Jia-Ying Xin

Production of methanol from methane by methanotrophic bacteria

Methanotrophs can oxidize methane to carbon dioxide through sequential reactions catalyzed by a series of enzymes including methane monooxygenase, methanol dehydrogenase, formaldehyde dehydrogenase, and formate dehydrogenase. When suspensions of methanotrophic bacteria of Methylosinus trichosporium IMV 3011 were incubated at 32°C with methane and oxygen, there was an extracellular accumulation of methanol from methane oxidation in response to carbon dioxide addition. Maximal accumulation of methanol was achieved with 40% carbon dioxide in the mixed reaction gases. A continuous experiment was performed in a continuous ultrafiltration reactor. The optimum gas mixture containing 20% (v v−1) methane, 20% oxygen, 20% nitrogen and 40% carbon dioxide was used to provide substrates and to maintain the transmembrane pressure. The product (methanol) was removed in the eluate buffer. The initial methanol concentration in the eluate buffer was 8.22 μmol L−1. The bioreactor was operated continuously for 198 h without obvious loss of productivity.

Biosynthesis of poly-3-hydroxybutyrate with a high molecular weight by methanotroph from methane and methanol

Abstract Poly-3-hydroxybutyrate (PHB) can be produced by various species of bacteria. Among the possible carbon sources, both methane and methanol could be a suitable substrate for the production of PHB. Methane is cheap and plentiful not only as natural gas, but also as biogas. Methanol can also maintain methanotrophic activity in some conditions. The methanotrophic strain Methylosinus trichosporium IMV3011 can accumulate PHB with methane and methanol in a brief nonsterile process. Liquid methanol (0.1%) was added to improve the oxidization of methane. The studies were carried out using shake flasks. Cultivation was performed in two stages: a continuous growth phase and a PHB accumulation phase under the conditions short of essential nutrients (ammonium, nitrate, phosphorus, copper, iron (III), magnesium or ethylenediamine tetraacetate (EDTA)) in batch culture. It was found that the most suitable growth time for the cell is 144 h. Then an optimized culture condition for second stage was determined, in which the PHB concentration could be much increased to 0.6 g/L. In order to increase PHB content, citric acid was added as an inhibitor of tricarboxylic acid cycle (TCA). It was found that citric acid is favorable for the PHB accumulation, and the PHB yield was increased to 40% (w/w) from the initial yield of 12% (w/w) after nutrient deficiency cultivation. The PHB produced is of very high quality with molecular weight up to 1.5×106Da.

Colorimetric detection of melamine based on methanobactin-mediated synthesis of gold nanoparticles

A simple and rapid field-portable colorimetric method for the detection of melamine in liquid milk was reported. Methanobactin (Mb) could reduce Au (III) to Au (0) and mediate the synthesis of gold nanoparticles (Au-NPs). Upon the addition of melamine, melamine interacted with oxazolone ring of Mb, which interrupted the formation of Au-NPs. Melamine could also stimulate the aggregation of formed Au-NPs. In this paper, these characteristics have been used to detect melamine in liquid milk by naked eyes observation with a detection limit of 5.56 × 10(-6)M (0.7 mg/kg). Further, the plasmon absorbance of the formed Au-NPs allowed the quantitative detection of melamine by UV-vis spectrometer. A linear correlation was existed between the absorbance and the melamine concentration ranging from 3.90 × 10(-7)M to 3.97 × 10(-6)M with a correlation coefficient of 0.9685. The detection limit (3σ) obtained by UV-vis spectrum was as low as 2.38 × 10(-7)M (i.e., 0.03 mg/kg).

Enzymatic resolution of (S)-(+)-naproxen in a trapped aqueous-organic solvent biphase continuous reactor.

A trapped aqueous-organic biphase system for the continuous production of (S)-(+)-2-(6-methoxy-2-naphthyl) propionic acid (Naproxen) has been developed. The process consists of a stereoselective hydrolysis of the racemic Naproxen methyl ester by Candida rugosa lipase in a trapped aqueous-organic biphase system. The reaction has been carried out in a laboratory-scale continuous-flow stirred tank reactor (CSTR). The staring material has been supplied in and remaining substrate recovered by organic phase. YWG-C(6)H(5), a poorly polar synthetic support, has been employed to immobilize the lipase and to restrict the aqueous phase. Lipase immobilized on YWG-C(6)H(5) containing aqueous phase has been added into the CSTR to catalyze the hydrolysis. A dialysis membrane tube containing a continuous flow closed-loop buffer has been applied in the CSTR for the extraction of product and recruiting of the aqueous part consumed. Various reaction conditions have been studied. The activity of immobilized enzyme was effected by the polarity of support, the substrate concentration, logP value of organic phase and the product inhibition. At steady-state operating conditions, an initial conversion of 35% has been obtained. The CSTR was allowed to operate continuously for 60 days at 30 degrees C with a 30% loss of activity. The hydrolysis reaction yielded (S)-(+)-Naproxen with >90% enantiomeric excess and overall conversion of 30%.

Improvement of the enantioselectivity of lipase-catalyzed naproxen ester hydrolysis in organic solvent.

