AN ABSTRACT OF THE THESIS OF David M. Doughty for the degree of Master of Science in Microbiology presented on January 6, 2003. Title: Metabolism of Dichioroethenes by the Butaneoxidizing Bacterium 'Pseudomonas butanovora'. Redacted for privacy Abstract approved:__ Peter J. Bottomlèy Reductive dechlorination of chlorinated ethenes is dependent upon suitable substrates promoting microbial activity and creating anaerobic conditions. At the periphery of active reductive dechiorinating zones combinations of lesser chlorinated ethenes should exist along with end products of the anaerobic metabolism that is driving reductive dechlorination. Potential end-products of anaerobic metabolism were investigated for their ability to stimulate oxidative cometabolism of dichloro ethenes (DCEs) by the butane-degrading bacterium, Pseudomonas butanovora. Organic acids that supported butane-monooxygenase (BMO) activity were acetate, propionate, lactate, and butyrate. Lactate consistently supported and sustained greater rates of cooxidation than did the other organic acids. When propane replaced butane as the growth substrate, lactate remained the superior electron donor, while the ability of butyrate and acetate to support BMO activity decreased. In contrast, propionate-supported cooxidation was only observed in propane-grown cells. Lactate supported the degradation of 1,2-trans dichioroethylene (1,2-trans DCE), 1,2-cis dichloroethylene (1,2-cis DCE) and 1,1-dichioroethylene (1,1-DCE) in butane-grown P. butanovora. 78 nmoles (25 tM) of 1,2-cis DCE were completely degraded by butane-grown P. butanovora. In contrast, smaller amounts of 1,1 -DCE and 1,2-trans DCE were degraded over the twenty minuet time course. Decreasing rates of cooxidation over time were observed for of all three DCEs, and 50% of BMO activity was irreversibly lost after 15 mm, 6 mm, and 0.5 mm exposures to 1,2-cis DCE, 1,2 trans-DCE, and 1,1-DCE respectively. Cell viability decreased by over 90, 95, and 99.95% during the transformation of 25 nmoles/mg protein of 1,2-cis DCE, 1,2-trans DCE and 1,1-DCE. These results indicate that cellular viability was more sensitive to cooxidation of 1 ,2-cis DCE and 1,2-trans DCE than was BMO. 1,2-cis DCE and 1,2-trans DCE induced BMO activity to 25 and 45% of the butane control, respectively. Induction by 1,2-trans DCE was observed at a threshold of about 20 M and higher concentrations did not increase BMO activity. Fusion of lacZ to the BMO catabolic promoter, with consequent knock out of BMO activity, provided the opportunity to assess substrate induction without the confounding effects of enzyme inactivation and product induction. While BMO substrates, butane, I ,2-cis DCE, and ethylene, were unable to induce lacZ activity the BMO products, 1 -butanol, and ethylene oxide, effectively induced lac Z activity. 1,2-trans DCE was unique among the BMO substrates tested in it's ability to induce expression of lacZ, 2-fold above background, in the reporter strain. A wide range of concentrations induced lacZ activities (10 to 100 SM), and low levels of 1,2-trans DCE achieved high levels of induction after 4 hrs. However, lac Z activities were limited to an induction of about four-fold above background and this limit allowed lower concentrations of 1,2-trans DCE to eventually produce equal levels of beta-galactosidease. These data provide proofof-concept that BMO-dependent cometabolism can occur independently of butane as an inducer and electron donor for BMO gene expression and activity. ©Copyright by David M. Doughty January 6, 2004 All Rights Reserved Metabolism of Dichioroethenes by the Butane-oxidizing Bacterium 'Pseudomonas butanovora'. by David M. Doughty A THESIS submitted to Oregon State University in partial fulfillment of the requirements for the degree of Master of Science Presented January 6, 2004 Commencement June, 2004 Master of Science thesis of David M. Doughty presented on January 6, 2003. APPROVED: Redacted for privacy Major Professor, Microbiology Redacted for privacy Head of the Department of$obiology Redacted for privacy Dean of th Ilri6uate School I understand that my thesis will become part of a permanent collection of Oregon State University libraries. My signature below authorizes release of my thesis to any reader upon request. Redacted for privacy DaviMt1hty, Author ACKNOWLEDGEMENTS I would like to express my sincere gratitude to Dr. Peter J. Bottomley. Without your experience and patience I would not have been able to complete my project. The questions you have asked have directed my work and development as a scientist. I have appreciated the opportunity to work so closely with Dr. Daniel Arp and his lab. Thank