Isolation and characterization of alkene-utilizing Xanthobacter spp.

Yellow-pigmented bacteria showing typical characteristics of Xanthobacter spp. were isolated from enrichments with propene and 1-butene, using classical techniques. The generation time for growth on propene and 1-butene of these bacteria ranged from 5 to 7h. A NADH-dependent mono-oxygenase was identified in cell-free extract of Xanthobacter Py2. This mono-oxygenase was not influenced by potential inhibitors tested indicating that propene mono-oxygenase is different from other hydrocarbon mono-oxygenases described until now. Nitrogenase activity could be measured using the acetylene reduction assay with propene as energy source, because acetylene did not inhibit the mono-oxygenase activity.     

Cloning and expression of the genes encoding the propene monooxygenase from Xanthobacter, Py2

Xanthobacter Py2 grows on propene as sole carbon source, converting propene to propene oxide (epoxypropane) using an alkene-specific monooxygenase, as the first step in catabolism. Four mutants, NZ1–4, with a propene^– propene oxide⁺ phenotype were isolated by 1-methyl-3-nitro-1-nitrosoguanidine mutagenesis or by enrichment with the suicide substrate vinylidene chloride, and were shown to have lost the ability to convert alkenes to epoxides. All four mutants were complemented by a number of clones of Xanthobacter Py2 chromosomal DNA in the broad-host-range cosmid pLAFR5, some of which appeared to be non-overlapping. Representatives of the different clones obtained were transferred into Xanthobacter autotrophicus JW33 and one, pNY2, the most frequently isolated clone, was shown to express an inducible, fully functional propene monooxygenase. Subcloning revealed that all four mutants were complemented by a 2.4-kb EcoRI-PstI fragment situated at one end of the cosmid insert. However, activity in X. autotrophicus JW33 could only be expressed from pNY2, containing the complete insert (25 kb), suggesting a large operon or some form of long-range control. pNY2 failed to express in E. coli. In X. autotrophicus JW33 [pNY2] at least three new polypeptides were evident after induction with propene compared with a control carrying only the cosmid pLAFR5.     

Production of epoxides from gaseous alkenes by resting-cell suspensions and immobilized cells of alkene-utilizing bacteria

Summary Newly isolated and already available strains of alkene-utilizing bacteria were able to oxidize ethene, propene or 1-butene to the respective 1,2-epoxides. Resting-cell suspensions of organisms isolated on propene and butene, when grown on these substrates converted ethene quantitatively to epoxyethane. Some, but not all ethene-utilizing strains accumulated 1,2-epoxypropane or 1,2-epoxybutane when propene or butene was supplied, although not quantitatively because the epoxides produced were partially further metabolized. Suitable epoxide producers which eventually may be employed as biocatalysts in a biotechnological process were used for immobilization in calcium alginate and K-carrageenan; after immobilization, 60%–100% activity for epoxide production was retained.     

Extending the alkene substrate range of vinyl chloride utilizing Nocardioides sp. strain JS614 with ethene oxide

Nocardioides sp. strain JS614 grows on the C₂ alkenes ethene (Eth), vinyl chloride, and vinyl fluoride as sole carbon sources. The presence of 400–800 μM ethene oxide (EtO) extended the growth substrate range to propene (C₃) and butene (C₄). Propene-dependent growth of JS614 was CO₂ dependent and was prevented by the carboxylase/reductase inhibitor 2-bromoethanesulfonic acid, sodium salt (BES), while growth on Eth was not CO₂ dependent or BES sensitive. Although unable to promote growth, both propene and propene oxide (PrO)-induced expression of the genes encoding the alpha subunit of alkene monooxygenase (etnC) and epoxyethane CoM transferase (etnE) to similar levels as did Eth and EtO. Propene was transformed by Eth-grown and propene-grown/EtO-induced JS614 to PrO at a rate 4.2 times faster than PrO was consumed. As a result PrO accumulated in growth medium to 900 μM during EtO-induced growth on propene. PrO (50–100 μM) exerted inhibitory effects on growth of JS614 on both acetate and Eth, and on EtO-induced growth on Eth. However, higher EtO concentrations (300–400 μM) overcame the negative effects of PrO on Eth-dependent growth.     

