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Biomedical subjects

R N Patel

Publications and source records attributed to R N Patel.

At least 55 records · Page 3Linked to original sources

Transformation of N epsilon-CBZ-L-lysine to CBZ-L-oxylysine using L-amino acid oxidase from Providencia alcalifaciens and L-2-hydroxy-isocaproate dehydrogenase from Lactobacillus confusus.

Biotransformations were developed to oxidize N epsilon-carbobenzoxy(CBZ)-L-lysine and to reduce the product keto acid to L-CBZ-oxylysine. Lysyl oxidase (L-lysine: O2 oxidoreductase, EC 1.4.3.14) from Trichoderma viride was relatively specific for L-lysine and had very low activity with N epsilon-substituted derivatives. L-Amino acid oxidase (L-amino acid: O2 oxidoreductase [deaminating], EC 1.4.3.2) from Crotalus adamanteus venom had low activity with L-lysine but high activity with N epsilon-formyl-, t-butyoxycarbonyl(BOC)-, acetyl-, trifluoroacetyl-, or CBZ-L-lysine. L-2-Hydroxyisocaproate dehydrogenase (EC 1.1.1.-) from Lactobacillus confusus catalyzed the reduction by NADH of the keto acids from N epsilon-acetyl-, trifluoroacetyl-, formyl- and CBZ-L-lysine but was inactive with the products from oxidation of L-lysine, L-lysine methyl ester, L-lysine ethyl ester or N epsilon-t-BOC-L-lysine. Providencia alcalifaciens (SC9036, ATCC 13159) was a good microbial substitute for the snake venom oxidase and also provided catalase (H2O2:H2O2 oxidoreductase EC 1.11.1.6). N epsilon-CBZ-L-Lysine was converted to CBZ-L-oxylysine in 95% yield with 98.5% optical purity by oxidation using P. alcalifaciens cells followed by reduction of the keto acid using L-2-hydroxyisocaproate dehydrogenase. NADH was regenerated using formate dehydrogenase (formate: NAD oxidoreductase, EC 1.2.1.2) from Candida boidinii. The Providencia oxidase was localized in the particulate fraction and catalase activity was predominantly in the soluble fraction of sonicated cells. The pH optima and kinetic constants were determined for the reactions.

Alcohol Oxidoreductases↗

X-band electron paramagnetic resonance spectra of bovine serum albumin-copper(II) and bovine serum albumin-copper(II)-aminoacid systems.

X-band electron paramagnetic resonance (epr) spectra of the binary systems, BSA-copper(II) (1:1 and 2:1), and the ternary systems, BSA-Cu(II)-aminoacid (1:1:1), are described. In the binary system, two distinct epr features have been observed. One of the features (towards the low pH), showing broad and overlapping epr signals, has been attributed to non-specific bonding of copper(II) to the albumin and other feature (towards higher pH), showing sharp intense epr signals, has been attributed to the specific bonding. The change from non-specific to specific binding is favoured by increase in pH as well as by increase in protein concentration. Specific binding of copper(II) in BSA-Cu(II) has been suggested to be similar to that in HSA-Cu(II). Spectra of BSA-Cu(II)-aminoacid (1:1:1) show simultaneous presence of binary BSA-Cu(II) and ternary BSA-Cu(II)-aminoacid.

Amino Acids↗

Stereospecific microbial reduction of 4,5-dihydro-4-(4-methoxyphenyl)-6-(trifluoromethyl-1H-1)-benzazepin+ ++-2-o ne.

A key intermediate, (3R-cis)-1,3,4,5-tetrahydro-3-hydroxy-4-(4-methoxyphenyl)-6-(trifluorome thyl)- 2H-1-benzazepin-2-one (compound II or SQ32191), with high optical purity was made by the stereoselective microbial reduction of the parent ketone 1. Several strains of bacterial and yeast cultures were screened for the ability to catalyse the stereoselective reduction of 4,5-dihydro-4-(4-methoxyphenyl)-6-(trifluoromethyl)-1H-1-benzazepin++ +-2,3-dione [compound I or SQ32425]. Microorganisms from the genera Nocardia, Rhodococcus, Alkaligenes, Corynebacterium, Arthrobacter, Hansenula, and Candida reduced compound I to compound II with 60-70% conversion yield. In contrast, microorganisms from the genera Pseudomonas and Acinetobacter reduced compound I stereospecifically to (trans)-1,3,4,5-tetrahydro-3-hydroxy-4-(4-methoxyphenyl)-6-(trifluoromet hyl-2H- 1-benzazepin-2-one (compound III or SQ32408). Among various cultures evaluated, N. salmonicolor SC6310 effectively catalysed the transformation of compound I to compound II with 96% conversion yield at 1.5-2.0 gl-1 concentration. Compound II was isolated and identified by NMR analysis, mass spectrometry, and comparison to an authentic sample. Preparative scale fermentation process and transformation process were developed using cell suspensions of N. salmonicolor SC6310 to catalyse the transformation of compound I to compound II. The isolated compound II had a melting point of 222 degrees C (reference 221-223 degrees C), optical rotation of +130.4 (reference +128 degrees C), and optical purity of greater than 99.9% as analyzed by NMR and chiral HPLC.

