INTRODUCTION

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A number of bacteria can utilize gaseous and liquid alkanes as growth substrates (5, 7, 43). n-Alkanes are oxidized to the corresponding primary or secondary alcohols by monooxygenases through either monoterminal oxidation, biterminal oxidation, or subterminal oxidation (4, 5, 37, 42). Due to their broad substrate specificities, alkane monooxygenases are capable of cometabolically degrading a number of chlorinated hydrocarbons (1, 8, 24, 47, 49); consequently, alkane-oxidizing bacteria have been studied for their potential use in bioremediation (11, 30, 45-47, 49). Alkane-oxidizing bacteria can be conveniently divided into three groups based on the length of the alkane growth substrate. Methane (C₁)-oxidizing bacteria are confined to methane as a growth-supporting alkane. Other gaseous alkanes (C₂ to C₄) will support the growth of the second group of alkane-oxidizing bacteria, while those bacteria which grow on the liquid alkanes (C₅ to C₁₂) constitute the third group.

Both methane and liquid alkane utilizers have been well characterized. Methane utilizers, methanotrophs, oxidize methane to methanol by the methane monooxygenase (MMO). There are two distinct forms of MMO: all methanotrophs can produce a membrane-bound particulate form of MMO (pMMO), while only some methanotrophs can produce a soluble form of MMO (sMMO) (31, 51). sMMO, which is produced under conditions of copper limitation (41), has broad substrate specificity and oxidizes alkanes (up to C₇) to alcohols and alkenes to epoxides or enols (22). sMMO has been purified and well characterized biochemically as well as genetically. It consists of three protein components: a hydroxylase (245 kDa) containing a binuclear iron cluster that is the active site of MMO, a reductase (40 kDa) containing flavin adenine dinucleotide and an [Fe₂-S₂] cluster, and a regulatory subunit (16 kDa) (18-20). In contrast to sMMO, pMMO is produced under conditions of copper sufficiency in methanotrophs. Although pMMO has a narrower substrate range than sMMO, it can still catalyze the cooxidation of several alternative substrates, including propane and butane (9, 12). pMMO consists of three polypeptides with molecular masses of 47, 27, and 25 kDa (51). Zahn and DiSpirito (51) recently proposed a model for pMMO in which the catalytic site involves both iron and copper. The functions of each subunit and their interaction are not well understood.

Among the group of bacteria which oxidize longer-chain, liquid alkanes (C₅ to C₁₂), the alkane hydroxylase system in Pseudomonas oleovorans has been characterized most thoroughly. P. oleovorans can grow on 6 to 12 carbon n-alkanes (5). The substrate range includes straight-chain, branched, and cyclic alkanes and fatty acids but not alkenes and arenes (33). Alkane monooxygenase consists of three polypeptides: an alkane hydroxylase (AlkB; 41 kDa), a rubredoxin (AlkG; 19 kDa), and a rubredoxin reductase (AlkT; 41 kDa) (15-17). Recently, Shanklin et al. showed that the alkane hydroxylase contains a binuclear iron cluster which is found in soluble diiron proteins, such as MMO, hemerythrin, and ribonucleotide reductase (39).

Short-chain, gaseous alkanes (C₂ to C₄) are utilized by the bacteria that mainly belong to the Corynebacterium-Nocardia-Mycobacterium-Rhodococcus complex (4, 34). In addition, some gram-negative Pseudomonas spp., including Pseudomonas butanovora, have been found to grow on short-chain alkanes (43). Studies have shown that short-chain alkanes can be oxidized by the monooxygenases to alcohols via terminal, subterminal, or a mixture of both pathways (4, 37, 42). There have been no descriptions of the purification to homogeneity of a monooxygenase from short-chain alkane-utilizing bacteria nor any isolations of genes that code for this group of monooxygenases. Our research focused on butane-oxidizing bacteria as representatives of this understudied group of alkane utilizers.