Propene removal from synthetic waste gas using a hollow-fibre membrane bioreactor

 Hollow-fibre modules containing microporous membrane material were evaluated as bioreactors for waste gas treatment. The reactors were inoculated with the propene-utilizing strain Xanthobacter Py2, which formed a biofilm on the inner side of the fibres. The removal of the poorly soluble volatile propene from synthetic waste gas was monitored for up to 170 days. The maximum removal rates were 70–110 g propene per m³ reactor per hour. A gas residence time of 80 s was required to remove 95% of an initial propene concentration of 0.84 g/m³. The presence of ammonium in the liquid medium resulted in the development of an additional population of nitrifying organisms. Therefore, nitrate was used as the source of nitrogen in later experiments. During long-term operation, the propene removal rates gradually decreased. At low liquid velocities (1–5 cm/s) clogging of individual fibres with excess biomass was observed. Elevation of the liquid velocity in the fibres to 90 cm/s resulted in the formation of a dense biofilm and prevented clogging of the fibres. However, also at this high liquid velocity a gradual decrease in propene removal rate was observed. These results suggest that aging of biofilms is a very important factor in long-term operation of hollow-fibre bioreactors. Received: 24 November 1995 / Received revision: 14 February 1996 / Accepted: 20 February 1996     

Inactivation of alkene oxidation by epoxides in alkene-and alkane-grown bacteria

Summary The oxidation of propene by resting-cells of ethene-grown Mycobacterium E3 was inactivated by 1,2-epoxypropane. Inactivation increased with increasing epoxide concentrations with 50% inactivation at approximately 30 mM epoxide. Other lower epoxides as epoxyethane and 1,2-epoxybutane also inactivated oxidation of propene as well as of other alkenes. Propene oxidation by resting-cells of ethane-grown Mycobacterium E20 and resting-cells of methane-grown Methylosinus trichosporium OB3b was inactivated for 50% at much lower 1,2-epoxypropane concentrations of approximately 1 and 3 mM respectively. It was demonstrated that in vivo the predominant effect of 1,2-epoxypropane was on the epoxidizing enzyme, i.e. alkene mono-oxygenase (strain E3), alkane mono-oxygenase (strain E20) and methane mono-oxygenase (methylotroph) and that the effect of the epoxide on the alkene mono-oxygenase was irreversible.     

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 mol/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.     

Oxidation of propene and 1-butene byMethylococcus capsulatus andMethylosinus trichosporium

Summary Methane-grown cells ofMethylococcus capsulatus andMethylosinus trichosporium readily oxidized propene and various isomers of butene to their respective epoxides. When examined in a proton NMR spectrum using tris([3-trifluoromethylhydroxymethylene]-d-camphorato), europium III derivative as an optically active chemical shift reagent, the products propylene oxide and 1,2-epoxybutane were found to contain equal amounts of both isomers. Methane-grown cells of both bacteria had considerable levels of reducing equivalents to catalyze the epoxidation of gaseous olefins. Cells depleted of reductants catalyzed the oxidation in the presence of low levels of methanol or formaldehyde with a stoichiometry of about 2:1. The rates of epoxidation of propene and 1-butene in a continuous reactor were 2–3-times that of a batch-wise reaction; the epoxidation activity, however, was lost within 3 h. The inactivation was attributed to the reactivity of the accumulated epoxides in the reactor. Propene and 1-butene oxidation by both bacteria were drastically inhibited by the respective products. Thus, the major problem in the application of microorganisms for production of epoxides from gaseous olefins is the rapid separation of the reactive products.     

Purification and Characterization of the Alkene Monooxygenase from Nocardia corallina B-276

Alkene monooxygenase from the propene utilizer Nocardia corallina B-276 was separated into three components, and all components were purified to homogeneity and their properties were examined. The epoxidase, with a molecular mass of 95 kDa, was considered to catalyze the oxidation of the substrate propene to propylene oxide. It consisted of 53- and 35-kDa subunits, which contained approximately 2-mol of non-heme iron per mole of protein. The reductase, molecular mass 40 kDa, was found to contain an FAD and an Fe₂ S₂ cluster. A third protein, which we have called the coupling protein, with a mass of 14 kDa, appears to function as a regulator of activity. The purified AMO system required NADH as an electron donor, and catalyzed alkene epoxidation only. Acetylene, a specific inhibitor for methane monooxygenase, did not inhibit the AMO activity.     

