The kinetic behavior of chicken liver sulfite oxidase.

A comprehensive kinetic study of sulfite oxidase has been undertaken over the pH range 6.0-10.0, including conventional steady-state work as well as rapid kinetic studies of both the reaction of oxidized enzyme with sulfite and reduced enzyme with cytochrome c (III). A comparison of the pH dependence of kcat, kred, and kox indicates that kred is principally rate limiting above pH 7, but that below this pH the pH dependence of kcat is influenced by that of kox. The pH independence of kred is consistent with our previous proposal concerning the reaction mechanism, in which attack of the substrate lone pair of electrons on a Mo(VI)O2 unit initiates the catalytic sequence. The pH dependence of kred/Kdsulfite indicates that a group on the enzyme having a pKa of approximately 9.3 must be deprotonated for effective reaction of oxidized enzyme with sulfite, possibly Tyr 322, which from the crystal structure of the enzyme constitutes part of the substrate binding site. There is no evidence for the HSO3-/SO32- pKa of approximately 7 in the pH profile for kred/Kdsulfite, suggesting that enzyme is able to oxidize the two equally well. By contrast, kcat/Kmsulfite and kred/Kdsulfite exhibit distinct pH dependence (the former is bell-shaped, the latter sigmoidal), again consistent with the oxidative half-reaction contributing to the kinetic barrier to catalysis at low pH. The pH dependence of kcat/Km(cyt c) (reflecting the second-order rate of reaction of free enzyme with free cytochrome) is bell-shaped and closely resembles that of kox/Kd(cyt c), reflecting the importance of the oxidative half-reaction in the low substrate concentration regime. The pH profile for kox/Kd(cyt c) indicates that two groups with a pKa of approximately 8 are involved in the reaction of free reduced enzyme with cytochrome c, one of which must be deprotonated and the other protonated. These results are consistent with the known electrostatic nature of the interaction of cytochrome c with its physiological partners.     

Kinetic study of a phosphoryl exchange reaction between fructose and fructose 1-phosphate catalyzed by the membrane-bound enzyme II of the phosphoenolpyruvate-fructose 1-phosphotransferase system of Bacillus subtilis.

A phosphoryl exchange reaction between fructose 1-phosphate and fructose was found to be catalyzed by a membrane preparation isolated from Bacillus subtilis. The regulation of the biosynthesis of the activity in the wild type as well as in the regulation mutants fruB closely correlates with that of the membrane-bound enzyme II of the phosphoenolpyruvate fructose 1-phosphotransferase system which is known to mediate the transmembrane vectorial phosphorylation of fructose. The computed analysis of the kinetic data shows that the mechanism of the enzyme II is ping-pong, i.e. that a phosphoryl-enzyme intermediate occurs in the reaction. The apparent dissociation constants of the enzyme II/fructose 1-phosphate complex and of the phosphoryl enzyme II/fructose complex are estimated. The value of the standard free energy of the hydrolysis of the bond between the phosphoryl moiety and the enzyme suggests a covalent bonding. This intermediate is assumed to occur in the physiological functioning of the enzyme which utilizes the phosphocarrier protein HPr as phosphoryl donor. The exchange reaction is competitively inhibited by high fructose concentrations: this indicates that the same site of the enzyme binds fructose and fructose 1-phosphate, this site being accessible to fructose on the external side of the membrane when the enzyme is phosphorylated.     

Immobilization of beta-galactosidase on fibrous matrix by polyethyleneimine for production of galacto-oligosaccharides from lactose