We chose three strains of butane-grown bacteria, P. butanovora, Mycobacterium vaccae JOB5, and an environmental isolate, CF8, and characterized their butane monooxygenases at the physiological level. P. butanovora was originally isolated from activated sludge for the purpose of biomass production from gaseous hydrocarbons (44). This gram-negative bacterium utilizes alkanes ranging from C₂ to C₉, primary alcohols and carboxylic acids of C₂ to C₄, and polyvalent alcohols of C₃ to C₄, while alkanes of C₁₀ and higher, C₁ compounds, n-alkenes, and sugars are not utilized. It has previously been shown (24) that the butane-grown P. butanovora can also degrade several chlorinated hydrocarbons, including chloroform, trichloroethylene, 1,2-cis-dichloroethylene, and vinyl chloride. Butane-grown P. butanovora oxidizes butane to 1-butanol by terminal oxidation (3). 1-Butanol is further oxidized to butyraldehyde and to butyrate. M. vaccae JOB5 was isolated from soil and can grow on a number of substrates, including butane and propane (7). This organism has a broad substrate range and cometabolically degrades a number of chlorinated hydrocarbons (8, 46, 47). Propane is metabolized by M. vaccae via either subterminal or terminal oxidation, while butane is thought to be metabolized via terminal oxidation only (36, 37). CF8, a gram-positive bacterium, was isolated from mixed cultures in microcosms enriched on butane from aquifer solids from the Hanford Department of Energy site in Washington State. Butane-grown CF8 has been shown to cometabolically degrade chlorinated hydrocarbons, including chloroform, trichloroethylene, 1,2-cis-dichloroethylene, 1,1,2-trichloroethane, and vinyl chloride (24).

In this work, we examined the effects of known monooxygenase inhibitors and inactivators on butane monooxygenase activities and [¹⁴C]acetylene-labeling patterns in butane-grown P. butanovora, M. vaccae, and CF8. The results showed some similarity along with remarkable diversity among these three butane monooxygenases. The substrate range of each butane monooxygenase was also examined.

	MATERIALS AND METHODS

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Bacterial strains and growth conditions. Cells of P. butanovora, CF8, and M. vaccae JOB5 were grown as previously described (24). P. butanovora (ATCC 43655) was cultured at 30°C with constant shaking in 150-ml sealed vials (50 ml of growth medium) with 7 ml of n-butane and 5 ml of CO₂ added as an overpressure. n-Butane gas (99.0%) was purchased from Airgas, Inc., Radnor, Pa. The growth medium consisted of 2 mM MgSO₄, 400 µM CaCl₂, 0.01% (wt/vol) yeast extract, and the same trace elements as described previously (50). The medium was buffered with phosphate ([pH 7.1] 60 mM (NH₄)₂HPO₄, 7 mM Na₂HPO₄ · 7H₂O, 15 mM KH₂PO₄). M. vaccae JOB5 (ATCC 29678) was grown in the Xanthobacter Py2 medium (50), except that NH₄Cl replaced NaNO₃, yeast extract was removed, and the pH was adjusted to 7.5. Cultures (50 ml of growth medium) were grown in 150-ml sealed vials with 50 ml of n-butane and 40 ml of O₂ added as an overpressure. CF8 was isolated from Hanford core material by growth on n-butane as the only carbon source. CF8 was grown in the same medium as M. vaccae with 50 ml of n-butane added as an overpressure. Cell growth was monitored by removing a portion of the cultures (1 ml) and measuring optical density at 600 nm (OD₆₀₀).