Bacteria↗

Spectroscopic properties of the hydroxylase of methane monooxygenase.

The hydroxylase component of methane monooxygenase (EC 1.14.13.25), which catalyzes the oxidation of methane to methanol, has been studied by visible, electron spin resonance and X-ray spectroscopies. The enzyme appears to possess a mu-oxo- or mu-hydroxo-bridged binuclear iron site, with no sulfur ligands to the cluster. Each Fe has 4-6 oxygen (or nitrogen) ligands, at an average distance of 1.92 +/- 0.03 A. The Fe-Fe distance is 3.05 +/- 0.05 A. Essentially all of the irons are in the Fe3+ state as the enzyme is prepared, but reduction with N-methylphenazonium methosulfate generates ESR-detectable states that appear to emanate from mixed-valence binuclear sites. One of these, with gav near 1.85, displays typical Curie law microwave saturation behavior, but the other, gav near 1.73, has a very potent method of spin-relaxation. Together they account for approximately 0.6 spins per molecule.

Binding Sites↗

Methane monooxygenase: purification and properties of flavoprotein component.

An anaerobic procedure was developed for the purification of the flavin:NADH oxidoreductase (flavoprotein) component of methane monooxygenase to homogeneity. The molecular weight of the flavoprotein determined by gel filtration was about 40,000, and by sedimentation equilibrium analysis, about 38,000. The purified flavoprotein is a monomeric protein with a sedimentation constant (S20,W) value of about 2.1 S. The absorption spectrum of the flavoprotein has a peak at 460 nm and shoulder at 395 nm. The fluorescent excitation and emission spectra of the fluorescent component of flavoprotein had peaks at 450, 370, and 530 nm, respectively. A FAD was identified as a prosthetic group of flavoprotein by thin-layer chromatography. The flavoprotein contained about 1 mol of FAD and 2 mol each of iron and acid-labile sulfide per mole of protein. The flavoprotein was directly reduced by NADH under anaerobic conditions. The formation of neutral flavin semiquinone was detected during anaerobic titration of flavoprotein by NADH and also as a free radical signal at a g value of 2.004 by EPR spectroscopy. The iron sulfur cluster has g values of 2.04, 1.96, and 1.87, yielding a g average of 1.96, characteristic of a Fe2S2 center. Antibody prepared against the flavoprotein reacted with flavoprotein and inhibited methane monooxygenase activity.

Chromatography, Gel↗

Purification and properties of the hydroxylase component of methane monooxygenase.

Methane monooxygenase from Methylobacterium sp. strain CRL-26 which catalyzes the oxygenation of hydrocarbons was resolved into two components, a hydroxylase and a flavoprotein. An anaerobic procedure was developed for the purification of the hydroxylase to homogeneity. The molecular weight of the hydroxylase as determined by gel filtration was 220,000, and that determined by sedimentation equilibrium analysis was about 225,000. The purified hydroxylase contained three nonidentical subunits with molecular weights of about 55,000, 40,000, and 20,000, in equal amounts as judged by sodium dodecyl sulfate-polyacrylamide gel electrophoresis, indicating that it is an alpha 2 beta 2 gamma 2 protein. Optical absorption spectra revealed peaks near 408 and 280 nm, and fluorescence spectra revealed emission peaks at 490 and 630 nm. The purified hydroxylase contained 2.8 +/- 0.2 mol of iron and 0.5 +/- 0.1 mol of zinc per mol of protein but negligible amounts of acid-labile sulfide. The antisera prepared against the hydroxylase showed cross-reactivity with hydroxylase components in soluble extracts from other methanotrophs.

Macromolecular Substances↗

Purification and properties of a NAD-linked 1,2-propanediol dehydrogenase from propane-grown Pseudomonas fluorescens NRRL B-1244.

