Preparative resolution of D,L-threonine catalyzed by immobilized phosphatase

Hydrolysis of L- and D-O-phosphothreonines catalyzed by four different phosphatases, alkaline phosphatases from calf intestine and E. coli and acid phosphatases from wheat germ and potato, has been kinetically studied. Alkaline phosphatases were found to have comparable reactivities towards the optical isomers. On the other hand, both acid phosphatases displayed a marked stereoselectivity, hydrolyzing the L-ester much faster than its D counterpart. Wheat germ acid phosphatase was the most stereoselective enzyme: V(L)/V(D) = 24 and K(m,L)/K(m,D) = 0.17. This enzyme was immobilized (in k-carrageenan gel, followed by crosslinking with glutaraldehyde) and used for the preparative resolution of D,L-threonine: the latter was first chemically O-phosphorylated and then asymmetrically hydrolyzed by the immobilized phosphatase. As a result, gram quantities of L-threonine of high optical purity and O-phospho-D-threonine were prepared. Immobilized wheat germ phosphatase has been tested for the resolution of other racemic alcohols: serine, 2-amino-1-butanol, 1-amino-2-propanol, 2-octanol, and menthol. In all those cases, the enzyme was either not sufficiently stereoselective or too slow for preparative resolutions.     

Preparative production of hydroquinone from benzoquinone catalysed by immobilized d-glucose oxidase

Benzoquinone can replace O₂ as an electron acceptor in the oxidation of d-glucose catalysed by A. niger d-glucose oxidase. As a result, a useful chemical, hydroquinone, is formed in nearly 100% yield. A column packed with d-glucose oxidase immobilized onto alumina was operated for two weeks with no measurable decline in its catalytic efficiency and produced more than one hundred grams of hydroquinone.     

Preparative separation and bioactivity of oligomeric proanthocyanidins

Phytochemistry Reviews - Oligomeric proanthocyanidins are among the most widely distributed polyphenols in the plant kingdom, being endowed with antioxidant, anti-inflammatory, antimicrobial,...     

Enzymatic polymerization catalyzed by immobilized endoglucanase on gold

Enzymatic polymerization was carried out on gold by immobilized genetically engineered endoglucanase II (EGII) from Trichoderma viride , and the polymerization behavior and the produced cellulose were analyzed in comparison with those by free enzymes. Mutant EGIIs were EGII(core2) and EGII(core2H), which consist of two sequential catalytic core domains with one His-tag (His6) on N-terminal and with totally two His-tags on both terminals, respectively. His-tagged EGIIs were immobilized via Ni chelators of nitrilotriacetic acid (NTA) introduced on gold surface. From SPR measurements, the affinity of EGII(core2H) to the surface was higher than that of EGII(core2), and the molecular occupation area of EGII(core2H) was larger than that of EGII(core2), indicating that EGII(core2H) was immobilized with utilizing two His-tags introduced on both terminals. The hydrolytic activity of the immobilized EGII(core2H) using cellohexaose as substrate was slightly lower than that of free EGII(core2H) when they were compared at the same amount in the hydrolytic system. Enzymatic polymerization catalyzed by both immobilized EGII(core2) and EGII(core2H) proceeded with producing highly crystalline cellulose in comparison with free enzyme. Immobilization of the endoglucanase is thus effective to obtain crystalline cellulose due to the high density of the catalytic domain on gold.     

Kinetics and mechanisms of reactions catalyzed by immobilized lipases*

This review focuses on the kinetics of several modes of immobilization of lipases, on the mechanisms of reactions of activation of immobilized lipases, and on the kinetics and mechanisms of reactions catalyzed by immobilized lipases. A comprehensive overview of the state of the art pertaining to structural features of lipases is provided as an aid to understand immobilization, interfacial activation, and catalytic performance. General rate expressions are duly derived; more frequent simplifying assumptions are stated and the results thereof listed. Physicochemical and statistical significance of parameters in rate expressions fitted to experimental data are also discussed whenever possible.     