Butane degradation assay. Cells were harvested from cultures by centrifugation (6,000 × g for 10 min), washed twice with the same buffer as the growth medium, and then resuspended to a constant cell density (based on OD). To optimize the determination of butane degradation, the assays were carried out in reaction vessels with a liquid phase only. When compared to reaction vessels with a gas and liquid phase, this method shortened reaction times because changes in butane concentration were confined to a single liquid phase rather than the liquid and the larger reservoir of butane in the gas phase. Vials (2 ml) were sealed with screw caps and teflon-coated rubber liners (Alltech Associates, Inc., Deerfield, Ill.). The vials were filled with phosphate buffer as in the growth medium (1.5 ml), O₂-saturated phosphate buffer (0.5 ml), and glass beads to facilitate mixing. Butane-saturated phosphate buffer (170 µl) was added by syringe and displaced existing buffer through a needle. The assays were initiated by the addition of the concentrated cell suspension (100 µl). The reactions were carried out at 30°C in a water bath. Liquid samples (4 µl) were removed and analyzed for butane with a gas chromatograph (Shimadzu GC-8A) equipped with a flame ionization detector and a 30- by 0.1-cm inner diameter stainless steel column packed with Porapak Q (Alltech Associates, Inc.). The gas chromatograph was run at a column temperature of 80°C and a detector temperature of 220°C. Time courses of butane consumption were linear until the butane was consumed after 10 to 30 min. Experiments were repeated at least three times.

1-Butanol production. The assays were conducted in 10-ml serum vials containing phosphate buffer (900 µl) and 1-propanol (5 mM for P. butanovora and 10 mM for CF8) or 1-pentanol (10 mM for M. vaccae). The vials were sealed with butyl rubber stoppers and aluminum crimp seals (Wheaton Scientific, Millville, N.J.). Butane gas (900 µl) was added as an overpressure to the headspace. Concentrated cell suspension (100 µl) was added to start the reaction, and the reactions were carried out in a water bath with constant shaking at 30°C. Liquid samples (4 µl) were removed to measure 1-butanol with a gas chromatograph (same as above) at a column temperature of 150°C and a detector temperature of 220°C.

Inactivator and inhibitor assays. For inactivator assays, concentrated cell suspensions (100 µl) were incubated for 5 min at 30°C with constant shaking in the sealed 10-ml serum vials that contained phosphate buffer (1.4 ml) and either 0.1% (vol/gas-phase vol) acetylene (40 µM) or 0.1 or 10% (vol/gas-phase vol) ethylene (4.4 µM and 440 µM, respectively). The concentrations of acetylene (40) and ethylene (14) in the aqueous phase were calculated from Henry's constants. Sodium butyrate (1 mM) was added as an electron donor for P. butanovora. For ethylene oxide inactivation assays, concentrated cell suspensions (100 µl) were incubated for 6 min at 30°C with constant shaking in the sealed 10-ml serum vial containing phosphate buffer (400 µl) and 0.001, 0.01, or 0.1% (vol/total vol) ethylene oxide (3, 30, or 300 µM, respectively) (MG Industries, Malvern, Pa.). Control cells were incubated for 5 min in phosphate buffer alone (CF8 and M. vaccae) or phosphate buffer plus 1 mM sodium butyrate (P. butanovora). After incubation for the indicated times, inactivators were removed from the vials by opening the cap and purging with air for 2 min. Reaction mixtures (total volume, 1.5 ml) were then transferred to 2-ml sample vials containing O₂-saturated phosphate buffer (0.5 ml), and butane degradation was monitored with a gas chromatograph following the addition of butane-saturated phosphate buffer (170 µl). For inhibition assays, cells were preincubated as described above for control cells. After 5 min, vials were purged with air, allyl thiourea (ATU; 200 µM or 2 mM) was added, and butane degradation was monitored as described above.