NAD-dependent 1,2-propanediol dehydrogenase (EC 1.1.1.4) activity was detected in cell-free crude extracts of various propane-grown bacteria. The enzyme activity was much lower in 1-propanol-grown cells than in propane-grown cells of Pseudomonas fluorescens NRRL B-1244, indicating that the enzyme may be inducible by metabolites of propane subterminal oxidation. 1,2-Propanediol dehydrogenase was purified from propane-grown Ps. fluorescens NRRL B-1244. The purified enzyme fraction shows a single-protein band upon acrylamide gel electrophoresis and has a molecular weight of 760,000. It consists of 10 subunits of identical molecular weight (77,600). It oxidizes diols that possess either two adjacent hydroxy groups, or a hydroxy group with an adjacent carbonyl group. Primary and secondary alcohols are not oxidized. The pH and temperature optima for 1,2-propanediol dehydrogenase are 8.5 and 20-25 degrees C, respectively. The activation energy calculated is 5.76 kcal/mol. 1,2-Propanediol dehydrogenase does not catalyze the reduction of acetol or acetoin in the presence of NADH (reverse reaction). The Km values at 25 degrees C, pH 7.0, buffer solution for 1,2-propan1,2-propanediol dehydrogenase are 8.5 and 20-25 degrees C, respectively. The activation energy calculated is 5.76 kcal/mol. 1,2-Propanediol dehydrogenase does not catalyze the reduction of acetol or acetoin in the presence of NADH (reverse reaction). The Km values at 25 degrees C, pH 7.0, buffer solution for 1,2-propan1,2-propanediol dehydrogenase are 8.5 and 20-25 degrees C, respectively. The activation energy calculated is 5.76 kcal/mol. 1,2-Propanediol dehydrogenase does not catalyze the reduction of acetol or acetoin in the presence of NADH (reverse reaction). The Km values at 25 degrees C, pH 7.0, buffer solution for 1,2-propanediol and NAD are 2 X 10(-2) and 9 X 10(-5) M, respectively. The 1,2-propanediol dehydrogenase activity was inhibited by strong thiol reagents, but not by metal-chelating agents. The amino acid composition of the purified enzyme was determined. Antisera prepared against purified 1,2-propanediol dehydrogenase from propane-grown Ps. fluorescens NRRL B-1244 formed homologous precipitin bands with isofunctional enzymes derived from propane-grown Arthrobacter sp. NRRL B-11315, Nocardia paraffinica ATCC 21198, and Mycobacterium sp. P2y, but not from propane-grown Pseudomonas multivorans ATCC 17616 and Brevibacterium sp. ATCC 14649, or 1-propanol-grown Ps. fluorescens NRRL B-1244. Isofunctional enzymes derived from methane-grown methylotrophs also showed different immunological and catalytic properties.

Amino Acids↗

Thermostable NAD-linked secondary alcohol dehydrogenase from propane-grown Pseudomonas fluorescens NRRL B-1244.

NAD-linked alcohol dehydrogenase activity was detected in cell-free crude extracts from various propane-grown bacteria. Two NAD-linked alcohol dehydrogenases, one which preferred primary alcohols (alcohol dehydrogenase I) and another which preferred secondary alcohols (alcohol dehydrogenase II), were found in propane-grown Pseudomonas fluorescens NRRL B-1244 and were separated from each other by DEAE-cellulose column chromatography. The properties of alcohol dehydrogenase I resembled those of well-known primary alcohol dehydrogenases. Alcohol dehydrogenase II was purified 46-fold; it was homogeneous as judged by acrylamide gel electrophoresis. The molecular weight of this secondary alcohol dehydrogenase is 144,500; it consisted of four subunits per molecule of enzyme protein. It oxidized secondary alcohols, notably, 2-propanol, 2-butanol, and 2-pentanol. Primary alcohols and diols were also oxidized, but at a lower rate. Alcohols with more than six carbon atoms were not oxidized. The pH and temperature optima for secondary alcohol dehydrogenase activity were 8 to 9 and 60 to 70 degrees C, respectively. The activation energy calculated from an Arrhenius plot was 8.2 kcal (ca. 34 kJ). The Km values at 25 degrees C, pH 7.0, were 8.2 X 10(-6) M for NAD and 8.5 X 10(-5) M for 2-propanol. The secondary alcohol dehydrogenase activity was inhibited by strong thiol reagents and strong metal-chelating agents such as 4-hydroxymercuribenzoate, 5,5'-dithiobis(2-nitrobenzoic acid), 5-nitro-8-hydroxyquinoline, and 1,10-phenanthroline. The enzyme oxidized the stereoisomers of 2-butanol at an equal rate. Alcohol dehydrogenase II had good thermal stability and the ability to catalyze reactions at high temperature (85 degrees C). It appears to have properties distinct from those of previously described primary and secondary alcohol dehydrogenases.