you for your commitment. It has been a pleasure working with you. A special thanks to Dr. Luis Sayavedra-Soto who selflessly provided his time and assistance throughout this degree. I have enjoyed our discussions of science and appreciate your encouragement in my professional pursuits. To the rest of the Arp and Bottomley labs, I have enjoyed working with all of you. Thank you for the creative and interesting discussions that we have had. Finally, I would like to thank my parents Michael and Lillian Doughty for their encouragement and support. CONTRIBUTION OF AUTHORS Peter J. Bottomley, Daniel J. Arp aided in the experimental designs and the creation of this manuscript. Luis A. Sayavedra-Soto provided bacterial strains and aided in the design of experiments. All experiments and analysis were conducted in the laboratories of Dr. Arp or Dr. Bottomley at Oregon State University. TABLE OF CONTENTS Chapter 1. ThTRODUCTION ................................................ 1 1.1. DCEs-industrial use, primary contaminants, and daughter products of reductive dechlorination ................. 1.1.1. Industrial use of chlorinated ethenes ..................... 1.1.2. Primary ground water pollution by DCEs ............... 1.1.3. Reductive dechlorination and the creation of DCEs ......................................................... 1.2. Cooxidation ......................................................... 1.2.1. Electron donation, monooxygenase induction and the competition of natural substrates in cooxidation .................................................. 1.2.2. Electron donation by alternative substrates ............. 1.2.3. Induction of non-specific oxygenases by chlorinated ethenes ....................................................... 1.3. Alkane oxidizing bacteria and multicomponent oxygenases .......................................................... 1 1 3 3 3 4 5 6 1.3.1. Induction of butane metabolism in P. butanovora ................................................... 8 1.3.2. Inductions of pathways involved in the metabolism of alternative electron donors .................................. 8 1.4. Research objectives ..................................................... 9 Chapter 2. MATERIALS AND METHODS ............................ 10 2.1. Bacterial strains and growth conditions ......................... 10 2.2. Ethene oxidation assay ............................................. 11 2.3. Degradation of chlorinated ethenes .............................. 11 TABLE OF CONTENTS (CONTINUED) Page 2.4. Irreversible effects of DCE cooxidation on BMO ............ 12 2.5. Inhibition of 02 uptake by DCEs ................................ 13 2.6. Determination of cell viability after cooxidation .............. 14 2.7. Induction of BMO by chlorinated ethenes ..................... 14 2.8. Induction of the LacZ reporter strain ........................... 15 2.9. Analytical and other methods .................................... 16 Chapter 3. RESULTS ....................................................... 17 3.1. Reductant enhanced cooxidation and metabolic fitness in P. butanovora ...................................................... 17 3.2. Characteristics of chlorinated ethene degradation in P. butanovora .......................................................... 22 3.3. Induction of BMO activity in P. butanovora by chlorinated ethenes ................................................ 32 Chapter 4. DISCUSSION................................................... 38 BIBLIOGRAPHY ............................................................ 45 LIST OF FIGURES Figure 3.1. 3.2. Page Concentration effects of electron donor on the cooxidation of ethene by butane-grown P. butanovora ........................ Effect of the alternative electron donors, 5mM butyrate or lactate, on the consumption of 1 ,2-cis DCE by butane-grown P. butanovora 3.3. 3.4. 3.5. 3.6. 3.7. 3.8. 19 ............................................................. 20 Time course of 1,2-cis DCE, 1,2-trans DCE, and 1,1-DCE consumption by butane-grown P. butanovora .................. 25 Time course of the irreversible loss of BMO activity during the consumption of 1,2-cis DCE, 1,2-trans DCE, and 1,1 DCE by butane-grown P. butanovora ........................... 27 Time course of lactate-dependent oxygen consumption by butane-grown P. butanovora during the cooxidation of 1,2cis DCE, 1,2-trans DCE, and 1,1-DCE ........................... 29 The effect of equimolar (25nmoles/mg protein) consumption of 1 ,2-cis DCE, 1,2-trans DCE, 1,1 DCE on cell viability in butane-grown P. butanovora ...................................... 