Enzymatic epoxidation: synthesis of 7,8-epoxy-1-octene, 1,2-7,8-diepoxyoctane, and 1,2-Epoxyoctane by Pseudomonas oleovorans.

The kinetics of the enzymatic formation of 7,8-epoxy-1-octene, 1,2-7,8-diepoxyoctane, and 1,2-epoxyoctane by growing and resting cell suspensions of Pseudomonas oleovorans are described. Formation of 1,2-epoxyoctane occurs concurrently with exponential growth on 1-octene, providing that 1-octene is in excess. Conversion of 1,7-octadiene to 7,8-epoxy-1-octene by cells growing on octane lags behind exponential growth and continues into the stationary phase, terminating upon cell death. Formation of 1,2-7,8-diepoxyoctane does not begin until the cells are well into the stationary phase and also continues until cell death. Results with growing and resting cell suspensions suggest that the various substrates compete for the same enzyme system; that viable cells are essential for substrate transport and epoxidation by whole cells; and that whole cells may concentrate and sequester the epoxides, rendering them unrecoverable by our current methods.     

Synthesis of 1,2-Epoxyoctane by Pseudomonas oleovorans During Growth in a Two-Phase System Containing High Concentrations of 1-Octene

We have optimized and compared the synthesis of 1,2-epoxyoctane from 1-octene by resting and by growing cells of Pseudomonas oleovorans. The net production of 1,2-epoxyoctane by resting cells never exceeded 0.6 mg/ml of suspension. In contrast, P. oleovorans produced much more epoxide when it was grown on high levels of 1-octene. To raise the total production of epoxide, the octene layer was repeatedly transferred to fresh, growing cultures of P. oleovorans. By using this approach, a maximum of 28 mg of epoxide was synthesized per ml of total culture, resulting in the accumulation of ca. 75 mg of epoxide per ml in the octene phase.     

Pseudomonas oleovorans as a tool in bioconversions of hydrocarbons: growth,morphology and conversion characteristics in different two-phase systems

The bioconversion of hydrocarbons by Pseudomonas oleovorans has been studied in two-phase systems. In these systems, the hydrocarbon substrate is present in sufficient amounts to form the bulk apolar phase. High cell densities (up to 20 mg dry mass per ml water phase) are reached when the apolar phase consists of n-octane, 1-octene or 1-decene. There is considerable cell damage after incubation for 50–70 h. Loss of cell viability and membrane damage as observed by freeze-fracture electron microscopy correlate with a loss of hydrocarbon oxidation, measured as the conversion of 1-octene to 1,2-epoxyoctane. The final yield of oxidized hydrocarbon in the apolar substrate phase can be increased substantially by replacing the damaged cells with freshly grown cells. Yields up to 150 mg 1,2-epoxyoctane per ml 1-octene and up to 20–25 mg 1,2-epoxyoctane per ml culture were obtained with four cycles of the cell renewal procedure. Several other substrates in addition to octene were tested in the optimized two-phase system. Of these, 1-decene was converted into (R)-1,2-epoxydecane with an optical purity of 60%, while allylbenzene was converted into chiral 1,2-epoxy-3-phenylpropane. Some of the future applications of the conversion products are discussed.     

Pseudomonas oleovorans Hydroxylation-Epoxidation System: Additional Strain Improvements

The isolation and characterization of a strain of Pseudomonas oleovorans which epoxidates 1-octene at a rate nine times that of the original strain are described. In addition, it has been confirmed that a greater amount of the mono-epoxide product is formed from 1,7-octadiene than is formed from 1-octene. 1,7-octadiene will not support growth, but will induce the enzymes required for epoxidation.     

Immobilization of microbial cells in a mixed matrix of silicone polymer and calcium alginate gel: epoxidation of 1-octene by Nocardia corallina B-276 in organic media.

Immobilization of Nocardia corallina B-276 was examined for production of 1,2-epoxyoctane from 1-octene in the presence of n-hexadecane as the organic solvent. Hydrophobic silicone polymer was the most suitable material for entrapment of the cells. Coentrapment of aqueous reaction medium into the silicone polymer matrix improved the epoxide productivity. It was also effective to immobilize the cells in a mixed matrix composed of silicone polymer and calcium alginate gel involving the reaction medium. In the organic monophase, the amount of epoxide accumulated with the cells immobilized in an almost equivolumetric composite of both materials was 2 and 7 times the amounts in the silicone and alginate single matrices, respectively, and it became larger than with the free cells in the aqueous-organic two-liquid phase after a longer period of batch operation. The use of such an optimized composite matrix enabled us to perform a relatively simple operation of the continuous three-phase bioreactor.     