Alcohol Dehydrogenase↗

Erythrocyte survival in patients with porcine xenograft aortic and mitral valves.

Ten patients with porcine xenograft aortic and mitral valve prostheses were studied three to 36 months (mean 15 months) postoperatively for evidence of hemolysis. Studies included complete blood count, reticulocyte count, red cell indices, percentage of schistocytes on blood smears, bilirubin concentration, lactic dehydrogenase, serum iron, total iron binding capacity, haptoglobin, serum folate and vitamin B12 levels, Coombs' test, methemoglobin reduction test, autologous 51Cr erythrocyte survival, and urinary examination for iron and hemosiderin. All patients were hemodynamically stable. Nine patients had normal valve function and no evidence of hemolysis. One patient with paravalvular aortic regurgitation had mechanical hemolytic anemia with a negative Coombs' test. Porcine valve xenografts do not seem to be associated with hemolysis unless complicated by a paravalvular leak.

Anemia, Hemolytic↗

Microbial Oxidation of Hydrocarbons: Properties of a Soluble Methane Monooxygenase from a Facultative Methane-Utilizing Organism, Methylobacterium sp. Strain CRL-26.

Methylobacterium sp. strain CRL-26 grown in a fermentor contained methane monooxygenase activity in soluble fractions. Soluble methane monooxygenase catalyzed the epoxidation/hydroxylation of a variety of hydrocarbons, including terminal alkenes, internal alkenes, substituted alkenes, branched-chain alkenes, alkanes (C(1) to C(8)), substituted alkanes, branched-chain alkanes, carbon monoxide, ethers, and cyclic and aromatic compounds. The optimum pH and temperature for the epoxidation of propylene by soluble methane monooxygenase were found to be 7.0 and 40 degrees C, respectively. Among various compounds tested, only NADH(2) or NADPH(2) could act as an electron donor. Formate and NAD (in the presence of formate dehydrogenase contained in the soluble fraction) or 2-butanol in the presence of NAD and secondary alcohol dehydrogenase generated the NADH(2) required for the methane monooxygenase. Epoxidation of propylene catalyzed by methane monooxygenase was not inhibited by a range of potential inhibitors, including metal-chelating compounds and potassium cyanide. Sulfhydryl agents and acriflavin inhibited monooxygenase activity. Soluble methane monooxygenase was resolved into three components by ion-exchange chromatography. All three compounds are required for the epoxidation and hydroxylation reactions.

Journal Article↗

Microbial oxidation of gaseous hydrocarbons: production of alcohols and methyl ketones from their corresponding n-alkanes by methylotrophic bacteria.

Cell suspensions of methane-utilizing bacteria oxidized n-alkanes (propane, butane, pentane, and hexane) to their corresponding alcohols and methyl ketones. The product alcohols and methyl ketones accumulated extracellularly. Methanol-grown cells of methane-utilizing bacteria did not oxidize n-alkanes. The product primary alcohol was detected in a cell-free system but only in a trace amount in the whole cell system due to further oxidation. The optimum conditions for in vivo formation of secondary alcohol and methyl ketone from n-alkanes were compared between two distinct types of C1-utilizing microbes: Methylococcus capsulatus M1 (type I membrane) and Methylosinus trichosporium OB3b (type II membrane). The production of acetone or 2-butanone from n-alkanes ceased after 3 h of incubation for strain OB3b and 5 h for strain M1. The amount of these methyl ketones did not decline during 30 h of incubation. The optimum pH for the in vivo production of methyl ketones from n-alkanes by both strains was around 7.0. However, secondary alcohols were accumulated at higher amounts around pH 6.0. The optimum temperature for the in vivo production of methyl ketones from n-alkanes was around 40 degrees C for strain M1 and around 30-35 degrees C for strain OB3b. Higher accumulation of secondary alcohol was detected at 30-40 degrees C for strain M1 and 25 degrees C for strain OB3b. The alkane hydroxylation enzyme was located in the cell-free particulate fraction precipitated between 10 000 and 40 000 X g centrifugation. The yield of primary and secondary alcohols from n-alkane in the cell-free system was about equal. Evidence obtained indicates that the hydroxylation of n-alkanes (both terminal and subterminal oxidations) is also catalyzed by the methane hydroxylation - alkene epoxidation enzyme system.