Induction assay. Cells of P. butanovora were grown in the medium described above without butane but supplemented with sodium lactate (10 mM). Cells were grown to stationary phase, harvested by centrifugation, and washed once with phosphate buffer. Cells were then resuspended with 50 ml of medium (without supplements), and butane gas (7 ml) was added to the gas phase as overpressure. After 7-h incubation at 30°C with constant shaking, butane-induced cells and lactate-grown cells were harvested and assayed for butane degradation activity. Cells of CF8 and M. vaccae were grown in the media (200 ml) described above without butane but supplemented with sodium lactate (5 mM) for CF8 or 0.01% (wt/vol) yeast extract and glucose (5 mM) for M. vaccae in 700-ml bottles sealed with butyl rubber-lined screw caps. Cells were grown to an OD₆₀₀ of 0.5 to 0.8. For lactate-grown or glucose-grown controls, 50 ml of culture was transferred into a 150-ml sterile vial and sealed with a rubber stopper and aluminum cap, and cells were continuously incubated at 30°C with constant shaking. For butane induction, 50% (vol/gas-phase vol) butane and 20% (vol/gas-phase vol) O₂ was added to the gas phase of 700-ml bottles as an overpressure and the cells were incubated at 30°C with constant shaking. Butane-induced and lactate- or glucose-grown cells were harvested after 15 h and assayed for butane degradation activity as described above. The OD₆₀₀s were around 1 to 1.4 for butane-induced cells and 0.5 to 0.8 for lactate- or glucose-grown cells.

[¹⁴C]acetylene assay. Cells of butane-grown P. butanovora, M. vaccae, and CF8 were treated with [¹⁴C]acetylene synthesized from Ba¹⁴CO₃ as described previously (27). Concentrated cell suspensions (200 µl) were incubated for 10 min at 30°C with constant shaking in 10-ml sealed vials containing phosphate buffer (800 µl), sodium butyrate (5 mM), and [¹⁴C]acetylene (1 ml [mixture of approximately 0.25% acetylene and air], approximately 1 to 2 µCi). Cells were also incubated with [¹⁴C]acetylene (1 ml) in the presence of 50% (vol/total vial vol) butane. Butane-induced and lactate- or glucose-grown cells (400 µl) were incubated for 20 min at 30°C with constant shaking in 15-ml sealed vials containing phosphate buffer (1 ml), sodium butyrate (5 mM), and [¹⁴C]acetylene (1 ml). After incubation, cells were harvested, washed twice with phosphate buffer (1 ml), and resuspended in phosphate buffer (200 or 400 µl). The cells of P. butanovora were solubilized in sodium dodecyl sulfate-polyacrylamide gel electrophoresis (SDS-PAGE) sample buffer. The cells of CF8 and M. vaccae were solubilized by using a Mini-beadbeater (Biospec Products, Inc., Bartlesville, Okla.) in the presence of SDS-PAGE sample buffer. Protein samples (50 µg) were separated on a 10% polyacrylamide gel at a constant current of 15 mA. Gels were stained with Coomassie blue and dried onto filter paper, and radioactive polypeptides were visualized by exposure on storage phosphor screens (Molecular Dynamics, Sunnyvale, Calif.) for 4 to 7 days. Densitometry was conducted with Imagequant software (Molecular Dynamics) to quantify ¹⁴C-labeling intensities.

Ammonia oxidation assay. Concentrated cell suspensions (100 µl) (approximately 0.17, 0.36, and 0.15 mg of protein in CF8, P. butanovora, and M. vaccae, respectively) were incubated at 30°C with constant shaking in 10-ml sealed serum vials containing phosphate buffer, as in the CF8 and M. vaccae growth media (900 µl), and 10 mM NH₄Cl. At selected times, cells were removed by centrifugation and supernatants were analyzed for hydroxylamine (32) and nitrite formation (23) by colorimetric assays.

Ethylene oxidation assay. Concentrated cell suspensions (100 µl) were incubated at 30°C with constant shaking in 10-ml sealed serum vials containing phosphate buffer (900 µl) and 25% (vol/total vial vol) ethylene. For acetylene pretreatment, cells were incubated in the presence of 1% (vol/total vial vol) acetylene for 10 min and purged with nitrogen gas for 2 min prior to 25% (vol/total vial vol) ethylene addition. After 30 min, a sample of gas phase (100 µl) was removed for analysis of ethylene oxide production with a gas chromatograph (Shimadzu GC-8A) equipped with a flame ionization detector and a 120- by 0.1-cm inner diameter stainless steel column packed with Porapak Q (Alltech Associates, Inc.). The gas chromatograph was run at a column temperature of 130°C and a detector temperature of 220°C.