Epoxidation of 1,7-octadiene by Pseudomonas oleovorans: fermentation in the presence of cyclohexane.

A very efficient conversion of 1,7-octadiene to 7,8-epoxy-1-octene and 1,2-7,8-diepoxyoctane was achieved by incorporating a high concentration of cyclohexane into the conventional fermentation medium. In the presence of cyclohexane, a 90-ml% conversion of substrate to product was accomplished within 72 h, compared with an 18,5-mol% conversion in the absence of cyclohexane. Furthermore, the products were simultaneously separated and concentrated in the organic phase.     

Silicone-immobilized biocatalysts effective for bioconversions in nonaqueous media.

A hydrophobic silicone polymer could be effectively applied to immobilization of two kinds of biocatalysts operating in organic media. Horse liver alcohol dehydrogenase, which was solubilized in a small amount of water, or deposited on water-filled hydrophilic particles, was immobilized in this material. This configuration of the preparation involving finely dispersed aqueous phase permitted a simple packed-bed operation for the enzymatic oxidation of alcohol and reduction of aldehyde with a coupled-substrate NAD(H) recycling in n-hexane. Another example was the immobilization of Nocardia corallina which catalysed epoxidation of liquid alkenes such as 1-tetradecene, 1-octene, and styrene in the presence of n-hexadecane. In order to adjust the hydrophobicity-hydrophilicity balance of the support, it was effective to immobilize the cells in a mixed matrix composed of silicone polymer and Ca-alginate gel. The optimum composition of the mixed matrix, which yielded the highest productivity of epoxide, was 80-90% silicone + 20-10% alginate for the production of 1,2-epoxytetradecane, 40-50% silicone + 60-50% alginate for 1,2-epoxyoctane, and almost 0% silicone + 100% alginate for styrene oxide. This significant change of the optimum composition was primarily associated with the degree of substrate inhibition.     

Epoxide hydrolase activity of Chryseomonas luteola for the asymmetric hydrolysis of aliphatic mono-substituted epoxides

Asymmetric hydrolysis of a homologous range of straight chain 1,2-epoxyalkanes was achieved using whole cells of Chryseomonas luteola. Depending on the chain length, hydrolyses of the racemic epoxides afforded optically active epoxides and diols with varying degrees of optical purity. In the case of 1,2-epoxyoctane, the enantiomeric excess of the remaining (S)-epoxide and formed (R)-diol was excellent (ees > 98% and eep = 86%). This is the first report of a bacterial epoxide hydrolase with such unusual enantioselectivity for terminal mono-substituted epoxides bearing no directing group on the chiral C-2 carbon. Benzyl glycidyl ether and the 2,2-disubstituted epoxide, 2-methyl-1,2-epoxyheptane, were hydrolysed, but no enantioselectivity was observed. © Rapid Science Ltd. 1998     

Glutathione depletion and cytotoxicity by naphthalene 1,2-oxide in isolated hepatocytes

The ability of naphthalene 1,2-oxide to diffuse across intact cellular membranes, the subsequent biotransformation of this epoxide and its potential to produce losses in cellular viability have been examined in incubations of isolated hepatocytes. Addition of 1R,2S- or 1S,2R-naphthalene oxide enantiomers (15, 30 and 60 microM) to isolated hepatocytes resulted in a rapid depletion of intracellular glutathione. Depletion of glutathione was concentration dependent and maximal at 5-15 min. Addition of either of the enantiomeric oxides at 60 microM resulted in the loss of more than 20 nmol glutathione/10(6) cells (1 ml cells); thus more than a third of the added epoxide was available for conjugation with intracellular glutathione. The time course and concentration dependence of glutathione depletion corresponded to the rapid, concentration-dependent formation of naphthalene oxide glutathione conjugates. The levels of glutathione adduct were highest 1 min after addition of naphthalene oxide and declined to 25% of this level after 30 min. Loss of glutathione conjugates from incubations correlated with the formation of N-acetylcysteine adducts. In contrast, the levels of glutathione adducts added exogenously to hepatocytes were relatively stable over a 120-min incubation suggesting that although further metabolism of naphthalene oxide glutathione adducts formed intracellularly is possible, extracellular glutathione adducts cannot penetrate the hepatocellular membrane. Small amounts of radiolabel from [3H]naphthalene 1,2-oxide were bound covalently to macromolecules in hepatocytes; the rate of this binding slowed rapidly after the first minute of incubation. Severe blebbing of the surface of the hepatocytes was noted in cells incubated for 30 min with 480 microM naphthalene oxide. Many of the cells were vacuolated at 60 min and progressed to frank necrosis with pyknotic nuclei and inability to exclude trypan blue. Cells incubated with 1-naphthol responded in a qualitatively similar fashion to those cells incubated with epoxide; however, hepatocytes incubated with 1-naphthol progressed to frank cellular necrosis at a slower rate. In hepatocytes partially depleted of glutathione by pretreatment with buthionine sulfoximine, addition of 1S,2R-naphthalene oxide at a rate of 1 nmol/min/10(6) cells resulted in significant losses in cell viability. In contrast, no losses in cell viability were observed with the enantiomer, 1R,2S-naphthalene oxide. Both epoxides produced similar losses in cellular glutathione levels.(ABSTRACT TRUNCATED AT 400 WORDS)     