The production of galacto-oligosaccharides (GOS) from lactose by Aspergillus oryzae beta-galactosidase immobilized on cotton cloth was studied. A novel method of enzyme immobilization involving PEI-enzyme aggregate formation and growth of aggregates on individual fibrils of cotton cloth leading to multilayer immobilization of the enzyme was developed. A large amount of enzyme was immobilized (250 mg/g support) with about 90-95% efficiency. A maximum GOS production of 25-26% (w/w) was achieved at near 50% lactose conversion from 400 g/L of lactose at pH 4.5 and 40 degrees C. Tri- and tetrasaccharides were the major types of GOS formed, accounting for about 70% and 25% of the total GOS produced in the reactions, respectively. Temperature and pH affected not only the reaction rate but also GOS yield to some extend. A reaction pH of 6.0 increased GOS yield by as much as 10% compared with that of pH 4.5 while decreased the reaction rate of immobilized enzyme. The cotton cloth as the support matrix for enzyme immobilization did not affect the GOS formation characteristics of the enzyme under the same reaction conditions, suggesting diffusion limitation was negligible in the packed bed reactor and the enzyme carrier. Increase in the thermal stability of PEI-immobilized enzyme was also observed. The half-life for the immobilized enzyme on cotton cloth was close to 1 year at 40 degrees C and 21 days at 50 degrees C. Stable, continuous operation in a plug-flow reactor was demonstrated for about 3 days without any apparent problem. A maximum GOS production of 26% (w/w) of total sugars was attained at 50% lactose conversion with a feed containing 400 g/L of lactose at pH 4.5 and 40 degrees C. The corresponding reactor productivity was 6 kg/L/h, which is several-hundred-fold higher than those previously reported.     

Kinetics of coupled enzyme reactions

A theory has been developed for the kinetics of coupled enzyme reactions. This theory does not assume that the first reaction is irreversible. The validity of this theory is confirmed by a model system consisting of enoyl-CoA hydratase (EC 4.2.1.17) and 3-hydroxyacyl-CoA dehydrogenase (EC 1.1.1.35) with 2,4-decadienoyl coenzyme A (CoA) as a substrate. This theory, in contrast to the conventional theory, proves to be indispensible for dealing with coupled enzyme systems where the equilibrium constant of the first reaction is small and/or the concentration of the coupling enzyme is higher than that of the intermediate. Equations derived on the basis of this theory can be used to calculate steady-state velocities of coupled enzyme reactions and to predict the time course of coupled enzyme reactions during the pre steady state.     

The effect of restricted hydration on the rate of reaction of glucose 6-phosphate dehydrogenase, phosphoglucose isomerase, hexokinase and fumarase. Relevance for metabolism in xeric (near-dry) conditions

A method is described for the measurement of enzyme activity under xeric conditions. The reaction mixtures had water contents ranging between 0.1 and 0.6g/g of reaction mixture. For glucose 6-phosphate dehydrogenase, hexokinase and fumarase, enzyme activity became detectable (about 0.05% of the fully hydrated rate) when the water content was about 0.2g/g of reaction mixture, and for phosphoglucose isomerase, around 0.15g/g of reaction mixture. With the water content raised to 0.3g/g of reaction mixture the reaction rates were only increased to 0.1-3% of the fully hydrated rate. When the combined rates for phosphoglucose isomerase and glucose 6-phosphate dehydrogenase were measured, reasonable agreement was found between the experimental data and those calculated from the individual experimentally determined rates on the assumption that diffusion was not further limiting. A method was devised for measuring the diffusion coefficients of low-molecular-weight substances in solutions having low water contents. The diffusion coefficients of riboflavin in sorbitol solution decreased by about 100-fold when the water content of the latter was reduced from 3 to 0.25g/g of sorbitol. It is concluded that to detect enzyme activity a certain minimal amount of water is required and that above this minimum the rate is still restricted by diffusion limitation. The relevance of the results to the physical state of water in reaction mixtures and to metabolism in seeds and spores in xeric conditions is discussed.     