Protein determinations. Protein content was determined by using the Biuret assay (21) after the cells were solubilized in 3 N NaOH for 30 min at 65°C. Bovine serum albumin was used as the standard.

	RESULTS

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Butane oxidation by three bacterial cultures, P. butanovora, CF8, and M. vaccae JOB5. Butane degradation rates by the resting cells of three strains of butane-grown bacteria were determined. Butane degradation rates were comparable among the three bacteria (Table 1). The reported butane degradation rate (4.9 nmol min¹ mg of protein¹) with butane-grown Nocardia TB1 (48) was much lower than those of our butane-grown bacteria. Time courses (not shown) were linear from 100 µM to about 5 µM butane. Butane oxidation rates for P. butanovora were rather variable from culture to culture and generally fell in the range of 20 to 65 nmol min¹ mg of protein¹. O₂ was required for butane degradation by all three bacteria (data not shown). We attempted to estimate K_s values (the apparent K_m observed in intact cells) for butane from time courses of butane degradation with initial butane concentrations of 10 to 20 µM (data not shown). For all three bacteria, the rate of butane degradation did not decrease until the butane concentration was 5 µM or less. These results indicated that the K_s for butane was below 5 µM for all three bacteria. A more accurate estimate could not be obtained because of the detection limit of the gas chromatograph.

1-Butanol production. During the butane degradation assays, the predicted products of butane oxidation, 1-butanol or 2-butanol, did not accumulate. In order to detect product formation, 1-butanol metabolism was partially blocked by the addition of an excess amount of the product structural analogs, 1-propanol or 1-pentanol. CF8 and P. butanovora accumulated 1-butanol in the presence of 10 or 5 mM 1-propanol, while M. vaccae accumulated 1-butanol in the presence of 10 mM 1-pentanol, when the cells were exposed to butane (10% [vol/gas-phase vol]) (Table 1). The rates of 1-butanol accumulation were less than the rates of butane consumption. However, even 10 mM of 1-propanol or 1-pentanol could only partially block the consumption of added 1-butanol (100 µM) (data not shown). Therefore, the lower rates of 1-butanol accumulation could reflect the continued consumption of some of the 1-butanol produced or the conversion of some of the butane to other products (e.g., 2-butanol). The product of the subterminal oxidation of butane, 2-butanol, was not examined in this experiment. 1-Butanol production by all three bacteria was specifically inhibited in the presence of 400 µM acetylene (1% [vol/gas-phase vol]), a known monooxygenase inhibitor. These results strongly support the presence of butane monooxygenases which oxidize butane to butanol in all three bacteria.

Inhibitor and inactivator assays. One known monooxygenase inhibitor and two inactivators were tested for their effects on butane degradation by the three strains of butane-grown bacteria. Acetylene is a mechanism-based inactivator of several monooxygenases, including sMMO, pMMO, and ammonia monooxygenase (AMO) (29, 38). Previously, it has been shown that acetylene inactivated chloroform degradation by CF8, P. butanovora, and M. vaccae (24). We have now examined the effect of acetylene on butane degradation (Table 2). To distinguish inactivation (irreversible) from inhibition (reversible), cells were preincubated in the presence of acetylene for 5 min, then the acetylene was removed by purging with air, and the cells were assayed for butane degradation activity. Compared to untreated cells, P. butanovora lost approximately 25% of its butane degradation activity after 5 min of preincubation, even in the absence of inactivators (Table 2). This loss of activity was not substantial in the case of CF8 or M. vaccae. Preincubation with 40 µM (0.1% [vol/gas-phase vol]) acetylene strongly inactivated (~80%) butane degradation activity in all three bacteria (Table 2). Prolonged preincubation time with acetylene resulted in complete inactivation (data not shown).