Differential effect of cycloheximide on penicillin and cephalosporin biosynthesis by Cephalosporium acremonium

In resting cells of Cephalosporium acremonium CW19, protein synthesis was inhibited completely by 100 μg cycloheximide per ml. Furthermore, ongoing protein synthesis halted abruptly when cycloheximide was added after 20 min of incubation. Although cycloheximide did not affect the specific rate of penicillin N production, it markedly inhibited the specific rate of cephalosporin C production. The effect of cycloheximide was not influenced by the carbon source used to prepare the cells for the resting cell system.     

Cloning and characterization of an epoxide hydrolase from Cupriavidus metallidurans-CH34

A putative epoxide hydrolase-encoding gene was identified from the genome sequence of Cupriavidus metallidurans CH34. The gene was cloned and overexpressed in Escherichia coli with His(6)-tag at its N-terminus. The epoxide hydrolase (CMEH) was purified to near homogeneity and was found to be a homodimer, with subunit molecular weight of 36 kDa. The CMEH had broad substrate specificity as it could hydrolyze 13 epoxides, out of 15 substrates tested. CMEH had high specific activity with 1,2-epoxyoctane, 1,2-epoxyhexane, styrene oxide (SO) and was also found to be active with meso-epoxides. The enzyme had optimum pH and temperature of 7.5 and 37°C respectively, with racemic SO. Biotransformation of 80 mM SO with recombinant whole E. coli cells expressing CMEH led to 56% ee(P) of (R)-diol with 77.23% conversion in 30 min. The enzyme could hydrolyze (R)-SO, ～2-fold faster than (S)-SO, though it accepted both (R)- and (S)-SO with similar affinity as K(m)(R) and K(m)(S) of CMEH were 2.05±0.42 and 2.11±0.16 mM, respectively. However, the k(cat)(R) and k(cat)(S) for the two enantiomers of SO were 4.80 and 3.34 s(-1), respectively. The wide substrate spectrum exhibited by CMEH combined with the fast conversion rate makes it a robust biocatalyst for industrial use. Regioselectivity studies with enantiopure (R)- and (S)-SO revealed that with slightly altered regioselectivity, CMEH has a high potential to synthesize an enantiopure (R)-PED, through an enantioconvergent hydrolytic process.     

Affinity purification and characterization of a yeast epoxide hydrolase

Purification of the membrane-associated epoxide hydrolase from the yeast Rhodosporidium toruloides CBS 0349 to electrophoretic homogeneity was achieved in a single chromatographic step employing the affinity ligand adsorbent Mimetic Green. More than 68% of the total epoxide hydrolase activity present in the whole cells was recovered from the membrane fraction. The enzyme was purified 26-fold with respect to the solubilized membrane proteins and was obtained in a 90% yield. The purified epoxide hydrolase has an apparent monomeric molecular weight of 54 kDa, and a pI of 7.3. The enzyme was optimally active at 30–40 °C, and pH 7.3–8.5. The enzyme is highly glycosylated with a carbohydrate content >42%. The specific activity of the purified enzyme for (±)-1,2-epoxyoctane is 172 mol min^–1 mg protein^–1. The amino acid composition of the protein was determined. This is the first report of a yeast epoxide hydrolase purified to homogeneity in milligram amounts.     

Production of 2-ketobutyric acid from 1,2-butanediol by resting cells of Rhodococcus equi IFO 3730

Summary Various microorganisms were screened for their ability to produce 2-ketobutyric acid (2-KBA) from 1,2-butanediol (1,2-BD). Among them, Rhodococcus equi IFO 3730 was selected as the best strain. The various culture and reaction conditions were optimized using this strain. Limitation of thiamine in the growing medium was found to be effective. The resting cells of the strain grown on 1,2-propanediol as the carbon source yielded 15.7 g/l of 2-KBA from 20 g/l of 1,2-BD after 32 h incubation at 30 °C in the reaction mixture under optimal conditions.     

