Kinetics of Pyruvate Decarboxylase Deactivation by Benzaldehyde

Based on experimental data, a kinetic model for the deactivation of partially purified pyruvate decarboxylase (PDC) by benzaldehyde (0–200 mM) in MOPS buffer (2.5 M) has been developed. An initial lag period prior to deactivation was found to occur. With first order dependencies of PDC deactivation on exposure time and on benzaldehyde concentration, a reaction time deactivation constant of 2.64×10^?3 h^?1 and a benzaldehyde deactivation coefficient of 1.98×10^?4 mM^?1 h^?1 were determined for benzaldehyde concentrations up to 200 mM. The PDC deactivation kinetic equations established in this study are an essential component in an overall model being developed to describe the enzymatic biotransformation of benzaldehyde and pyruvate to produce the pharmaceutical intermediate (R)-phenylacetylcarbinol (R-PAC).     

A kinetic model for the deactivation of pyruvate decarboxylase (PDC) by benzaldehyde

To provide further understanding of the biotransformation of benzaldehyde to L-phenylacetyl carbinol (L-PAC), an intermediate in L-ephedrine production, a kinetic model has been developed for the deactivation of pyruvate decarboxylase (PDC) by benzaldehyde. The model confirms that deactivation is first order with respect to benzaldehyde concentration and exhibits a square root dependency on time. The model covers the range of benzaldehyde concentrations 100–300 mM, as it has been shown previously that 200 mM benzaldehyde can produce L-PAC concentrations up to 190 mM (28.6 g/L) using partially purified PDC from Candida utilis.     

Enzymatic synthesis of new aromatic and aliphatic esters of flavonoids using Candida antarctica lipase as biocatalyst

Enzymatic acylation of rutin and esculin with aromatic, aliphatic and aryl-aliphatic acids using Candida antarctica lipase in tert amyl alcohol as solvent was investigated under low water content. Whatever the acyl donor used, the conversion yields and initial rates for esculin were higher than for rutin. For a given flavonoid, the performance of these reactions depended on the acyl donor structures. For aliphatic acids, conversion yields and initial rates of both flavonoids were respectively in the ranges of 68-90% and of 9.5×10^-2-72×10^-2 mmol l^-1 h^-1. For aromatic acids, the reaction occurred only with the aryl subgroup (cinnamic, hydrocinnamic, 3,4-dihydroxyhydrocinnamic and 4-hydroxyphenyl acetic acids) and was drastically influenced by the presence of side chain and substitution patterns of the aromatic ring. Except for hydrocinnamic acid (75%, 23.4×10^-2 mmol l^-1 h^-1), with these acids the conversion yields and initial rates were lower and in the range of 10-45% and of 0.7×10^-2 to 12.1×10^-2 mmol l^-1 h^-1. Unsaturation of the side chain of the hydrocinnamic acid decreased the esculin conversion rate from 75 to 13% and initial rate from 23.4 to 1.76×10^-2 mmol l^-1 h^-1. The presence of hydroxyl or nitro-groups on the aromatic ring of the aryl aliphatic acid also reduced conversion yields and initial rates. Even without a spacer, the non-phenolic ring acid (quinic acid) was reactive and lead to conversion yields of about 20 and 23% respectively for rutin and esculin.     

Studies on the continuous production of (R)-(−)-phenylacetylcarbinol in an enzyme-membrane reactor

The optimization of a continuous enzymatic reaction yielding (R)-(−)-phenylacetylcarbinol ((R)-PAC), a key intermediate of the (1R,2S)-(−)-ephedrine synthesis, is presented. We compare the suitability of different mutants of the pyruvate decarboxylase (PDC) from Zymomonas mobilis with respect to their application in biotransformation using pyruvate or acetaldehyde and benzaldehyde as substrates, respectively. Starting from 90 mM pyruvate and 30 mM benzaldehyde, (R)-PAC was obtained with a space time yield of 27.4 g/(L·day) using purified PDCW392I in an enzyme-membrane reactor. Due to the high stability of the mutant enzymes PDCW392I and PDCW392M towards acetaldehyde, a continuous procedure using acetaldehyde instead of pyruvate was developed. The kinetic results of the enzymatic synthesis starting from acetaldehyde and benzaldehyde demonstrate that the carboligation to (R)-PAC is most efficiently performed using a continuous reaction system and feeding both aldehydes in equimolar concentration. Starting from an inlet concentration of 50 mM of both aldehydes, (R)-PAC was obtained with a space-time yield of 81 g/(L·day) using the mutant enzyme PDCW392M. The new reaction strategy allows the enzymatic synthesis of (R)-PAC from cheap substrates free of unwanted by-products with potent mutants of PDC from Z. mobilis in an aqueous reaction system.     