31 Induction of BMO activity in lactate-grown cells of P. butanovora in response to exposure to butane or varying concentrations of 1,2-trans DCE .................................. 34 Induction of lac Z in the reporter strain by varying concentrations ofi -butanol, 1,2-trans DCE, 1 ,2-cis DCE, and1,1-DCE ......................................................... 35 LIST OF TABLES Table 3.1 3.2. Page Reduc ant enhanced oxidation of ethene to ethene oxide by butane and propane-grown P. butanovora................... 21 Induction of BMO activity in P. butanovora and lacZ activity in the lacZ-BMO fusion in response to various substrates and products of BMO ................................................ 37 Metabolism of Dichioroethenes by the Butane-oxidizing Bacterium 'Pseudomonas butanovora'. Chapter 1. INTRODUCTION 1.1. DCEs - industrial use, primary contaminants, and daughter products of reductive dechlorination 1.1.1. Industrial use of chlorinated ethenes Chlorinated ethenes are used in a wide range of industrial processes and in the creation of consumer goods. Vinyl chloride (VC), 1,1 dichloroethene (1,1 DCE), trichioroethene (TCE) , and tetrachloroethene (PCE) are commonly used chlorinated ethenes. TCE and PCE are used as organic solvents for the degreasing of metal machinery, and as dry cleaning fluids. Vinyl chloride and 1,1 -DCE will undergo polymerization to polyvinyl chloride and polyvinylidene chloride respectively, and are used in furniture coverings and food wraps. Mixing these compounds with each other or TCE will cause different chain linking in the polymer and produce plastics with different properties. Industrial demands for TCE in the United States alone topped 171 million pounds in 1998 and continues to grow by 7-9% a year (Agency for Toxic Substances and Disease Registry 2003). 2 1.1.2 Primary pround water pollution by DCEs Chlorinated ethenes are suspected carcinogens and known neuro depressants (Agency for Toxic Substances and Disease Registry, 1995). The EPA has regulated the concentration of chlorinated ethenes in drinking water since 1994 (Agency for Toxic Substances and Disease Registry 2003). Prior to their regulation, industrial wastes containing high levels of chlorinated ethenes were disposed of haphazardly. These disposal practices made chlorinated ethenes common ground water contaminants in urban areas. EPA standards for safe drinking water limit the concentration of chlorinated ethenes to 2ppb, 5ppb, and 7ppb for vinyl chloride, 1,1-DCE, and TCE respectively; EPA standards for 1,2-cis DCE and 1,2- trans DCE are about ten-fold higher (Agency for Toxic Substances and Disease Registry, 1997). 1.1.3. Reductive dechlorination and the creation of DCEs Many different organisms are known to metabolize and cometabolize chlorinated ethenes (Chauhan et al. 1998; Coleman et al. 2002 a and b; Major et al. 2002; Sullivan et al. 1998; Verce 2001; Verce 2002; Yeager et al. 2001). Some organisms are able to use chlorinated ethenes as terminal electron acceptors during growth under anaerobic conditions. This ability results in stepwise reductive dechlorination according to the following pathway: PCE, TCE, DCEs, VC, and ethene. The degradation of chlorinated ethenes becomes stereochemically and thermodynamically restricted resulting in buildup of lesser-chlorinated ethenes 3 (Semprini, 1995). The persistence of DCE and VC leads to their eventual diffusion away from the contaminated site. As a result, low concentrations of DCE and VC may persist in the groundwater adjacent to sites experiencing reductive dechlorination of more highly chlorinated ethenes (Freedman et al. 2001; Kastner 1991). 1.2. Cooxidation Aerobic cooxidation occurs when a non-specific oxygenase enzyme converts chlorinated ethenes into epoxides or alcohols. Several characteristics of cooxidation limit this process. First, enzymatic attack by oxygenases on chlorinated ethenes drains the reductant needed for other cellular processes. Second enzyme inactivation brought about by successful cooxidation can limit the amount of chlorinated ethenes degraded. As a result the sustained cooxidation of chlorinated ethenes requires the presence of an appropriate substrate to induce monooxygenase activity and requires a suitable electron donor to support monooxygenase activity (Arp et al. 2001). 