[¹⁴C]acetylene labeling of cellular polypeptides from P. butanovora, CF8, and M. vaccae. Our previous study showed that acetylene inactivation of butane monooxygenases in each of the three strains of butane-grown bacteria required enzyme turnover and that butane protected the enzyme from inactivation (24). These results, coupled with the results in Table 2, suggest that acetylene works as a mechanism-based inactivator for butane monooxygenase. Insights into the mechanism of acetylene inactivation of other known monooxygenases were obtained by the use of [¹⁴C]acetylene (29, 38). For example, acetylene or a product of acetylene oxidation irreversibly bound to the enzyme, thereby allowing a monooxygenase polypeptide to be identified among the cellular proteins (29, 38). Therefore, specific acetylene binding to butane monooxygenases was examined by exposing butane-grown P. butanovora, CF8, and M. vaccae to [¹⁴C]acetylene.

View larger version (113K): [in this window] [in a new window]   FIG. 1.   Incorporation of 14C from [14C]acetylene into cellular proteins of P. butanovora (lanes 1 and 2), CF8 (lanes 3 and 4), and M. vaccae (lanes 5 and 6). Butane-grown cells were incubated with [14C]acetylene (lanes 1, 3, and 5) or [14C]acetylene in the presence of 50% (vol/total vial vol) butane (lanes 2, 4, and 6). Incorporation of 14C into polypeptides was analyzed by SDS-PAGE and visualized by a phosphorimager as described in Materials and Methods. Each gel lane contains approximately 50 µg of cell extract protein.

Butane-dependent induction of butane degradation activity. Butane degradation activity was not detected for lactate-grown P. butanovora or CF8 or for glucose-grown M. vaccae. When lactate- or glucose-grown cells were exposed to butane (10% [vol/gas-phase vol]) for P. butanovora and 50% [vol/gas-phase vol] for CF8 and M. vaccae) for 7 to 15 h, induction of butane degradation activity was observed. The levels of butane degradation activity of P. butanovora after 7-h exposure to butane were 20 to 30% of those observed in butane-grown cells. After 15-h exposure to butane, butane degradation activities in CF8 and M. vaccae reached 70 to 100% of those observed in butane-grown cells.

View larger version (63K): [in this window] [in a new window]   FIG. 2.   Induction of specific polypeptides during the induction of butane degradation activity in P. butanovora (lanes 1 to 3), CF8 (lanes 4 to 6), and M. vaccae (lanes 7 to 9). (A) Coomassie blue-stained SDS-polyacrylamide gel of butane-grown cells (lanes 1, 4, and 7), butane-induced cells (lanes 2, 5, and 8), and lactate- or glucose-grown cells (lanes 3, 6, and 9). (B) Phosphorimager image of [14C]acetylene-labeled butane-grown cells (lanes 1, 4, and 7), butane-induced cells (lanes 2, 5, and 8), and lactate- or glucose-grown cells (lanes 3, 6, and 9). The apparent molecular masses of the labeled polypeptides are shown on the left of each panel.

Substrate range of butane monooxygenases. We examined three well-known substrates of other monooxygenases, methane, ammonia, and ethylene, as substrates for P. butanovora, CF8, and M. vaccae. Methane oxidation was not detected in any of the three bacteria. Additionally, P. butanovora (43) and CF8 (data not shown) could not grow with methane as a substrate. The distinction between gaseous alkane utilizers and methanotrophs extends to their ability to oxidize methane. We also examined the oxidation of ammonia by butane-grown bacteria. Both C₁-oxidizing monooxygenases can also oxidize ammonia, but ammonia oxidation has not been examined for other alkane-oxidizing bacteria. For ammonia oxidation, both the initial product of ammonia oxidation, hydroxylamine, and the product of hydroxylamine oxidation, nitrite, were measured (Table 3). All three butane-grown bacteria oxidized ammonia to some extent (Table 3). Both hydroxylamine and nitrite accumulated in CF8 incubations, while only nitrite accumulated in M. vaccae incubations. P. butanovora produced much more product than CF8 or M. vaccae. Interestingly, very little nitrite was detected in P. butanovora incubations. Addition of an exogenous electron donor, sodium butyrate, enhanced ammonia oxidation in most cases. The effect of butyrate was greater with P. butanovora than with CF8 or M. vaccae, and this is consistent with our previous result, which showed the requirement of butyrate for chloroform degradation by P. butanovora but not by CF8 or M. vaccae (24). In the presence of 10% (vol/gas-phase vol) butane, ammonia degradation was inhibited in all three strains of bacteria, suggesting that the same enzyme is capable of both butane and ammonia degradation. The involvement of a monooxygenase in ammonia oxidation was also suggested from the results that acetylene inhibited product formation (Table 3) and O₂ was required (data not shown).