Hydration of an 18O epoxide by a cytosolic epoxide hydrolase from mouse liver

The mechanism of enzymatic epoxide hydration by a cytosolic or 100,000 g soluble mammalian liver enzyme (in contrast to the microsomal enzymes) was examined by monitoring ¹⁸O distribution following chemical and enzymatic hydrations of ¹⁶O or ¹⁸O epoxide labeled (±) 1-(4′-ethylphenoxy)-3, 7-dimethyl-6, 7-epoxyoctane. Acid catalyzed hydration of the ¹⁸O epoxide in ¹⁶O water, and hydration of the ¹⁶O epoxide in ¹⁸O water, indicated that attack by water was predominantly on the tertiary carbon (C-7). Enzymatic epoxide hydration led to attack predominantly on secondary carbon (C-6). These data are consistent with water attacking as a nucleophile in the enzymatic reaction.     

The metabolism of 1,2-propanediol by the propylene oxide utilizing bacterium Nocardia A60

A bacterium designated Nocardia A60 was isolated for its capacity to utilize propylene oxide (1,2-epoxypropame) aerobically as a carbon and energy source for growth. Extracts of cells grown on the epoxide catalyzed the conversion of propylene oxide to 1,2-propanediol This epoxidase activity was absent in cells grown on 1,2-propanediol or succinate. During growth of the organism on propylene oxide and 1,2-propanediol it contained high levels of diol dehydratase (EC 4.2.1.28). Enhanced levels of propionyl-CoA carboxylase during growth on propylene oxide and 1,2-propanediol suggest that these compounds are metabolized via propionate and succinate.     

Epoxide hydrase in Trypanosoma cruzi epimastigotes.

1. Microsomal fractions from Trypanosoma cruzi epimastigotes catalyze the hydration of styrene oxide to styrene glycol. The activity is linear up to 45 min of incubation, is proportional to microsomal protein concentration within certain range, and has an optimum pH of 8.5. 2. Double-reciprocal plots indicate a Km value of 5.3 . 10(-4) M for styrene oxide and a V of 29.6 pmol of styrene glycol formed/min per mg protein at 37 degrees C. 4-Chlorophenyl-2,3-epoxypropyl either (Ki = 2.08 . 10(-4) M) and juvenile hormone I (Ki = 2.7 . 10(-4) M) are competitive inhibitors; whereas, 1-chloro-2,3-epoxypropane is a non-competitive inhibitor. The enzyme is induced about three-fold by 5 mM phenobarbital in the growth medium. 3. The epoxide hydrase is not activated by detergents but rather inhibited by concentrations of Tween-80 and Lubrol as low as 0.025%. 4. Experiments with intact cells indicate that about 3% of [8-14C]styrene oxide penetrates after 90 min of incubation; whereas, over 30% of juvenile hormone I is found intracellularly after the same incubation period. Intracellular styrene oxide is hydrated to styrene glycol to a significant extent and the in vivo hydration is increased by pretreatment with phenobarbital and inhibited upon the addition of 4-chlorophenyl-2,3-epoxypropyl ether. Only a small amount of the intracellular juvenile hormone I is recovered as the corresponding diol ester.     

Preparative-scale kinetic resolution of racemic styrene oxide by immobilized epoxide hydrolase

Epoxide hydrolase from Aspergillus niger was immobilized onto the modified Eupergit C 250 L through a Schiff base formation. Eupergit C 250 L was treated with ethylenediamine to introduce primary amine groups which were subsequently activated with glutaraldehyde. The amount of introduced primary amine groups was 220 μmol/g of the support after ethylenediamine treatment, and 90% of these groups were activated with glutaraldehyde. Maximum immobilization of 80% was obtained with modified Eupergit C 250 L under the optimized conditions. The optimum pH was 7.0 for the free epoxide hydrolase and 6.5 for the immobilized epoxide hydrolase. The optimum temperature for both free and immobilized epoxide hydrolase was 40 °C. The free epoxide hydrolase retained 52 and 33% of its maximum activity at 40 and 60 °C, respectively after 24 h preincubation time whereas the retained activities of immobilized epoxide hydrolase at the same conditions were 90 and 75%, respectively. Immobilized epoxide hydrolase showed about 2.5-fold higher enantioselectivity than that of free epoxide hydrolase. A preparative-scale (120 g/L) kinetic resolution of racemic styrene oxide using immobilized preparation was performed in a batch reactor and (S)-styrene oxide and (R)-1-phenyl-1,2-ethanediol were both obtained with about 50% yield and 99% enantiomeric excess. The immobilized epoxide hydrolase was retained 90% of its initial activity after 5 reuses.     