Improved enzymatic two-phase biotransformation for (R)-phenylacetylcarbinol: Effect of dipropylene glycol and modes of pH control

An octanol/aqueous two-phase process for the enzymatic production of (R)-phenylacetylcarbinol (PAC) has been investigated further with regard to optimal pH control and replacement of 2.5 M MOPS buffer by a low cost solute. The specific rate of PAC production in the 2.5 M MOPS system controlled at pH 7 was 0.60 mg U^-1 h^-1 (reaction completed at 34 h), a 1.6 times improvement over the same 2.5 M MOPS system without pH control (0.39 mg U^-1 h^-1 at 49 h). An improved stability of PDC was evident at the end of biotransformation for the pH-controlled system with 84% residual carboligase activity, while 23% of enzyme activity remained in the absence of pH control. Lowering the MOPS concentration to 20 mM resulted in a lower benzaldehyde concentration in the aqueous phase with a major increase in the formation of by-product acetoin and three times decreased PAC production (0.21 mg U^-1 h^-1). Biotransformation with 20 mM MOPS and 2.5 M DPG as inexpensive replacement of high MOPS concentrations provided similar aqueous phase benzaldehyde concentrations compared to 2.5 M MOPS and resulted in a comparable PAC concentration (92.1 g L^-1 in the total reaction volume in 47 h) with modest formation of acetoin.     

Kinetic Behavior of Native Alkaline Phosphatase from Human Placenta

The kinetic behavior of human placental alkaline phosphatase, which catalyses the hydrolysis of p-nitrophenyl and of o-carboxyphenyl phosphates, was studied by means of graphical and non-linear regression statistical fitting analysis of data of rate versus substrate concentration. Non linear Lineweaver-Burk and Eadie-Hofstee plots and rational functions of degree 2:2 (F-test assessing the goodness of fit) show non-Michaelian kinetic behavior. In the same way, the behavior of the enzyme was also non-Michaelian in the simultaneous presence of these two substrates.

Norlaudanosoline is a key intermediate in the biosynthesis of the benzylisoquinoline alkaloids providing the benzyl-isoquinoline portion of the morphinan skeleton. This study examines a coupled reaction system for the production of norlaudanosoline from dopamine. In this coupled system, dopamine is enzymatically converted by monoamine oxidase (MAO) to 3,4-dihydroxyphenylacetaldehyde (dopaldehyde). In the presence of dopamine, this aldehyde undergoes a spontaneous Pictet-Spengler condensation to form norlaudanosoline. Three potential sources of MAO were investigated: a fungal source (Aspergillus niger), a bacterial source (Sarcina lutea) and a commercial source isolated from bovine plasma. Kinetic studies with dopamine as the substrate gave Michaelis constants (K_m) of 1.81 × 10^-5 M, 6.94 × 10^-3, and 1.61 × 10^-3 M for A. niger, S. lutea and bovine plasma oxidase, respectively. The reaction system is complicated because of the effect of the condensation reaction, so a more rigorous model was developed to account for this effect. The model was suitable for showing the effect of dopamine concentration on norlaudanosoline production alghough there were some model inadequacies. Using the model a forward rate constant for the Pictet-Spengler condensation was determined to be 6.8 × 10^-2 M^-1 s^-1 and the reverse reaction appears to be negligible. Overall conversion was 14% which is 20 times that achieved in an in situ reaction system using whole cells of Aspergillus niger.     