A method is presented to improve the enantioselectivity of lipase-catalyzed hydrolysis of naproxen methyl ester in water-saturated isooctane. It is shown that coupling of the enantioselective hydrolysis of Naproxen methyl ester with the photo-dissociation methanol leads to the photocatalytic conversion of methanol into water, by which the equilibrium constant (K) of the lipase-catalyzed hydrolysis was changed. The equilibrium yield and enantiomeric excess are increased. Because the lipase would not dissolve in the organic solvent, it was adsorbed on photocatalyst particles, which may facilitate the isolation of enzyme from reaction system.

Particulate methane monooxygenase from Methylosinus trichosporium is a copper-containing enzyme

Particulate methane monooxygenase (pMMO) has been exfoliated and isolated from membranes of the Methylosinus trichosporium IMV 3011. It appears that the stability of pMMO in the exfoliation process is increased with increasing copper concentration in the growth medium, but extensive intracytoplasmic membrane formed under higher copper concentration may inhibit the exfoliation of active pMMO from membrane. The highest total activity of purified pMMO is obtained with an initial concentration of 6 microM Cu in the growth medium. The purified MMO contains only copper and does not utilize NADH as electron donor. Treatment of purified pMMO with EDTA resulted in little change in copper level, suggesting that the copper in the pMMO is tightly bound with pMMO.

Continuous biocatalytic synthesis of epoxypropane using a biofilm reactor

Abstract Mixed culture methanotrophic attached biofilms immobilized on diatomite particles in a three-phase fluidized bed reaction system were developed. Methane monooxygenase (MMO) activity on diatomite particles increased as soon as the lag phase ended. More than 90% of the MMO activity in the fluidized bed was attached. A biofilm concentration of 3.3c3.7mg dry weight cell (dwc) per g dry solid (DS) was observed. Batch experiments were performed to explore the possibility of producing epoxypropane by a propene–methane co-oxidation process. The effect of methane on the epoxidation of propene and the effect of propene on the growth of methanotroph was also studied. In continuous experiments, optimum mixed gas containing 35 methane, 20 propene and 45% oxygen were continuously circulated through the fluidized bed reactor to deliver substrates and extract product. Initial epoxypropane productivity was 110–150 μmol/day. The bioreactor operated continuously for 53 days without obvious loss of epoxypropane productivity.

Fine separation and characterization of Candida rugosa lipase isoenzymes.

Commercial Candida rugosa lipase has been separated into two distinct fractions (CRLA and CRLB) by anion‐exchange chromatography. As analyzed on SDS‐polyacrylamide gel electrophoresis, CRLA and CRLB are homogenous. At high ionic strength, CRLA and CRLB have similar hydrophobicity and UV spectra, suggesting that the open extent of the large hydrophobic pockets of CRLA and CRLB may be similar. At low ionic strength, using “hydrophobic interfacial affinity chromatography”, both CRLA and CRLB have been separated into four isofractions. They have different hydrophobicity and UV spectra, suggesting that the open extent of the large hydrophobic pocket of the four forms may be different. Further, the conversion of CRL isoenzymes in the process of organic solvent treatment and ester hydrolysis were examined. The results clearly showed not only that CRLB had been converted to CRLA, but also that CRLA sub‐fractions with different open extent of large hydrophobic pocket had been converted

Efficient microbial elimination of methanol inhibition for Naproxen resolution by a lipase

To eliminate methanol inhibition of the activity of a lipase, methanotrophic bacteria, which can convert methanol into water and CO2, were introduced to the reaction of enantioselective hydrolysis of Naproxen methyl ester catalysed by lipase from Candida rugosa. Both the activity and stability of lipase were improved by the removal of methanol by the bacteria.

Epoxypropane biosynthesis by Methylomonas sp. GYJ3: batch and continuous studies

Methylomonas sp. GYJ3 is a methanotrophic bacterium containing methane monooxygenase (MMO), which catalyses the epoxidation of propene to epoxypropane. In this study, the cell suspension of Methylomonas sp. GYJ3 has been used for epoxypropane biosynthesis from propene. When propene is epoxidized, the product epoxypropane is not further metabolized and accumulates extracellularly. Unfortunately, continuous production of epoxypropane is usually difficult due to exhaustion of reductant and the accumulation of toxic products. Hence, in order to address these problems, batch experiments were performed to explore the possibility of producing epoxypropane by a co-oxidation process. Methane was chosen as the most suitable electron-donating co-substrate since it did not result in molecular toxicity and provided abundant reductant for epoxidation. It was found that the maximum production of epoxypropane occurred in an atmosphere of 30% methane. Batch experiments also indicated that continuous removal of product was necessary to overcome the inhibition of epoxypropane. In continuous experiments, optimum mixed gaseous substrates were continuously circulated through the stirred tank bioreactor to remove product from the cell suspension. Initial epoxypropane productivity was 268 μmol/day. The bioreactor has been allowed to operate continuously for 12 days without obvious loss of epoxypropane productivity, and more than 96% of initial MMO activity was retained.