Influence of luteinizing hormone and adenosine 3':5'-cyclic monophosphate on the metabolism of free and esterified cholesterol in mouse Leydig-cell tumours

1. Male C57B1/6J mice bearing Leydig-cell tumours known to synthesize steroids in response to luteinizing hormone (LH) were given intravenous injections of [1,2-(3)H]cholesterol (50-100muCi per animal). Single-cell suspensions were prepared from the tumours 5-9 days after the injection of [(3)H]cholesterol and were incubated at 37 degrees C in foetal calf serum supplemented with 50mm-Tris-HCl, pH7.4. At various times after the start of incubation cells were collected by filtration of portions of the suspension and their sterols analysed. Within 10min after LH (5mug/ml) or 3':5'-cyclic AMP (20mm) was added to the cell suspensions an increased conversion of ester cholesterol into free cholesterol could be demonstrated. 2. To observe this rapid effect of LH it was necessary to incubate the cells for 60min before addition of hormone. 3. The specific radioactivity of testosterone produced was approximately equal to that of the intracellular cholesterol regardless of the presence or absence of LH. 4. The amount of free cholesterol produced in response to LH was far greater than that needed for steroid synthesis. 5. Free cholesterol, but not esterified cholesterol, was released into the incubation medium linearly with time and this release was unaffected by LH. LH may stimulate steroidogenesis in part by increasing the concentration of free cholesterol within the cell.     

Interaction of epoxide hydrolase with itself and other microsomal proteins

The interactions of rat liver epoxide hydrolase (EC 3.3.2.3) with itself and with cytochromes P-450 and NADPH-cytochrome P-450 reductase were investigated in microsomal preparations and in reconstituted systems in which all of the enzymes are functionally active. Hydrodynamic measurements indicated that purified epoxide hydrolase behaves as a single aggregate of approximately 16 monomeric units and that further aggregation of the protein only occurs in the presence of high concentrations of phospholipid. Neither guanidine-HCl nor the nonionic detergent Lubrol PX was able to completely dissociate the aggregate into monomers. The interactions of epoxide hydrolase with NADPH-cytochrome P-450 reductase and the major forms of cytochrome P-450 isolated from phenobarbital- and 5,6-benzoflavone-treated rats were studied by Soret difference spectroscopy, by perturbation of the fluorescence of NADPH-cytochrome P-450 reductase and fluorescein-labeled epoxide hydrolase, and by CD spectroscopy. The spectra provided evidence that binding of the proteins to each other occurs and some of the results suggest that affinity constants are on the order of 10⁷, m^?1. The spectral perturbations were not observed with other intrinsic membrane proteins. When microsomes were treated with the crosslinking reagent dimethylsuberimidate and solubilized with detergents, epoxide hydrolase could be precipitated with antibodies raised to cytochromes P-450 or NADPH-cytochrome P-450 reductase. Transient times were determined for the conversion of 1-octene to octene-1,2-dihydrodiol in a reconstituted enzyme system and for the conversion of naphthalene to naphthalene-1,2-dihydrodiol in rat liver microscomes and compared to the transient times predicted from the enzymatic rates of hydrolysis of the intermediate epoxides. In all cases the observed transient times were shorter than expected, in support of the view that coupling of epoxide hydrolase with cytochromes P-450 occurs. These results support the view that epoxide hydrolase couples with cytochrome P-450-containing mixed-function oxidase systems and may have relevance to the metabolism of potentially harmful xenobiotics by these enzymes.     

丝氨酸生产菌的筛选及静息细胞培养系统中L-丝氨酸的合成

从广西隆安县沼气池里的残渣中筛选到一株能以甲醇为唯一碳源生长的MB200菌株。根据常规形态特征、生理生化性状及16S rDNA基因序列分析将其鉴定为甲基杆菌属(M ethylobacteriumsp.)。其最佳生长条件为:温度32℃、pH值8.0、甲醇体积分数1.25%。建立了MB200生成L-丝氨酸的静息细胞培养系统。确定静息细胞培养的条件为:甘氨酸质量浓度为10 g.L-1,甲醇50 g.L-1,菌体质量浓度为30 g.L-1,pH8.9,于摇床250 r.m in-1,32℃静息培养48 h,L-丝氨酸产量为7.2 g.L-1。