1.2.1. Electron donation, monooxygenase induction and competition of natural substrates in cooxidation Induction of non-specific oxygenases required for the cooxidation of DCEs usually involves the natural substrate. Under these conditions, the natural substrate also serves as the growth substrate, and indirectly as the electron donor for chlorinated ethene cooxidation. However, the metabolism of natural substrates supplied to enhance cooxidation of chlorinated ethenes competes with the cooxidative process. Kim et al. (2002a) showed that the degradation of 1,2-cis DCE and 1,1 -DCE by a butane-grown mixed culture proceeded more slowly in the presence of butane because the transformation of the growth substrate limited the allocation of reductant to the cooxidation reaction (Alvarez-Cohen and McCarty 1991 a and b; Kim et al. a and b). Under these conditions the transformation yield, the ratio of electrons allocated to cooxidation versus other cellular processes, may be low. 1.2.2. Electron donation by alternative substrates Conceptually, competition between natural substrates and cosubstrates may be averted by supplying cells with an alternative electron donor. The transformation yield in these systems may be very high as long as cosubstrate availability and enzyme activity are not limiting. This concept has been highlighted in methanotrophic systems where formate, a downstream intermediate of methane metabolism, was used to support oxidative cometabolism (Alvarez- Cohen and McCarty 1991a; Arp et al. 2001). In these systems, alternative electron donors allowed kinetic and cytotoxic effects to be studied without the confounding effects of inhibition by the natural substrate. Exogenous electron donors may lead to faster initial rates of degradation, however, enzyme activity will decline because of either protein turnover, or inhibition of the enzyme by the cosubstrate. 1.2.3. Induction of non-specific oxygenases by chlorinated ethenes Induction of non-specific monooxygenase enzymes by their cosubstrates has been reported in a variety of organisms (Ensign 1996; Ryoo et al. 2001; Yeager et al. In Press 2004). Chlorinated ethene induction of a monooxygenase circumvents the need for a "natural" substrate, and, conceptually, relieves the competition between the natural substrate and the cosubstrate. This permits a greater percentage of reductant to be allocated to chlorinated ethene cooxidation and supports a higher transformation yield. Enzyme induction by chlorinated ethenes has been most extensively studied in toluene-oxidizing bacteria. A 3-fold induction of monooxygenase activity was observed following exposure of Pseudomonas stutzeri OXI to 100 pM TCE or PCE. Toluene monooxygenase activity was not observed following exposure to other chlorinated ethenes including DCEs. Transfer of the inducible monooxygenase system to a heterologous host produced an inducible monooxygenase system that responded to the natural substrate, but did not respond to PCE or TCE. It was concluded that factors outside the previously known genes and gene products were required for induction by TCE or PCE relative to toluene (Ryoo et al. 2001). Four tolueneoxidizing bacteria were evaluated for the range of electron donors able to support the degradation of TCE when TCE was also used as the inducing compound. The ability of Pseudomonas mendocina KR1, Pseudomonasputida Fl, and Raistonia pickettii PKOI to degrade TCE depended on the growth-supporting substrate. Differences in the ability of electron donors to support cooxidation were likely due to catabolite repression or sensitivity to the cooxidative process. Various carbon sources supported different rates of degradation and growth, leading to speculation that the allocation of reductant varied by organism and by electron donor. P. mendocina KR1 degraded TCE in the presence of lactate, glucose, fructose, and glutamate, but not in the presence of acetate or Luria-Bertani broth. These results showed P. mendocina KR1 to be the most versatile in its ability to use growthsupporting substrates as electron donors for the cooxidation of TCE (Yeager et al. In Press, 2004). 1.3. Alkane oxidizing bacteria and multicomponent oxygenases Alkane oxidizing bacteria may be grouped empirically according to the chain length of the alkanes used for growth. Methanotrophic bacteria comprise the first group, and two representative organisms, Methylococcus capsulatus Bath and Methylosinus trichosporium OB3b, have been the subject of intense study (Stafford et al. 2003; Csaki 2003; Coufal et al. 2000). Particulate methane monooxygenase (pMMO) is a membrane-bound enzyme capable of converting methane to methanol. Under conditions of copper limitation methanotrophs may express a soluble cytoplasmic methane monooxygenase (sMMO). pMMO and sMMO are representative of two families of non-specific oxygenases that have been adapted by organisms for growth on a variety of substrates and have been exploited for bioremediation of chlorinated ethenes (Sullivan et al. 1998). Alkanes 7 of C2 to C4 in chain length are growth substrates for another