Role of pyruvate in enhancing pyruvate decarboxylase stability towards benzaldehyde

Biotransformation of benzaldehyde and pyruvate into (R)-phenylacetylcarbinol (PAC) catalysed by Candida utilis pyruvate decarboxylase (PDC) at low buffer concentration (20 mM MOPS) was enhanced by maintenance of neutral pH through acetic acid addition. PDC was very stable in this buffer (half-life 138 h at 6 degrees C), however a benzaldehyde emulsion (400 mM) caused rapid deactivation. The inclusion of 2M glycerol did not protect PDC from inactivation by benzaldehyde but initial rates were increased by 50% and the final PAC level was enhanced from 40 to 51 g l(-1). Low levels of by-products acetaldehyde (0.1-0.15 g l(-1)) and acetoin (1.1-1.3 g l(-1)) were formed in both the presence and absence of 2 M glycerol. Interestingly PDC was more stable towards benzaldehyde when pyruvate was present: no activity was lost during the first hour of biotransformation (2 M glycerol, benzaldehyde concentration decreased from 400 to 345 mM, pyruvate from 480 to 420 mM) but PDC was completely inactivated in less than 30 min when exposed to the same concentrations of benzaldehyde in the absence of pyruvate. Thus the enzyme in catalytic action was more stable than the resting enzyme.     

Production of L-phenylacetylcarbinol (L-PAC) from benzaldehyde using partially purified pyruvate decarboxylase (PDC)

Biotransformation of benzaldehyde to L-phenylacetylcarbinol (L-PAC) as a key intermediate for L-ephedrine synthesis has been evaluated using pyruvate decarboxylase (PDC) partially purified from Candida utilis. PDC activity was enhanced by controlled fermentative metabolism and pulse feeding of glucose prior to the enzyme purification. With partially purified PDC, several enzymatic reactions occurred simultaneously and gave rise to by-products (acetaldehyde and acetoin) as well as L-PAC production. Optimal reaction conditions were determined for temperature, pH, addition of ethanol, PDC activity, benzaldehyde, and pyruvate:benzaldehyde ratio to maximize L-PAC, and minimize by-products. The highest L-PAC concentration of 28.6 g/L (190.6 mM) was achieved at 7 U/mL PDC activity and 200 mM benzaldehyde with 2.0 molar ratio of pyruvate to benzaldehyde in 40 mM potassium phosphate buffer (pH 7.0) containing 2.0 M ethanol at 4 degrees C. (c) 1996 John Wiley & Sons, Inc.     

Kinetic analysis and modelling of enzymatic (R)-phenylacetylcarbinol batch biotransformation process

Initial rate and biotransformation studies were applied to refine and validate a mathematical model for enzymatic (R)-phenylacetylcarbinol (PAC) production from pyruvate and benzaldehyde using Candida utilis pyruvate decarboxylase (PDC). The rate of PAC formation was directly proportional to the enzyme activity level up to 5.0 U ml-1 carboligase. Michaelis-Menten kinetics were determined for the effect of pyruvate concentration on the reaction rate. The effect of benzaldehyde followed the sigmoidal shape of the Monod-Wyman-Changeux (MWC) model. The biotransformation model, which also included a term for PDC inactivation by benzaldehyde, was used to determine the overall rate constants for the formation of PAC, acetaldehyde, and acetoin. These values were determined from data for three batch biotransformations performed over a range of initial concentrations (viz. 50-150 mM benzaldehyde, 60-180 mM pyruvate, 1.1-3.4 U ml-1 enzyme activity). The finalized model was then used to predict a batch biotransformation profile at 120/100 mM initial pyruvate/benzaldehyde (initial enzyme activity 3.0 U ml-1). The simulated kinetics gave acceptable fitting (R2 = 0.9963) to the time courses of these latter experimental data for substrates pyruvate and benzaldehyde, product PAC, by-products acetaldehyde and acetoin, as well as enzyme activity level.     