Enzymatic hydrolysis of lime-pretreated corn stover and investigation of the HCH-1 Model: inhibition pattern, degree of inhibition, validity of simplified HCH-1 Model

The inhibition pattern was identified for a reaction system composed of Trichoderma reesei cellulase enzyme complex and lime-pretreated corn stover. Also, the glucose inhibition effect was quantified for the aforementioned reaction system over a range of enzyme loadings and substrate concentrations. Lastly, the range of substrate concentrations and enzyme loadings were identified in which the linear form of the simplified HCH-1 Model is valid. The HCH-1 Model is a modified Michaelis-Menton Model with non-competitive inhibition and the fraction of insoluble substrate available to bind with enzyme. With a high enzyme loading, the HCH-1 Model can be integrated and simplified in such a way that sugar conversion is linearly proportional to the logarithm of enzyme loading. A wide range of enzyme loadings (0.25-50 FPU/g dry biomass) and substrate concentrations (10-100g/L) were investigated. All experiments were conducted with an excess cellobiase loading to ensure the experimental results were not influenced by cellobiose inhibition. A non-competitive inhibition pattern was identified for the corn stover-cellulase reaction system, thereby validating the assumptions of the HCH-1 Model. At a substrate concentration of 10 g/L, glucose inhibition parameters of 0.986 and 0.979 were measured for enzyme loadings of 2 FPU/g dry biomass and 50 FPU/g dry biomass, respectively. At 5 FPU/g dry biomass, glucose inhibition parameters of 0.985 and 0.853 were measured for substrate concentrations of 10 and 100g/L, respectively. The linear form of the HCH-1 Model predicted biomass digestibility for lime-pretreated corn stover over an enzyme loading range of 0.25-50 FPU/g dry biomass and substrate concentration range of 10-100g/L.     

Kinetic studies on the reaction mechanism of sarcosine oxidase

A sarcosine oxidase (sarcosine: oxygen oxidoreductase (demethylating), EC 1.5.3.1) isolated from Corynebacterium sp. U-96 contains both covalently bound FAD and noncovalently bound FAD. The noncovalent FAD reacts with sarcosine, the covalent FAD with molecular oxygen (Jorns, M.S. (1985) Biochemistry 24, 3189-3194). To clarify the reaction mechanism of the enzyme, kinetic investigations were performed by the stopped-flow method as well as by analysis of the overall reaction. The absorption spectrum of the enzyme in the steady state was very similar to that of the oxidized enzyme, and no intermediate enzyme species, such as a semiquinoid flavin, was detected. The rate for anaerobic reduction of the noncovalently bound FAD and the covalently bound FAD by sarcosine were 31 and 6.7 s-1, respectively. The latter value was smaller than the value of respective Vmax/e0 obtained by the overall reaction kinetics (Vmax/e0: the maximum velocity per enzyme concentration). Both rate constants for oxidation of the two FADs by molecular oxygen were 100 s-1. A reaction scheme of sarcosine oxidase is proposed to account for the data obtained; 70% of the enzyme functions via a fully reduced enzyme, and 30% of the enzyme goes along a side-path, without forming the fully reduced enzyme. In addition, it is suggested that the reactivity of noncovalently bound FAD with sarcosine is affected by the oxidation-reduction state of the covalently bound FAD, in contrast to the reactivity of the covalently bound FAD with molecular oxygen, which is independent of the oxidation-reduction state of the noncovalently bound FAD.     

Purification and characterization of a pyridine nucleotide glycohydrolase from rabbit spleen

A particulate NMN glycohydrolase of rabbit spleen was solubilized with Triton X100 and purified approximately 100-fold. The enzyme was shown to have a pH maximum of 6.5, a Km of 0.25 mM, a Vmax of 5.3 mumol/min/mg protein, an activation energy of 7.9 kcal/mol, and a molecular weight of approximately 400,000. Both of the purified and the particulate enzymes exhibited identical catalytic properties with respect to substrate specificity, activation energy, pH profile and exchange reaction with nicotinic acid, except that the purified enzyme was highly activated with Triton X100 as compared with the particulate enzyme; it appears that the purified enzyme possesses the same catalytic properties as the enzyme present in the tissue and that solubilization does not significantly alter the native protein. In addition to catalytic activity with NMN, the rabbit spleen enzyme catalyzed an irreversible hydrolysis with NAD and NADP, exhibiting catalyzing activity ratios of NMN:NAD:NADP = 1.00:1.45:0.44 and Vmax/Km ratios of 1.00:1.7:2.3, respectively. These ratios of activity remained constant throughout purification of the enzyme and no separation of these activities was detected. Mutually competitive inhibition of the enzyme with Ki values similar to Km, and identical rates of thermal denaturation of the enzyme and activity-pH profiles with NMN or NAD indicated the hydrolysis of the C-N glycosidic linkage of the pyridine nucleotides to be catalyzed by the same enzyme. The enzyme was less specific for the purine structure of the substrate dinucleotides but was stereospecific for the glycosidic linkage cleaved. Nicotinamide riboside, the nicotinic acid analogs and the reduced forms were not hydrolyzed. A linear noncompetitive inhibition of NMN hydrolysis with nicotinamide indicated an ordered Uni-Bi mechanism in which nicotinamide was the first product released from the enzyme. A property that the rabbit spleen enzyme appears to share with other NAD glycohydrolases is the transglycosidation reaction. The ratio of transglycosidation reaction vs. hydrolysis catalyzed by the enzyme in the presence of NMN and nicotinic acid indicated that the enzyme could function as a primary transglycosidase rather than a hydrolytic enzyme in vivo.     

