth decreased to 0.1 g l⁻¹ (96.0% protein loss). The obtained broth when concentrated by vacuum distillation resulted in the crystallization of inorganic salts. Subsequently, 1,3-propanediol was purified by gradient chromatography using silica gel as a stationary phase and mixture of chloroform and methanol as a mobile phase. Finally, with the optimal flow rate of 10 ml min⁻¹ and loading amount of 80 ml, the yield of 1,3-propanediol achieved was 89%. The overall yield of 1,3-propanediol using the proposed procedure was 75.47%. The developed method was found to be a simple, rapid, and efficient procedure for the purification of 1,3-propanediol from fermentation broth.