group of alkane oxidizing bacteria (Hamamura et al. 1999). Bacteria in this group use both sMMO and pMMO homologs to oxidize alkanes. P. butanovora is a gram negative representative of this group and the subject of study in this thesis. At the other extreme, alkane oxidizing bacteria also exist that grow on liquid alkanes of chain lengths C5-C 12. Pseudomonas putida GPo 1 (formerly Pseudomonas oleovorans) relies on a membrane bound enzyme analogous to pMMO and has been studied as a model system for the expression and regulation of alkane-oxidizing genes (Dinamarca et al. 2002). Sluis et al. (2002) sequenced the BMO gene cluster and compared the deduced amino acid sequences with other multi-component monooxygenases. BMO subunits shared as much as 64% identity with sMMO. The high sequence identity suggests that BMO is a member of a family of non-specific oxygenases called three component hydroxylases. The substrate binding pocket and active site are located on the hydroxylase subunit (Coufal et al. 2000), while the regulatory subunit is associated with substrate sensing and regio-specificity of hydroxylation (Astier et al. 2003). Both subunits are conserved features of this family of oxygenase enzymes. Despite similarities in sequence between sMMO and BMO, methane oxidation and the production of 2-butanol during butane oxidation are characteristics of sMMO not shared with BMO (Sluis et al. 2002). These results suggest that substrate range of BMO is more restricted than for sMMO. The reflection of these trends in the kinetics of cooxidation of the three DCE isomers will be discussed later in this thesis. 1.3.1. Induction of butane metabolism in P. Pseudomonas butanovora butanovora is able to use butane as the sole source of carbon and energy necessary for growth. Although lactate or citrate-grown P. butanovora cultures do not consume butane, butane consumption may be induced by butane (Sayavedra-Soto et al. 2001). Exposure of a BMO-minus mutant to butane, however, did not stimulate the consumption of 1-butanol, a down-stream intermediate in butane metabolism. These results indicate that the enzymes involved in the downstream oxidation of butane are regulated by mechanisms different from the BMO gene cluster (Sayavedra-Soto et al. 2001). 1.3.2. Induction of pathways involved in the metabolism of alternative electron donors Inducible metabolic pathways will influence the sources of reductant that may be used to drive monooxygenase activity. Two inducible alcohol dehydrogenases expressed during growth on butane were determined to be controlled by separate regulatory mechanisms (Vangnai et al. 2001; Vangnai et al. 2002 a and b) The first alcohol dehydrogenase was expressed in response to 1butanol or butane, the second alcohol dehydrogenase was expressed in response to butane or lactate. The regulation of other metabolic pathways in P. have not been elucidated. butanovora 1.4. Research objectives TCE and DCEs are some of the most common ground water pollutants in the United States. Reductive dechlorination of TCE and PCE has enjoyed considerable popularity because it is a sustainable and growth supporting process (Maymo-Gatell et al. 2001; Beeman and Bleckman 2002; Major et al. 2002). However, the partially dechlorinated end products of reductive dechlorination can persist as toxic contaminants of ground water. Successful reductive dechlorination depends on intense microbial metabolism that creates anaerobic conditions, which may result in the formation of organic acids and alcohols as metabolic end products (Kastner 1991). The objectives of the current work were to determine the extent that aerobic cooxidation may be supported by putative fermentative end products of anaerobic processes, and to examine the range of chlorinated aliphatics that induce BMO in P. butanovora. '[C Chapter 2. MATERIALS AND METHODS 2.1. Bacterial strains and growth conditions P. butanovora liquid cultures were grown in 750 ml flasks that were sealed with butyl rubber stoppers and contained 200 ml of liquid medium. Flasks were incubated at 300 C with constant circular shaking (180 rpm) for two days. Butane and propane gas (99% Airgas Randor, Penn.), were sterilized by passing through a 0.2 jm filter. When butane or propane served as the growth substrate, cultures were supplied with an overpressure of 7% volume! total volume (or 10% headspace) of the gas. When organic acids served as the carbon source for growth, a concentration of 10 mM was used. Minimal media used during growth on either alkanes or organic acids consisted of, per liter, 2.7 g, (NH4)2HPO4; 4.3 g, Na2HPO4; 4.2 g, KH2PO4; 0.5 g, MgSO4*7H20; 0.06 g, CaC12*2H20; and lml trace element solution (Wiegant and de Bont, 1980) and adjusted to pH 7.1. Cells were sedimented by centrifugation (10 mm at 6000 rpm and 10°C) after cultures reached early stationary phase, and washed three times in 50 mM phosphate buffer (as described for the media except potassium and sodium phosphate concentrations were adjusted to compensate for the omission of (NH4)2HPO4). Harvested cells, kept as a concentrated cell suspension on ice, retained ethene-dependent ethene oxide production for greater than 3 hours without observable loss in activity. Fresh cells were harvested daily or when needed. 