	DISCUSSION

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Butane degradation by three strains of butane-grown bacteria, P. butanovora, M. vaccae JOB5, and an environmental isolate, CF8, was characterized at the physiological level. The presence of butane monooxygenases in these organisms was indicated by the following results. (i) Butane oxidation required O₂. (ii) 1-Butanol was produced as a product of butane oxidation. (iii) Butane oxidation as well as 1-butanol production was inactivated by acetylene. All three strains of bacteria oxidized butane at similar rates (Table 1) and exhibited a strong affinity for butane (K_s < 5 µM). Incubation of butane-grown P. butanovora, CF8, and M. vaccae with [¹⁴C]acetylene resulted in the covalent binding of ¹⁴C label to specific polypeptides (Fig. 1). The presence of butane protected enzyme from [¹⁴C]acetylene binding (Fig. 1). These results are consistent with acetylene acting as a mechanism-based inactivator of butane monooxygenases in all three strains of bacteria.

The substrate ranges of these butane monooxygenases apparently extend to compounds other than n-alkanes. Previous studies (8, 24, 46, 47) showed that a number of chlorinated hydrocarbons of environmental concern are substrates of butane-grown CF8 and P. butanovora and propane-grown M. vaccae. In this study, all three strains of butane-grown bacteria were shown to oxidize ammonia (Table 3); thus they are heterotrophic nitrifiers. However, the amounts and distributions of products formed discriminated among the three bacteria. CF8 and M. vaccae formed much less oxidation product from ammonia than P. butanovora. But all three strains of butane-grown bacteria oxidized more ammonia than other heterotrophic nitrifiers. For instance, Pseudomonas putida oxidized the ammonium (4.6 mM) to 1.7 µM nitrite in 24 h during heterotrophic growth on -aminobutyrate (final OD₆₈₀, 1.4) (13). CF8 and M. vaccae oxidized ammonia to nitrite. Perhaps, these organisms possess hydroxylamine oxidoreductase which catalyzes the oxidation of hydroxylamine to nitrite. Hydroxylamine oxidoreductase in autotrophic nitrifiers has been well characterized (2). All three strains of butane-grown bacteria also oxidized ethylene to ethylene oxide. Ethylene oxidation by propane-grown bacteria has been reported (26). Various propane-grown bacteria showed ethylene oxidation rates ranging from 0.1 to 2.6 µmol h¹ mg of protein¹. A nitrifying bacterium, Nitrosomonas europaea, also oxidized ethylene and produced ethylene oxide at a rate of 1.54 µmol h¹ mg of protein¹ in the presence of 10 mM NH₄⁺ (28). Methane was not oxidized by any of the strains of butane-grown bacteria. These results showed similarities in the alternative substrate ranges of the butane monooxygenases among the three strains of bacteria.