Biphasic kinetics of Zn removal from Zn metallothionein by nitrilotriacetate are associated with differential reactivity of the two metal clusters

We investigated the kinetics of nitrilotriacetate (NTA) extraction of Zn²⁺ from Zn₇-metallothionein (MT) and a metal-hybrid derivative, Zn₄Ag₆MT, in which the Zn²⁺ and Ag⁺ ions occupy sites in the C-terminal and N-terminal β domains of the protein, respectively. Biphasic kinetics were observed for Zn₇MT under pseudo-first-order conditions. Rate constants were (5.2±0.6)×10⁻³ and (1.0±0.3)×10⁻⁴s⁻¹ in 20 mM phosphate, 100 mM KF, pH 7.5 at 23C. In contrast, Zn₄Ag₆MT showed a single kinetic step with a rate constant of (2.9±0.4)×10⁻³s⁻¹. These results indicate that the biphasic reactivity of Zn₇MT stems from differential susceptibility of the metal in the two metal–thiolate clusters to removal by competing ligands, with Zn²⁺ in the more stable -domain cluster reacting faster than that in the less stable β-domain cluster. Such behavior suggests that the structures of the two domains of mammalian MT may have evolved to assure that Cu binding does not compromise the structural characteristics that allow Zn to be rapidly transferred from MT to essential cellular ligands.     

Aerobic biological treatment of black table olive washing wastewaters: effect of an ozonation stage

The present work is a study of oxidative degradation of the organic matter present in the washing waters from the black table olive industry. Pollutant organic matter reduction was studied by an aerobic biological process and by the combination of two successive steps: ozonation pretreatment followed by aerobic biological degradation. In the single aerobic biological process, the evolution of biomass and organic matter contents was followed during each experiment. Contaminant removal was followed by means of global parameters directly related to the concentration of organic compounds in those effluents: chemical oxygen demand (COD) and total phenolic content (TP). A kinetic study was performed using the Contois model, which applied to the experimental data, provides the specific kinetic parameters of this model: 4.81×10⁻² h⁻¹ for the kinetic substrate removal rate constant, 0.279 g VSS g COD⁻¹ for the cellular yield coefficient and 1.92×10⁻² h⁻¹ for the kinetic constant for endogenous metabolism. In the combined process, an ozonation pretreatment is conducted with experiments where an important reduction in the phenolic compounds is achieved. The kinetic parameters of the following aerobic degradation stage are also evaluated, being 5.42×10⁻² h⁻¹ for the kinetic substrate removal rate constant, 0.280 g VSS g COD⁻¹ for the cellular yield coefficient and 9.1×10⁻³ h⁻¹ for the kinetic constant for the endogenous metabolism.     

Binding Specificity and Affinity of Acriflavine for Nucleic Acids

A set of conditions was developed for the specific binding of acriflavine to the DNA of intact squamous cells. This was achieved through a series of studies into the relative affinities for dye between DNA and various biopolymers by an agar gel diffusion technique. Specificity was ascertained by DNase and RNase treatment of the cells. The final conditions, based on an estimated DNA-to-dye ratio of 4:1, required a constant cell count of 100,000 and dye at a concentration of 0.0025 μg per ml in 10 ml of phosphate buffer, pH 6.0-7.4. These quantities were dictated by the sensitivity limitations of the analytical apparatus. To make use of standard fluorometric instrumentation, the whole cell population method for determining average values was followed. Free dye was analyzed after cell samples were stained, and the difference between this value and that of an aliquot of working dye was taken as the amount of bound dye. To ensure cell-free residues of dye, cells were removed by centrifugation through Teflon membrane filters. The average amount of dye which was bound to the DNA of normal squamous cells was 1.6 × 10^-7 μg (0.7 × 10^-15 mole) per cell, and the amount bound to HeLa cells was 2.3 × 10^-7 μg (1 × 10^-15 mole). These values were highly replicable, making it possible to use them as an expression of the DNA content of the cells. The mildness of the staining conditions, and the preservation of cellular integrity in this technique may permit quantitative measurements of the DNA content of living cells.     