11 2.2. Ethene oxidation assay Ethene dependent ethene oxide production served as the standard measure of BMO activity (Sayavedra-Soto et al. 2001). Vials (10 ml) sealed with butyl rubber stoppers and aluminum crimp caps served as the reaction chamber for this assay. Vials contained 1 ml of whole cell suspensions (no more than 0.35 mg of cellular protein), the specified electron donor, and 20% (v/v) ethylene gas was added as over pressure to start the assay (Hamamura et al. 1999). Vials were agitated (150 rpm) at 300 C in a covered water-bath shaker. Ethene oxide formation was followed by gas chromatography with a Shimadzu GC-8A equipped with a flame ionization detector and a 120 cm Porapak Q column (Ailtech Associates, Inc.). The colunm temperature was set at 120° C and the injector and detector were maintained at 200 °C as previously described (Hamamura et al. 1999). Samples (100 jtl) of the headspace were taken with a gas tight syringe at the time intervals of 0, 2.5, 5, and 7.5 mm. Assays that determined BMO activity were limited to less than 10 mm because the product ethene oxide has been associated with BMO inactivation. 2.3. Degradation of chlorinated ethenes The degradation of chlorinated ethenes was followed by measuring their disappearance from the headspaces by gas chromatography. Abiotic controls, which did not receive P. butanovora, and butane-grown P. butanovora cells pretreated with acetylene, a mechanism based inhibitor of BMO (Hamamura et al. 12 1997), were used to ensure that the observed disappearance of the chlorinated ethene was due to the activity of the BMO enzyme. Vials (10 ml) were prepared containing phosphate buffer (900 p1) and the specified electron donor. Aliquots of a DCE saturated solution were injected into the vials sealed with Teflon-lined butyl rubber stoppers and allowed to equilibrate by shaking at 150 rpm and 30° C for 30 mm prior to the start of the assay. Assays were initiated by the injection of 100 /Ll of concentrated cell suspension. Protein concentration in the cell suspensions were determined using the biuret assay (Gornall et al. 1949) and usually ranged from 0.7 to 1 mg protein per vial. 2.4. Irreversible effects of BCE cooxidation on BMO Vials were prepared as described above. Accurate assessment of timedependent irreversible inactivation required the prompt interruption of the cooxidation reaction. To accomplish this, butane was flushed into the headspace of the vial. Conceptually this prevented the continued degradation of the DCE during the washing procedure by purging oxygen and DCE out of the vial while providing the natural substrate to compete for the BMO active site. Two 60 ml syringes were used, the first syringe was kept empty with the plunger suppressed, and the second syringe was filled with butane. Both syringes were inserted into the vial and pulling back the plunger of the empty syringe pulled the butane from the second syringe through the vial. Cells were then washed three times by microcentrifuge, resuspended in phosphate buffer and tested for residual BMO 13 activity using the ethene oxidation assay. Control vials that did not receive a chloroethene were also flushed with butane. 2.5. Inhibition of 02 uptake by DCEs Lactate-dependent 02 uptake was followed using a Clark-style 02 electrode with glass reaction vial equipped with an YSI Model 5300 Biological Oxygen Monitor (Yellow Springs Co., Yellow Springs, OH). Temperature of the reaction chamber was maintained at 30° C by a circulating water jacket. Phosphate buffer (1.75 ml, 50mM) was allowed to equilibrate with air for 5 mm before the start of each assay, and the reaction chamber was washed 20 times with water and twice with phosphate buffer between assays to remove residual carbon sources and other contaminants. The reaction chamber was capped, and additions were made by injection in the following order: butane-grown P. butanovora cells (0.2 mg protein), lactate (2mM in electrode chamber), and the indicated cosubstrate (25 M in electrode chamber). This order of addition allowed for the sequential determination of