Study of coenzyme reorientation in the active center of tryptophanase by linear dichroism method

Tryptophanase from E.coli was oriented in a compressed slab of polyacrylamide gel and its linear dichroism (LD) and absorption spectra were measured. The free enzyme displays four LD bands at 305, 340, 425 and 490 nm. Two bands at 340 and 425 nm belong to the internal coenzyme-lysine aldimine. The 305 nm band apparently belongs to an aromatic amino acid residue; the sign and form of this band are changed upon the enzyme reaction with substrate analogs. The 490 nm band is present in the LD spectra of holo- and apoenzyme and disappears after treatment with NaBH4. It is suggested that the 490 nm band belongs to a quinoid enzyme subform. The reaction of tryptophanase with threo-beta-phenyl-DL-serine and L-threonine leads to formation of the external aldimine with a strong absorption band at 420-425 nm. The reduced LD (delta A/A) in this band is one order of magnitude greater than that in the 420 nm of the free enzyme. The complex with D-alanine is characterized by an intermediate LD value in the 425 nm band. In the presence of indole this complex displays the same LD as that observed with beta-phenylserine. The reaction of tryptophanase with L-alanine and oxindolyl-L-alanine leads to formation of the quinoid intermediate with a 500 nm absorption band. The LD value in this band differs from those in the absorption bands of the free enzyme. It is concluded that reorientations of the coenzyme occur in the course of the tryptophanase reaction.     

Putrescine activation of Trypanosoma cruzi S-adenosylmethionine decarboxylase

S-Adenosylmethionine decarboxylase (AdoMetDC) is a pyruvoyl-dependent enzyme that is processed from a single polypeptide into two subunits creating the cofactor. In the human enzyme, both the proenzyme processing reaction and enzyme activity are stimulated by the polyamine putrescine. The processing reaction of Trypanosoma cruzi AdoMetDC was studied in an in vitro translation system. The enzyme was fully processed in the absence of putrescine, and the rate of this reaction was not stimulated by addition of the polyamine. Residues in the putrescine binding site of the human enzyme were evaluated for their role in processing of the T. cruzi enzyme. The E15A, I80K/S178E, D174A, and E256A mutant T. cruzi enzymes were fully processed. In contrast, mutation of R13 to Leu (the equivalent residue in the human enzyme) abolished processing of the T. cruzi enzyme, demonstrating that Arg at position 13 is a major determinant for proenzyme processing in the parasite enzyme. This amino acid change is a key structural difference that is likely to be a factor in the finding that putrescine has no role in processing of the T. cruzi enzyme. In contrast, the activity of T. cruzi AdoMetDC is stimulated by putrescine. Equilibrium sedimentation experiments demonstrated that putrescine does not alter the oligomeric state of the enzyme. The putrescine binding constant for binding to the T. cruzi enzyme (K(d) = 150 microM) was measured by a fluorescence assay and by ultrafiltration with a radiolabeled ligand. The mutant T. cruzi enzyme D174V no longer binds putrescine, and is not activated by the diamine. In contrast, mutation of E15, S178, E256, and I80 had no effect on putrescine binding. The k(cat)/K(m) values for E15A and E256A mutants were stimulated by putrescine to a smaller extent than the wild-type enzyme (2- and 4-fold vs 11-fold, respectively). These data suggest that the putrescine binding site on the T. cruzi enzyme contains only limited elements (D174) in common with the human enzyme and that the diamine plays different roles in the function of the mammalian and parasite enzymes.     