Enzymatic (R)-phenylacetylcarbinol production in benzaldehyde emulsions

(R)-Phenylacetylcarbinol [(R)-PAC)] is the chiral precursor for the production of the pharmaceuticals ephedrine and pseudoephedrine. Reaction conditions were improved to achieve increased (R)-PAC levels in a simple batch biotransformation of benzaldehyde emulsions and pyruvate, using partially purified pyruvate decarboxylase (PDC) from the filamentous fungus Rhizopus javanicus NRRL 13161 as the catalyst. Lowering the temperature from 23 degrees C to 6 degrees C decreased initial rates but increased final (R)-PAC concentrations. Addition of ethanol, which increases benzaldehyde solubility, was not beneficial for (R)-PAC production. It was established that proton uptake during biotransformation increases the pH above 7 thereby limiting (R)-PAC production. For small-scale studies, biotransformations were buffered with 2-2.5 M MOPS (initial pH 6.5). High concentrations of MOPS as well as some alcohols and KCl stabilised PDC. A balance between PDC and substrate concentrations was determined with regards to ( R)-PAC production and yields on enzyme and substrates. R. javanicus PDC (7.4 U/ml) produced 50.6 g/l (337 mM) ( R)-PAC in 29 h at 6 degrees C with initial 400 mM benzaldehyde and 600 mM pyruvate. Molar yields on consumed benzaldehyde and pyruvate were 97% and 59%, respectively, with 17% pyruvate degraded and 24% converted into acetaldehyde and acetoin; 43% PDC activity remained, indicating reasonable enzyme stability at high substrate and product concentrations.     

Microencapsulated Chromatophores for the Production of ATP

Chromatophores, organelles for photophosphorylation in non-sulfur purple photosynthetic bacteria, were microencapsulated and utilized in ATP production. The microcapsules were formed by photocrosslinking with trimethylolpropane triacrylate (TMPTA). In batch experiments chromatophores microencapsulated in TMPTA capsules were repeatedly used in ATP production for more than 5 times. Continuous ATP production was then undertaken. ATP was produced at a production rate of 14 μmol h^-1 L^-1 over 200 hrs. The yield (from ADP to ATP) was 35%. The total amount of ATP produced was 0.7 mM (μM Bchl)^-1. Therefore, this microencapsulation method was found to be suitable for the continuous ATP production using chromatophores.     

A study in UF-membrane reactor on activity and stability of nitrile hydratase from Microbacterium imperiale CBS 498-74 resting cells for propionamide production

The bioconversion of propionitrile to propionamide was catalysed by nitrile hydratase (NHase) using resting cells of Microbacterium imperiale CBS 498-74 (formerly, Brevibacterium imperiale). This microorganism, cultivated in a shake flask, at 28 °C, presented a specific NHase activity of 34.4 U mg_DCW⁻¹ (dry cell weight). The kinetic parameters, K_m and V_max, tested in 50 mM sodium phosphate buffer, pH 7.0, in the propionitrile bioconversion was evaluated in batch reactor at 10 °C and resulted 21.6 mM and 11.04 μmol min⁻¹ mg_DCW⁻¹, respectively. The measured apparent activation energy, 25.54 kJ mol⁻¹, indicated a partial control by mass transport, more likely through the cell wall.

UF-membrane reactors were used for kinetic characterisation of the NHase catalysed reaction. The time dependence of enzyme deactivation on reaction temperature (from 5 to 25 °C), on substrate concentrations (from 100 to 800 mM), and on resting cell loading (from 1.5 to 200 μg  ml⁻¹) indicated: lower diffusional control (E_a=37.73 kJ mol⁻¹); and NHase irreversible damage caused by high substrate concentration. Finally, it is noteworthy that in an integral reactor continuously operating for 30 h, at 10 °C, 100% conversion of propionitrile (200 mM) was attained using 200 μg  ml⁻¹ of resting cells, with a maximum volumetric productivity of 0.5 g l⁻¹ h⁻¹.     