Biocatalysts for production of chiral epoxides

Summary A number of bacterial strains, representing a range of genera, were isolated in pure culture with ethene or propene as the sole source of carbon and energy. The organisms included Aerococcus, Alcaligenes, Micrococcus and Staphylococcus spp. and a variety of Gram-negative, Gram-positive and Gram-variable mesophilic rods/ coccobacilli not yet identified. This suggests that the ability to utilize gaseous olefins is more widespread in nature than previously recognised. All 18 organisms tested stereospecifically formed R-1,2-epoxypropane (enantiomeric excess, ee=90–96%), R-1,2-epoxybutane (ee=90–98%) and trans-(2R,3R)-epoxybutane (ee=64–88%) from the corresponding olefins. In addition to Micrococcus sp. M90C, the substrate specificities of six other organisms were studied. The pattern of reactivity for the group of four ethene (M26, M90C, M93A, M186)- and two propene (M142, M156)-utilizers differed from that found with peracids, whereas the chemical reactivity of the substrate appeared to affect enzymatic epoxidations in Staphylococcus sp. M97B. Offprint requests to: M. Mahmoudian     

Production of propene oxide in an organic liquid-phase immobilized cell reactor

Some major restrictions of the production of propene oxide in an organic liquid-phase immobilized cell packed-bed reactor were quantified, and techniques were investigated to enhance the epoxide production rates. Propene-epoxidizing Mycobacterium cells were entrapped in calcium alginate gel and contacted with the substrates, propene and oxygen, which were dissolved in a continuous organic phase, n-hexadecane. The effects of product inhibition by the toxic epoxide—microbial consumption of propene oxide and immobilized cell deactivation—restricted severely the accumulation of the epoxide in the recirculation reactor system and could be predicted using a simple mathematical model. Epoxide inhibition was reduced by absorbing the product in the gas phase in old di-n-octyl phthalate. The resulting increase in propene oxide production agreed with model calculations. An alternating supply of propene and a co-substrate (ethene) prolonged the half-life of the immobilized cells. Using 50 g dry weight of cells, 1.5 g stereospecific propene oxide was produced in two days, of which 1.0 g was absorbed in the di-n-octyl phthalate phase.     

Epoxidation of alkenes by alkene-grown Xanthobacter spp.

Summary Newly isolated Xanthobacter spp. were able to grow on the gaseous alkenes like ethene, propene, 1-butene and 1,3-butadiene. Resting-cell suspensions of propene-, 1-butene- or 1,3-butadiene-grown Xanthobacter Py10 accumulated 1,2-epoxyethane from ethene. Ethene-grown Xanthobacter Py10 did not produce any 1,2-epoxyalkane from the alkenes tested. Furthermore, propenegrown Xanthobacter Py2 accumulated 2,3-epoxybutane from trans-butene and cis-butene but did not form epoxides from other substrates tested.     

Batch cultivation of Xanthobacter Py2 on 1-pentene

Summary The propene isolated strain Xanthobacter Py2 was able to grow on 1-pentene. The biomass yield for growth under 1-pentene limiting conditions was 0.48 (Ceq/Ceq). Upon storage at both +4°C and -20°C no loss of enzymatic epoxide degrading activity in resting cell suspensions was observed after a month. However, activity decay was pronounced during the stationary phase of growth as well as under reaction conditions.     

Stereospecific formation of 1,2-epoxypropane, 1,2-epoxybutane and 1-chloro-2,3-epoxypropane by alkene-utilizing bacteria

Resting cells of ethene grown Mycobacterium 2W produced 1,2-epoxypropane stereospecifically from propene as revealed by optical rotation, ¹H n.m.r. using a chiral shift reagent, and also by complexation gas chromatography involving a glass capillary column coated with an optically active metal chelate. The gas-liquid chromatography method allowed the rapid screening of 11 strains with regard to stereospecific formation of 1,2-epoxypropane, 1,2-epoxybutane and 1-chloro-2,3-epoxypropane. Bacteria grown on either ethene, propene or butadiene all predominantly produced the R form of 1,2-epoxypropane from propene and 1,2-epoxybutane from 1-butene while the strains tested for 1-chloro-2,3-epoxypropane production from 3-chloro-1-propene predominantly accumulated the S enantiomer.     

Continuous degradation of trichloroethylene by Xanthobacter sp. strain Py2 during growth on propene.