Kinetic properties and inhibition of Trypanosoma cruzi 3-hydroxy-3-methylglutaryl CoA reductase

A detailed kinetic analysis of the recombinant soluble enzyme 3-hydroxy-3-methylglutaryl CoA reductase (HMGR) from Trypanosoma cruzi has been performed. The enzyme catalyzes the normal anabolic reaction and the reductant is NADPH. It also catalyzes the oxidation of mevalonate but at a lower proportion compared to the anabolic reaction. We report that the catalytically active species of HMGR in solution is the tetrameric form. Fluvastatin inhibited competitively the enzyme while cerivastatin binds by a mechanism which is more accurately described by a biphasic process characteristic of a class of ‘slow, tight-binding’ inhibitors.     

Thermodynamic and kinetic aspects of the hydrolysis of ethyl(R)-2- (benzyloxycarbonylamino)-3-sulfamoylpropionate in the presence of free and immobilized alpha-chymotrypsin

The hydrolysis of ethyl (R)-2-(benzyloxycarbonylamino)-3-sulfamoylpropionate (blocked cysteic acid S-amide) by native and immobilized alpha-chymotrypsin was studied. The experiments were performed using a constant enzyme/substrate ratio of 1:8 and at a temperature of 10-40 degrees C; the immobilized enzyme was bound to a dialdehyde cellulose matrix. A kinetic equation (Eq.10) was found to be applicable which confirms that the mechanism of the enzyme reaction consists of several stages, irrespective of the enzyme state. The temperature dependence of the reaction velocity was investigated and applied using the Arrhenius equation. The constant value thus obtained for the activating energy showed that the active centres retained their character during immobilization. The differences between the velocities of the reaction with immobilized and with native enzyme corresponded to the different number of active centres during the reaction time. Based on these results a kinetic model of the mechanism of the studied reaction is presented which includes an initial balanced stage of the chemosorption type.     

The catalytic potency of β-glucosidase from Pyrococcus furiosus in the direct glucosylation reaction

Enzymes from extremophiles operate at conditions that are different from their ‘normal’ counterparts, and are therefore a useful extension of the enzyme toolbox. In this paper, the direct glucosylation reaction mediated by a hyperthermophilic β-glucosidase from Pyrocuccus furiosus was investigated. Hexanol was successfully coupled to glucose with this enzyme. A preliminary study was conducted to improve the product yield. A maximum product concentration of 12.9 g.l⁻¹ was attainable by increasing the glucose concentration to the maximum solubility of 2000 g.(kg buffer solution)⁻¹ at the reaction temperature. The highest glucose based yield of 2.64% was achieved with a glucose concentration of 900 g.(kg buffer solution)⁻¹ at a reaction temperature of 65°C and a pH of 6.0. Performing the reaction at higher pH and temperature led to lower product concentrations. This was caused by deactivation of the enzyme accompanied by browning of the reaction mixture. A pH of 4.4 did have a negative effect on both the storage and the operational stability of the enzyme.     

The molecular weight and thiol residues of acetyl-coenzyme A synthetase from ox heart mitochondria