Preparative separation of small molecular weight peptides from casein hydrolysate using gel filtration and immobilized metal ion affinity chromatography

A two step method consisting of a gel filtration step, followed by a Immobilized Metal Affinity Chromatography (IMAC) step using a IDA-Cu coupled Sephadex G-25 column, on a preparative scale is described for the group separation of peptides from a casein hydrolysate. The 48 groups of peptides thus separated are further characterised by RP-HPLC and amino acid analysis. Some peptides after the analytical RP-HPLC step are further characterised by sequencing. An insight into the mechanism of retention on IMAC of the peptides is attempted. In such complex mixtures as casein hydrolysate, the peptide-peptide interaction can mask the potential sites of interactions in a single peptide. The results obtained using volatile buffers as eluents show the possibility of using IMAC step as an alternative to obtain gram quantities of group of peptides free of salts from complex protein hydrolysates.     

Preparative 2'-reduction of ATP catalyzed by ribonucleotide reductase purified by liquid-liquid extraction

Recombinant Lactobacillus leichmannii ribonucleosidetriphosphate reductase (RTPR, E.C.1.17.4.2) constitutively expressed by E. coli HB101 pSQUIRE has been purified from sonicated cell material in a one-step procedure by PEG 4000 (16% (w/w))/phosphate (7% (w/w)) liquid-liquid extraction. A high yield of 75.1% RTPR in the top phase and a partitioning of 8.5:1 between total RTPR activity in top and bottom phase were obtained in this preparative system. The RTPR-containing top phase was used to reduce ATP in the 2'-position on a gram scale with high final conversion and yield proving the ribonucleotide reductase approach feasible for the preparative synthesis of 2'-deoxyribonucleotides. High concentrations of sodium acetate in the reaction served to substitute for allosteric effectors of RTPR. 1,4-Dithio-DL-threitol was used as an artificial reducing agent for RTPR.     

Kinetic modeling of interesterification reactions catalyzed by immobilized lipase

Kinetic data for lipase-catalyzed interesterification reactions between free fatty acids and triglycerides were collected and the dynamics of the interesterification reactions were successfully modeled using tow rate experssions requiring a total of five adjustable parameters. One rate expression describes the disappearance of the free fatty acid (octanoic or linolenic acid), and the second describes the rate of release of fatty acid residues from the triglycerides (olive oil or milkfat). This model is able to account for the effects of the concentration of all chemical species participating in interesterification throughout the entire reaction. When the data for both milkfat and olive oil were subjected to nonlinear regression analyses using the same mathematical model, the parameter estimates for both systems were comparable. In addition to reproducing the tendencies observed experimentally, simulations of the interesterification system under a variety of initial conditions provided insight into the effects of several reaction variables which could not be examined experimentally. Among the most significant findings of the simulation work are (1) there is a limit beyond which increasing the initial concentration of water produces no further increase in the initial rate of the interesterification reaction; (2) an increase in the initial concentration of lower glycerides produces a concomitant increase in the rate of the interesterification reaction; (3) the free fatty acids inhibit the rate of hydrolysis of the fatty acid residues of the triglycerides; (4) there is a limit beyond which increasing the initial concentration of triglycerides produces no significant increase in the rate of either the hydrolysis reaction or the interesterification reaction. (c) 1994 John Wiley & Sons, Inc.     