虎斑乌贼的胚胎耗氧率

为了探究虎斑乌贼胚胎不同发育时期的耗氧率变化和几种生态因子对胚胎发育过程耗氧率的影响,试验采用封闭静水装置,对不同发育时期(12期)的耗氧率进行测定,并研究不同盐度(21、24、27、30、33)、温度(18、21、24、27、30 ℃)和pH(7.0、7.5、8.0、8.5、9.0)对胚胎4个主要发育时期(受精卵期、原肠胚期、器官形成期和内骨骼形成期)耗氧率的影响.结果表明: 胚胎各个发育时期耗氧率不同,随着发育的进程而增大,受精卵期为0.082 mg·(100 eggs)^-1·h^-1,而到原肠胚期的耗氧率显著升高,为0.279 mg·(100 eggs)^-1·h^-1,到孵化期时,耗氧率达到1.367 mg·(100 eggs)^-1·h^-1;盐度对器官形成期和内骨骼形成期的耗氧率均有显著影响(P<0.05),对受精卵期和原肠胚期影响不显著(P>0.05),当盐度为30时,4个发育时期耗氧率均达到最大值,分别为0.082、0.200、0.768和1.301 mg·(100 eggs)^-1·h^-1;温度对原肠胚期、器官形成期和内骨骼形成期的耗氧率有显著影响(P<0.05),对受精卵期无显著性影响(P>0.05),在27 ℃时,胚胎4个发育时期均达到最大值,分别为0.082、0.286、0.806和1.338 mg·(100 eggs)^-1·h^-1;而pH对4个发育时期的耗氧率均无显著性影响(P>0.05),受精卵期在pH 8.0时达到最大值,为0.116 mg·(100 eggs)^-1·h^-1,原肠胚期、器官形成期、内骨骼形成期在pH 8.5时达到最大值,分别为0.281 、0.799和1.130 mg·(100 eggs)^-1·h^-1.     

Enzymatic production of (R)-phenylacetylcarbinol by pyruvate decarboxylase from <Emphasis Type="Italic">Zymomonas mobilis</Emphasis>

Herein, we synthesized (R)-phenylacetylcarbinol (PAC), a pharmaceutical intermediate for ephedrine and pseudoephedrine, from benzaldehyde and pyruvate using a recombinant pyruvate decarboxylase (PDC) from Zymomonas mobilis. A whole cell reaction consisting of 30 mM benzaldehyde, 60 mM pyruvate, and a mutant PDC enzyme (PDC W329M; 1.6 mg DCW/mL) produced 12.4 mM (R)-PAC and less than 0.3 mM benzyl alchohol in 15 h at 20°C, outperforming the crude enzyme extract reaction (1.2 mM (R)-PAC) and minimizing formation of benzyl alchohol, the major by-product of S. cerevisiae whole cell reaction. These observations suggested that recombinant E. coli whole cell reactions are more efficient than crude enzyme extract or yeast-based reactions. We also demonstrated that the E. coli whole cell reaction performed effectively without expensive thiamin diphosphate cofactor. Finally, whole cell reaction (8 mg DCW/mL) was carried out with 200 mM benzaldehyde, 400 mM pyruvate in 10 mL of 500 mM phosphate buffer (pH 6.5), and 72 mM (R)-PAC was produced with 36% conversion for 15 h. © KSBB     

虎斑乌贼的胚胎耗氧率

为了探究虎斑乌贼胚胎不同发育时期的耗氧率变化和几种生态因子对胚胎发育过程耗氧率的影响,试验采用封闭静水装置,对不同发育时期(12期)的耗氧率进行测定,并研究不同盐度(21、24、27、30、33)、温度(18、21、24、27、30 ℃)和pH(7.0、7.5、8.0、8.5、9.0)对胚胎4个主要发育时期(受精卵期、原肠胚期、器官形成期和内骨骼形成期)耗氧率的影响.结果表明: 胚胎各个发育时期耗氧率不同,随着发育的进程而增大,受精卵期为0.082 mg·(100 eggs)^-1·h^-1,而到原肠胚期的耗氧率显著升高,为0.279 mg·(100 eggs)^-1·h^-1,到孵化期时,耗氧率达到1.367 mg·(100 eggs)^-1·h^-1;盐度对器官形成期和内骨骼形成期的耗氧率均有显著影响(P<0.05),对受精卵期和原肠胚期影响不显著(P>0.05),当盐度为30时,4个发育时期耗氧率均达到最大值,分别为0.082、0.200、0.768和1.301 mg·(100 eggs)^-1·h^-1;温度对原肠胚期、器官形成期和内骨骼形成期的耗氧率有显著影响(P<0.05),对受精卵期无显著性影响(P>0.05),在27 ℃时,胚胎4个发育时期均达到最大值,分别为0.082、0.286、0.806和1.338 mg·(100 eggs)^-1·h^-1;而pH对4个发育时期的耗氧率均无显著性影响(P>0.05),受精卵期在pH 8.0时达到最大值,为0.116 mg·(100 eggs)^-1·h^-1,原肠胚期、器官形成期、内骨骼形成期在pH 8.5时达到最大值,分别为0.281 、0.799和1.130 mg·(100 eggs)^-1·h^-1.     