Propene-grown Xanthobacter sp. strain Py2 cells can degrade trichloroethylene (TCE), but the transformation capacity of such cells was limited and depended on both the TCE concentration and the biomass concentration. Toxic metabolites presumably accumulated extracellularly, because the fermentation of glucose by yeast cells was inhibited by TCE degradation products formed by strain Py2. The affinity of the propene monooxygenase for TCE was low, and this allowed strain Py2 to grow on propene in the presence of TCE. During batch growth with propene and TCE, the TCE was not degraded before most of the propene had been consumed. Continuous degradation of TCE in a chemostat culture of strain Py2 growing with propene was observed with TCE concentrations up to 206 microns in the growth medium without washout of the fermentor occurring. At this TCE concentration the specific degradation rate was 1.5 nmol/min/mg of biomass. The total amount of TCE that could be degraded during simultaneous growth on propene depended on the TCE concentration and ranged from 0.03 to 0.34g of TCE per g of biomass. The biomass yield on propene was not affected by the cometabolic degradation of TCE.     

Membrane bioreactor with a porous hydrophobic membrane as a gas-liquid contactor for waste gas treatment

A novel type of bioreactor for waste gas treatment has been designed. The reactor contains a microporous hydrophobic membrane to create a large interface between the waste gas and the aqueous phase. To test the new reactor, propene was chosen because of its high air/water partition coefficient, which causes a low water concentration and hampers its removal from air. Propene transfer from air to a suspension of propene-utilizing Xanthobacter Py2 cells in the membrane bioreactor proved to be controlled by mass transfer in the liquid phase. The resistance of the membrane was negligible. Simulated propene transfer rates agreed well with the experimental data. A stable biofilm of Xanthobacter Py2 developed on the membrane during prolonged operation. The propene flux into the biofilm was 1 x 10(-6) mol m(-2) s(-1) at a propene concentration of 9.3 x 10(-2) mol m(-3) in the gas phase. (c) 1995 John Wiley & Sons, Inc.     

Continuous biocatalytic synthesis of epoxypropane using a biofilm reactor

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.     

水-有机溶剂两相体系中甲基单孢菌Z201细胞催化丙烯环氧化的初步研究

Laabe于1987年提出了生物催化剂工程(Biocatalyst engineering)和介质工程(Medium engineering)的概念^[1]。有机相生物催化中溶剂的选择也是介质工程的内容之一。纯酶在有机相中的催化作用已有大量报道^[2],但对完整细胞研究甚步。本文以甲基单胞菌(Methylomonas Z201)完整细胞为生物催化剂．丙烯环氧化为指标反应．研究有机溶剂对活性的影响并对催化活性——溶剂疏水性进行了相关性分析。研究了水一十六烷两相体系中十六烷含量和搅拌速度对丙烯环氧化速度的影响和细胞的操作稳定性。     

水-有机溶剂两相体系中甲基单胞菌Z201催化丙烯环氧化的初步研究

Lanne于1987年提出了生物催化剂工程（Biocatalyst engimeering）和介质工程（Medium enineering）的概念^[1].有机相生物催化中溶剂的选择也是介质工程的内容之一。纯酶在有机相中的催化作用已有大量报道^[2],但对完整细胞研究甚少。本文以甲基单胞菌（Methylomonos）Z201完整细胞为生物催化剂,丙烯环氧化为指标反应,研究有机溶剂对活性的影响并对催化活性-溶剂疏水性进行了相关性分析。研究了水-十六烷两相体系中十六烷含量和搅拦速度对丙烯环氧化速度的影响和细胞的操作稳定性。     

单相和两相发酵体系中Methylomonas Z201细胞的生长和环氧丙烷的合成

研究了单相和两相发酵体系中甲基单胞菌（Methylomonas）Z201细胞的生长和环氧丙烷的合成。在单相发酵体系中,底物丙烯和产物环氧丙烷抑制细胞生长,水相中环氧丙烷的浓度达到13mmol／L。在两相发酵体系中,十六烷作为生长底物甲烷以及反应底物丙烯和分子氧的“储器”,减小了丙烯对细胞生长的抑制作用,水相和十六烷相中环氧丙烷的浓度分别达到1．7mmol／L和2．6mmol／L。同休止细胞相比,单相和两相发酵体系中辅酶NADH的原位再生使生长细胞的操作稳定性显著提高,尤为两相体系为甚。