Ectoine improves yield of biodiesel catalyzed by immobilized lipase

To improve the production of biodiesel by enzymatic conversion of triglycerides in cottonseed oil, compatible solutes were added to the solvent-free methanolysis system to prevent competitive methanol inhibition on the immobilized lipase (Novozym^® 435). The results indicated that the addition of ectoine increased biodiesel synthesis using a three-step methanol addition process. The concentration of methyl ester (ME) reached a maximum of 95.0% in the presence of 1.1 mmol/l ectoine, an increase of 20.9% compared to that in the absence of ectoine. On the other hand, excess ectoine decreased the ME concentration. Ectoine was also shown to enhance reuse of the immobilized lipase, significantly improving ME concentrations in each recycling test. Total concentrations of ME with added ectoine were about 1.5 times that without ectoine during five recycling tests (molar ratio of cottonseed oil to methanol, 1:4). Enzymatic reaction kinetics showed, in the concentration ranges of 0.8–1.14 mol/l and 0.03–8 mol/l for triglyceride and methanol, respectively, that ectoine had no effect on the initial reaction rates when methanol concentrations were below 0.5 mol/l. When methanol concentration exceeded 0.5 mol/l, the addition of 0.8 mmol/l ectoine increased the initial reaction rates, and the lipase exhibited a lower affinity for methanol and higher affinity for triglyceride (kinetic parameters of K_mA increase, K_mTG decrease). However, the initial reaction rates decreased significantly when 8 mmol/l ectoine was added, with the lipase having higher affinity for methanol and lower affinity for triglyceride (K_mA decrease, K_mTG increase). The supplementation of ectoine provided a new method for the purpose of improving yield of biodiesel catalyzed by enzyme.     

Reactor optimization for alpha-1,2 glucooligosaccharide synthesis by immobilized dextransucrase

The immobilization of dextransucrase in Ca-alginate beads relies on the close association between dextran polymer and dextransucrase. However, high amounts of dextran in the enzyme preparation drastically limit the specific activity of the immobilized enzyme (4 U/mL of alginate beads). Moreover, even in the absence of diffusion limitation at the batch conditions used, the enzyme behavior is modified by entrapment so that the dextran yield increases and the alpha-1,2 glucooligosaccharides (GOS) are produced with a lower yield (46.6% instead of 56.7%) and have a lower mean degree of polymerization than with the free dextransucrase. When the immobilized catalyst is used in a continuous reaction, the reactor flow rate necessary to obtain high conversion of the substrates is very low, leading to external diffusion resistance. As a result, dextran synthesis is even higher than in the batch reaction, and its accumulation within the alginate beads limits the operational stability of the catalyst and decreases glucooligosaccharide yield and productivity. This effect can be limited by using reactor columns with length to diameter ratio > or =20, and by optimizing the substrate concentrations in the feed solution: the best productivity obtained was 3.74 g. U(-1). h(-1), with an alpha-1,2 GOS yield of 36%.     

Preparative separation of human B and T lymphocytes by free flow electrophoresis

An electrophoretic method for the quantitative separation of human B and T lymphocytes in a carrier-free system is presented. The method is based on the fact that B and T lymphocytes show marked overlap in their size and density characteristics, but differ sufficiently in surface charge to be separable by electrophoresis. The technique is performed in phosphate-buffered saline and appears to be especially suitable for the enrichment of nonstimulated, functionally intact lymphocytes which can be directly used for further immunological or biochemical studies.     

Preparative separation of DNA-ethidium bromide complexes by zonal density gradient centrifugation

Ethidium bromide-DNA complexes separated by rate-zonal sedimentation through a density gradient can be readily visualized and purified with little cross-contamination. The method is simple, rapid, and efficient.     

Preparative separation of punicalagin from pomegranate husk by high-speed countercurrent chromatography

Punicalagin, the main ingredient of pomegranate (Punica granatum L.) husk, is a high molecular weight polyphenolic compound. It has shown remarkable pharmacological activities attributed in the presence of dissociable OH groups. To isolate punicalagin, previous methods included labor intensive and expensive solid phase extractions by column chromatography (C-18, polyamides, dellulose, Sephadex Lipophilic LH-20, Diaion HP20). High-speed countercurrent chromatography (HSCCC) was used for isolation and purification of punicalagin from pomegranate husk. Using preparative HSCCC about a 350 mg amount of the crude extract was separated, yielding 105 mg of punicalagin at a high-purity of over 92%. Eighty milligrams of gallic acid was simultaneously separated as another product, at a purity of 75%.     