1. A constant molecular weight of 57000 was obtained by gel filtration of highly purified acetyl-CoA synthetase over a 1000-fold range of enzyme concentrations. The amino acid analysis is reported. 2. With native enzyme at 20 degrees C the relatively rapid reaction of four thiol residues with p-hydroxymercuribenzoate caused an immediate inhibition reversible by either CoA or mercaptoethanol. Other substrates did not protect against this rapid inhibition. 3. The much slower reaction of the remaining four thiol residues was independent of the concentration of the mercurial, first-order with respect to enzyme, and had a large energy of activation (+136kJ/mol), suggesting that a conformation change in the protein was rate-limiting. This slow phase of the reaction was accompanied by an irreversible inactivation of the enzyme. 4. The effects of substrates on this irreversible inactivation at pH7.0 in 5 mm-MgCl(2) indicated strong binding of ATP and pyrophosphate by the enzyme (concentrations for half-maximal effects, K((1/2)), were <30mum and <10mum respectively) and weaker binding of acetyl-CoA (K((1/2)) about 1 mm), AMP (K((1/2)) about 2mm) and acetate. In the presence of acetate, MgCl(2) and p-hydroxymercuribenzoate, titration of the enzyme with ATP revealed at least two ATP binding sites/mol. 5. The experiments suggest that reaction of the thiol residues with mercurial causes loss of enzymic activity by altering the structure of the enzyme, rather than that the thiol residues play a direct role in the catalysis.     

A definitive mechanism for chorismate mutase

In previous research presentations, we have described the important features of the chorismate --> prephenate reaction using molecular dynamics (MD) and thermodynamic integration studies. This investigation of the reaction in Escherichia coli and water involves QM/MM procedures (SCCDFTB/MM two-dimensional reaction coordinates to identify transition state structures in the water, enzyme, and gas phase followed by B3LYP/6-31+G* single-point computations which allow the determination of activation energies in water and in the E. coli enzyme). Computed activation energies of 11.3 kcal/mol in enzyme and 20.3 kcal/mol in water may be compared to the experimental values of 12.7 and 20.7 kcal/mol, respectively. The transition state structures in the gas phase, water, and enzyme are much the same. The transition states are characteristic of a concerted pericyclic rearrangement. The very small differences in the partial charges of O13 in NAC and TS support only a small preferential (10%) electrostatic stabilization of TS. The free energy of NAC formation in water exceeds that in enzyme by 8.5 kcal/mol, and it is this favored formation of NAC that provides the major kinetic advantage to the enzymatic reaction. These findings compare most favorably with those previous observations of this laboratory employing molecular dynamics and thermodynamic integrations. A definitive mechanism for the chorismate mutase enzymes is provided.     

Optimization of a heterogeneous reaction system for the production of optically active D-amino acids using thermostable D-hydantoinase

A thermostable D-hydantoinase from Bacillus stearothermophilus SD-1 was previously mass-produced by batch cultivation of the recombinant E. coli harboring the gene encoding the enzyme (Lee et al., 1997). In this work, we attempted to optimize the process for the production of N-carbamoyl-D-p-hydroxyphenylglycine, which is readily hydrolyzed to D-p-hydroxyphenylglycine under acidic conditions, from 5-(4-hydroxyphenyl)hydantoin using the mass-produced D-hydantoinase. In an effort to overcome the low solubility of the substrate, enzyme reaction was carried out in a heterogeneous system consisting of a high substrate concentration up to 300 g/L. In this reaction system, most of substrate is present in suspended particles. Optimal temperature and pH were determined to be 45 degrees C and 8.5, respectively, by taking into account the reaction rate and conversion yield. When the free enzyme was employed as a biocatalyst, enzyme loading higher than 300 unit/g-substrate was required to achieve maximum conversion. Use of whole cell enzyme resulted in maximum conversion even at lower enzyme loadings than the free enzyme, showing 96% conversion yield at 300 g/L substrate. The heterogeneous reaction system used in this work might be applied to the enzymatic production of other valuable compounds from a rarely water-soluble substrate.     