Alcohols↗

Microbial Oxidation of Gaseous Hydrocarbons: Production of Secondary Alcohols from Corresponding n-Alkanes by Methane-Utilizing Bacteria.

Over 20 new strains of methane-utilizing bacteria were isolated from lake water and soil samples. Cell suspensions of these and of other known strains of methane-utilizing bacteria oxidized n-alkanes (propane, butane, pentane, hexane) to their corresponding secondary alcohols (2-propanol, 2-butanol, 2-pentanol, 2-hexanol). The product secondary alcohols accumulated extracellularly. The rate of production of secondary alcohols varied with the organism used for oxidation. The average rate of 2-propanol, 2-butanol, 2-pentanol, and 2-hexanol production was 1.5, 1.0, 0.15, and 0.08 mumol/h per 5.0 mg of protein in cell suspensions, respectively. Secondary alcohols were slowly oxidized further to the corresponding methylketones. Primary alcohols and aldehydes were also detected in low amounts (rate of production were 0.05 to 0.08 mumol/h per 5.0 mg of protein in cell suspensions) as products of n-alkane (propane and butane) oxidation. However, primary alcohols and aldehydes were rapidly metabolized further by cell suspensions. Methanol-grown cells of methane-utilizing bacteria did not oxidize n-alkanes to their corresponding secondary alcohols, indicating that the enzymatic system required for oxidation of n-alkanes was induced only during growth on methane. The optimal conditions for in vivo secondary alcohol formation from n-alkanes were investigated in Methylosinus sp. (CRL-15). The rate of 2-propanol and 2-butanol production was linear for the 40-min incubation period and increased directly with cell protein concentration up to 12 mg/ml. The optimal temperature and pH for the production of 2-propanol and 2-butanol were 40 degrees C and pH 7.0. Metalchelating agents inhibited the production of secondary alcohols. The activities for the hydroxylation of n-alkanes in various methylotrophic bacteria were localized in the cell-free particulate fractions precipitated by centrifugation between 10,000 and 40,000 x g. Both oxygen and reduced nicotinamide adenine dinucleotide were required for hydroxylation activity. The metal-chelating agents inhibited hydroxylation of n-alkanes by the particulate fraction, indicating the involvement of a metal-containing enzyme system in the oxidation of n-alkanes. The production of 2-propanol from the corresponding n-alkane by the particulate fraction was inhibited in the presence of methane, suggesting that the subterminal hydroxylation of n-alkanes may be catalyzed by methane monooxygenase.

Journal Article↗

Microbial Oxidation of Gaseous Hydrocarbons: Production of Methylketones from Corresponding n-Alkanes by Methane-Utilizing Bacteria.

Cell suspensions of methane-utilizing bacteria grown on methane oxidized n-alkanes (propane, butane, pentane, hexane) to their corresponding methylketones (acetone, 2-butanone, 2-pentanone, 2-hexanone). The product methylketones accumulated extracellularly. The rate of production of methylketones varied with the organism used for oxidation; however, the average rate of acetone, 2-butanone, 2-pentanone, and 2-hexanone production was 1.2, 1.0, 0.15, and 0.025 mumol/h per 5.0 mg of protein in cell suspensions. Primary alcohols and aldehydes were also detected in low amounts as products of n-alkane (propane and butane) oxidation, but were rapidly metabolized further by cell suspensions. The optimal conditions for in vivo methylketone formation from n-alkanes were compared in Methylococcus capsulatus (Texas strain), Methylosinus sp. (CRL-15), and Methylobacterium sp. (CRL-26). The rate of acetone and 2-butanone production was linear for the first 60 min of incubation and directly increased with cell concentration up to 10 mg of protein per ml for all three cultures tested. The optimal temperatures for the production of acetone and 2-butanone were 35 degrees C for Methylosinus trichosporium sp. (CRL-15) and Methylobacterium sp. (CRL-26) and 40 degrees C for Methylcoccus capsulatus (Texas). Metal-chelating agents inhibited the production of methylketones, suggesting the involvement of a metal-containing enzymatic system in the oxidation of n-alkanes to the corresponding methylketones. The soluble crude extracts derived from methane-utilizing bacteria contained an oxidized nicotinamide adenine dinucleotide-dependent dehydrogenase which catalyzed the oxidation of secondary alcohols.

Journal Article↗