Esterification of phenolic acids catalyzed by lipases immobilized in organogels

Lipases from Rhizomucor miehei and Candida antarctica B were immobilized in hydroxypropylmethyl cellulose organogels based on surfactant-free microemulsions consisting of n-hexane, 1-propanol and water. Both lipases kept their catalytic activity, catalyzing the esterification reactions of various phenolic acids including cinnamic acid derivatives. High reaction rates and yields (up to 94%) were obtained when lipase from C. antarctica was used. Kinetic studies have been performed and apparent kinetic constants were determined showing that ester synthesis catalyzed by immobilized lipases occurs via the Michaelis–Menten mechanism.     

Preparative separation of four isomers of synthetic anisodamine by HPLC and diastereomer crystallization

Anisodamine (654‐1), a well‐known cholinergic antagonist, is marketed as synthetic anisodamine (mixture of four isomers, 654‐2) in China. To preparative resolution and comparison of the bioactivities of the four isomers of synthetic anisodamine, current work explores an economic and effective separation method by using preparative high performance liquid chromatography (HPLC) and diastereomer crystallization. Their absolute configurations were established by single‐crystal X‐ray diffraction and circular dichroism method. The purities of each isomer were more than 95%. Among them, 654‐2‐A2 (6R, 2′S configuration) exhibited better effect on cabachol preconditioned small intestine tension more than 654‐2 and other isomers. The direct separation method without using HPLC was tried as well, which was still on progress. This is the first report of the method for preparative separation of four isomers of synthetic anisodamine which could be used for large‐scale production in industry.     

Factors controlling initial and long-term ATP regeneration catalyzed by immobilized chromatophores

Photosynthetic ATP regeneration was measured in open reactors using immobilized Chromatophores from Rhodopseudomonas capsulata. The influence of several factors on both initial and long-term ADP photophosphorylation was studied. The effect of phosphate salts and of bovine serum albumin on the organelle activity yield was studied. Photophosphorylation was initiated either with ADP or regenerated ATP and the roles of these nucleotides were compared. Different photoreactor configurations were tested for the production of a phosphorylated compound and a flat reactor selected. The presence of inorganic pyrophosphate in the reaction medium was shown to improve the synthesis of ATP 1.4 times. Using the optimal conditions described here, the total G-6P production was 50-fold higher than in batch reactors.     

Preparative scale separation of neutral lipids and phospholipids by centrifugally accelerated thin-layer chromatography

Mixtures of lipids and phospholipids were separated by centrifugally accelerated thin-layer chromatography on a preparative scale (300-500 mg lipid mixture per run). The isolated lipids and phospholipids were identified by 1H and 13C NMR spectroscopy and their fatty acid composition was determined by GLC and GLC-MS of their methyl esters.     

Enantiomer separation by complexation SFC on immobilized Chirasil-nickel and Chirasil-zinc

The use of complexation SFC for enantiomer separation of Lewis base selectands on chiral nickel(II)- and zinc(II)-bis[(3-heptafluorobutanoyl)-10-methylene-(1R)-camphora te] chemically bonded to poly(dimethylsiloxane) (Chirasil-nickel and Chirasil-zinc) and employed as Lewis acid selectors is described. The method is especially suited for less volatile and configurationally labile racemates. The variation of the experimental parameters temperature T, pressure p and density rho of the mobile phase carbon dioxide on the retention factor k, relative retention r and chiral separation factor alpha is studied, providing insights into the mechanisms of chiral recognition under supercritical conditions. For mecoprop methyl ester (methyl 2-(4-chloro-2-methylphenoxy)propanoate) an unusual increase of alpha at increased temperature is observed on Chirasil-nickel. Supercritical carbon dioxide does not inadvertently affect the complexation equilibria between Lewis donor selectands and the Lewis acid metal selectors during complexation SFC.