Purification and characterization of the maize amyloplast stromal 112-kDa starch phosphorylase

A plastidic 112-kDa starch phosphorylase (SP) has been identified in the amyloplast stromal fraction of maize. This starch phosphorylase was purified 310-fold from maize endosperm and characterized with respect to its enzymological and kinetic properties. The purification procedure included ammonium sulfate fractionation, Sephacryl 300 HR chromatography, affinity starch adsorption, Q-Sepharose, and Mono Q chromatography. The procedure resulted in a nearly homogeneous enzyme preparation as determined by native and SDS-polyacrylamide gel electrophoresis. Anti-SP antibodies recognized the purified 112-kDa SP enzyme and N-terminal amino acid sequence analysis confirmed that the purified enzyme is the amyloplast stromal 112-kDa SP. Analysis of the purified enzyme by Superose 6 gel filtration chromatography indicated that the native enzyme consisted of two identical subunits. The pH optimum for the enzyme was 6.0 in the synthetic direction and 5.5 in the phosphorolytic direction. SP activity was inhibited by thioreactive agents, diethyl pyrocarbonate, phenylglyoxal, and ADP-glucose. The activation energies for the synthetic and phosphorolytic reactions were 11.1 and 16.9 kcal/mol, respectively, and the enzyme was thermally labile above 50 degrees C. Results of kinetic experiments indicated that the enzyme catalyzes its reaction via a sequential Bi Bi mechanism. The Km value for amylopectin was eight-fold lower than that of glycogen. A kinetic analysis indicated that the phosphorolytic reaction was favored over the synthetic reaction when malto-oligosaccharides (4 to 7 units) were used as substrates. The specificity constants (Vmax/Km) of the enzyme measured in either the synthetic or the phosphorolytic directions increased with increasing chain length.     

Determination of half-reaction equilibrium in a ping-pong enzyme mechanism

Substituted enzyme (or ping-pong) mechanisms usually involve enzymes that exist in two forms that alternate during the catalytic reaction. A method is described here for determining the position of the equilibrium of a half reaction in a ping-pong enzyme mechanism that is based on the kinetics of the burst reaction which occurs upon addition of reactants that recycle the enzyme from one form to another. The theoretical basis for the analysis is developed, and the method is applied to the half reaction of the aldimine form of aspartate transaminase with difluoro-oxaloacetate. Special issue dedicated to Herman Bachelard     

Steady-state kinetic analysis for the reaction of ammonium and alkylammonium ions with methylamine dehydrogenase from bacterium W3A1

The steady-state kinetic mechanism for the reaction of n-alkylamines and phenazine ethosulfate (PES) or phenazine methosulfate (PMS) with methylamine dehydrogenase from bacterium W3A1 is found to be of the ping-pong type. This conclusion is based on the observations that 1/v versus 1/[methylamine] or 1/[butylamine] plots, at various constant concentrations of an oxidizing substrate, and 1/v versus 1/[PES] or 1/[PMS] plots, at various constant concentrations of a reducing substrate, are parallel. Additionally, the values of kcat/Km for four n-alkylamines are identical when PES is the oxidizing substrate, as were the kcat/Km values for four reoxidizing substrates when methylamine was the reducing substrate. Last, analysis of steady-state kinetic data obtained when methylamine and propylamine are presented to the enzyme simultaneously and PES and PMS are used simultaneously also supports the involvement of a ping-pong mechanism. The enzymic reaction with either methylamine or PES is dependent on the ionic strength, and the data indicate that each interacts with an anionic site on methylamine dehydrogenase. The presence of ammonium ion at low concentration activates the enzyme, but at high concentration this ion is a competitive inhibitor in the reaction involving methylamine and the enzyme. A complete steady-state mechanism describing these ammonia effects is presented and is discussed in light of the nature of the pyrroloquinoline quinone cofactor covalently bound to the enzyme.     

Production of platelet thromboxane A2 inactivates purified human platelet thromboxane synthase.

Human platelet thromboxane synthase was partially purified by DEAE-cellulose, Affi-Gel Blue, and Sephacryl S-300 chromatography to a specific activity of 259 nmol of thromboxane B2/min per mg. Thromboxane synthase retained 75-90% of its enzymic activity when bound to phenyl-Sepharose. The immobilized enzyme was inactivated at pH 3.0 and inhibited by 1-benzylimidazole and U-63,557A. The ability of the enzyme to produce thromboxane A2 from prostaglandin H2 was dramatically reduced by multiple additions of prostaglandin H2. Our data suggest that the production of thromboxane A2 by the enzyme is self-limiting and that the enzyme is inactivated during the reaction.