Further examination of butane oxidation in response to ethylene, a known monooxygenase inactivator, and ATU, a known monooxygenase inhibitor, showed a remarkable diversity among the three strains of butane-grown bacteria. The effects of these two compounds allowed us to discriminate among the butane monooxygenases in these organisms. Ethylene is known to irreversibly inactivate monooxygenases containing a P-450 prosthetic group by alkylating the heme group (35). Ethylene strongly inactivated butane oxidation by P. butanovora but not by CF8 or M. vaccae. Further examination showed that the oxidation product of ethylene, ethylene oxide, inactivated butane oxidation by P. butanovora. Although we did not rule out the possibility that ethylene itself was also an inactivator, the fact that high concentrations of ethylene protected cells from ethylene oxide inactivation suggested that ethylene oxide, not ethylene, was the inactivator.

The inhibitory effect of ATU provides further discrimination among the three butane-grown bacteria. ATU is a copper-selective chelator and reversibly inhibits copper-containing monooxygenases, such as pMMO and AMO (6). ATU strongly inhibited butane degradation by CF8. The low concentration of ATU (200 µM) showed complete inhibition, which was consistent with the results observed with pMMO and AMO. The results from [¹⁴C]acetylene labeling assays also support the similarity among butane monooxygenases of CF8, pMMO, and AMO. Active preparations of pMMO from Methylococcus capsulatus (Bath) consisted of three major polypeptides (47, 27, and 25 kDa), and the 27-kDa polypeptide was identified as the acetylene-binding protein (51). AMO, which shares many characteristics with pMMO, also contains an acetylene-binding protein with a molecular mass of 27 kDa (29). It is noteworthy that the [¹⁴C]acetylene-binding polypeptide in CF8 has a similar molecular mass (ca. 30 kDa [Fig. 1]). It is possible that a butane monooxygenase in CF8 is a third example of the type of copper-containing monooxygenases found in autotrophic ammonia oxidizers and methanotrophs. In contrast, butane oxidation by P. butanovora was insensitive to even a high concentration (2 mM) of ATU. Only partial inhibition was observed with M. vaccae. This weak inhibition could be explained by ineffective ATU binding to a copper site or nonspecific ATU binding to metal prosthetic groups other than copper. One possible prosthetic group for butane monooxygenase of M. vaccae could be a diiron cluster, which is widely distributed among known monooxygenases, including sMMO and alkane hydroxylase in P. oleovorans (18-20, 39).

The mechanism-based inactivator, acetylene, was used to identify specific polypeptides that most likely contain the active site of the enzyme. The three strains of butane-grown bacteria showed distinct [¹⁴C]acetylene labeling patterns (Fig. 1). The limited labeling of additional proteins could be due to nonspecific labeling by some reactive intermediates of acetylene oxidation that escaped from the enzyme active site and reacted with closely located proteins. In all three strains of bacteria, exposure of lactate- or glucose-grown cells to butane induced butane degradation activity accompanied with the induction of specific acetylene-binding polypeptides that were absent in lactate- or glucose-grown cells (Fig. 2B). There was a correlation between butane-oxidizing activity and the amount of ¹⁴C label incorporated into the specific polypeptides.

We studied butane oxidation by P. butanovora, CF8, and M. vaccae as representatives of short-chain alkane utilizers. A remarkable level of diversity was observed in butane monooxygenases among the three butane-grown bacteria. Inhibitor and inactivator profiles might imply the presence of different prosthetic groups in the butane monooxygenases among the three butane-grown bacteria. Bacterial oxygenases are known to utilize various metal ions, such as iron, copper, and manganese, as cofactors to bind dioxygen (25). The presence of diverse cofactors has been found in monooxygenases, including a diiron cluster in alkane hydroxylase from P. oleovorans (39) and sMMO from methanotrophs (18-20), both iron and copper in pMMO from M. capsulatus (Bath) (51), and cytochrome P-450 in n-octane hydroxylase in Corynebacterium sp. strain 7E1C (10). The result from [¹⁴C]acetylene labeling also supports the diversity among the three bacteria we have studied. Further characterization of these butane monooxygenases at the biochemical and genetic levels will be necessary to elaborate on the differences and similarities among these three enzymes.