Kinetic evaluation of biotransformation of benzaldehyde to L-phenylacetylcarbinol by immobilized pyruvate decarboxylase from Candida utilis

Biotransformation of benzaldehyde to L-phenylacetylcarbinol (L-PAC) as a key intermediate for L-ephedrine has been evaluated using immobilized pyruvate decarboxylase (PDC) from Candida utilis. PDC immobilized in spherical polyacrylamide beads was found to have a longer half-life compared with free enzyme. In a batch process, the immobilized PDC generally produced lower L-PAC than free enzyme at the same concentrations of substrates due to increased by-products acetaldehyde and acetoin and reduced benzaldehyde uptake. With immobilized PDC, L-PAC formation occurred at higher benzaldehyde concentrations (up to 300 mM) with the highest L-PAC concentration being 181 mM (27.1 g/L). For a continuous process, when 50 mM benzaldehyde and 100 mM sodium pyruvate were fed into a packed-bed reactor at 4 degrees C and pH 6.5, a productivity of 3.7 mM/h (0.56 g/L . h) L-PAC was obtained at an average concentration of 30 mM (4.5 g/L). The half-life of immobilized PDC reactor was 32 days. (c) 1996 John Wiley & Sons, Inc.     

Epr Spectroscopic Studies of Detection of a Carbon-Centered Free Radical During Acetylcholine-Induced and Endothelium-Dependent Relaxation of Guinea Pig Pulmonary Artery

Vascular smooth muscle relaxation by several vasodilators, including acetylcholine (Ach) and ATP, depends on the presence of intact endothelium. Ach is thought to activate muscarinic receptors on endothelium to release an endothelium-derived relaxing factor (EDRF) which brings about relaxation of smooth muscle. In order to assess the role of free radicals in the endothelium-dependent relaxation of blood vessel, we have studied the effect of a spin-trapping agent, phenyl t-butyl nitrone (PBN). on Ach-, ATP-, and sodium nitroprusside-induced relaxation of guinea pig pulmonary artery. Arterial strips were mounted in a 5-ml organ bath containing Krebs solution equilibrated with 95% O₂ and 5% CO₂ at 37°C. After increasing vascular tone by a synthetic prostaglandin endoperoxide analog (50 ng/ml), the strips relaxed dose-dependently in response to Ach (5 × 10^-8M), ATP (1.5 × 10^-6M) or sodium nitroprusside (6 × 10^-9 M). Removal of the endothelium abolished the relaxation by Ach or ATP, but did not affect the relaxation by sodium nitroprusside. PBN inhibited Ach-induced relaxation of pulmonary artery dose-dependently, but had no effect on relaxations by ATP or sodium nitroprusside. PBN did not block radioligand binding to muscarinic cholinergic membrane receptors on both chick embryonic heart and guinea pig pulmonary artery endothelial cells indicating that it does not block the muscarinic receptors. Spin trapping in combination with electron paramagnetic resonance (EPR) spectral analysis revealed a carbon-centered radical with hyperfine splitting constants of a_N = 16.0 G and a_β^H: = 3.85 G in the lipid extracts of pulmonary artery (0.2-0.4g) incubated with PBN (14mM) and Ach (3 × 10^-6M) for 20min. No signal was detected when endothelium was removed. Our data suggest that the endothelium-dependent relaxation of pulmonary artery by Ach is associated with the generation of a free-radical and can be prevented by a spin-trapping agent. ATP, however, relaxes the arterial smooth muscle by a different mechanism.