abiotic 02 consumption, resting cell 02 consumption, lactate dependent 02 consumption, and the effects of the cosubstrate. Control reactions received the same treatments except cells were first treated with acetylene to inactivate BMO. 14 2.6. Determination of cell viability after cooxidation Cell viability after treatment with chlorinated ethenes was determined by dilution plating, on R2A agar, pH 7.2 (Becton, Dickerson and Company, Sparks MD). Cells were treated as described for the degradation of chlorinated ethenes, except, a sterile 0.5 ml microfuge tube was inserted into the vials to serve as a reservoir for the nonsterile DCEs. DCE solutions were injected into the open end of the microcentrifuge tube and allowed to equilibrate with the phosphate buffer outside of the tube. Assays were initiated by injecting cells, and incubated with constant shaking for 20 mm. Controls included acetylene-treated cells to inactivate BMO, and control cells that did not receive DCE. 2.7. Induction of BMO by chlorinated ethenes Cells were grown in 10 mM lactate and the minimal medium described above. Induction vials received aliquots of the indicated compounds and were allowed to reach equilibrium by circular shaking at 30° C for 30 mm prior to the start of the experiment. Uninduced cells were resuspended in fresh ammonium phosphate buffer plus minimal medium and were aliquoted into 10 ml vials with 900 /Ll of growth media plus ammonium phosphate buffer, sealed with Teflon coated butyl rubber stoppers and aluminum crimp caps. Unless otherwise indicated, all inductions were 4 h in length, and included positive butane and negative buffer controls. After 4 h, cells were harvested in a microcentriflige and tested for BMO activity using the ethene oxidation assay described above. 15 2.8. Induction of the LacZ reporter strain Dr. Sayavedra-Soto provided a reporter strain with a bicistronic expression system in which kanamycin resistance was constitutive and the BMO catabolic promoter controlled lacZ expression. The lacZ fusion provided multiple in-frame transcriptional stop codons before the beginning of the BMO structural genes that effectively eliminated BMO activity. The reporter strain was grown on citrate in the same growth medium and buffer as the wild type cells except that kanamycin sulfate (1 jzglml) was added to the medium to maintain the insert containing the j3- galactosidase gene. Inductions were performed in 1 OmI vials with Imi of the reporter strain culture diluted with growth media to an OD600 of 0.3. All vials were sealed with butyl rubber stoppers and aluminum crimp caps. Inductions were 2, 4, or 6 hours in length and were initiated by the injection of cells. j3galactosidase activity was determined by adding 2 jil SDS (10%), 2 jil 3mercaptoethanol, 4 jig ortho-nitrophenyl j3-D-galactopyranoside (ONPG), and a drop of chloroform are expressed in Miller units (Miller 1972). /3-galactosidase assays were incubated at 36°C and stopped by the addition of 200 jil 5% calcium carbonate. All activities were calculated using the following equation to compensate differences in the duration of fl-galactosidase assays and the number of cells! ml that were assayed. The variables are, OD 420 ONPG absorption; OD 600 the wavelength of the cell density during induction; OD turbidity after cell lysis; and time is in hours (Miller 1972). 540 is the 16 1 = Miller Units OOD420 -1.75(OD54 L 2.9. Analytical and other methods Analytical/HPLC grade PCE, TCE, 1,2-trans DCE, 1,2-cis DCE, 1,1-DCE were acquired from Sigma and Aldrich (St. Louis, Mo.). PCE, TCE, 1 ,2-cis DCE, 1,2-trans DCE, and 1,1 -DCE saturated solutions were prepared by agitating two phase solutions (aqueous/chlorinated ethene) for 24 h with constant circular shaking. The saturated aqueous phase was used to aliquot chlorinated ethenes into the reaction vials. Concentrations of chlorinated ethenes in the liquid phase of reaction vials were assumed to follow the unitless Henry's constant (Hc) displayed in equation 1 (Gossett 1987) with volume (V) in liters and concentration (C) in molarity. The unsaturated DCE solutions were created based on calculation given in equation 2. Equation 1: CI Cg= HC Equation 2: Moles VICI+ V9C9 Moles C9 HcVg+Vi 17 Chapter 3. RESULTS 3.1. Reductant enhanced cooxidation and metabolic fitness in P. butanovora. An earlier report indicated that the cooxidation of 1 ,2-cis DCE by butane- grown P. butanovora was dependent upon exogenous reductants, but did not evaluate differential effects of alternative electron donors on oxidative cometabolism (Hamamura et al. 1997). Cooxidation of 1,2-cis DCE by butanegrown P. butanovora was enhanced to different extents by 5mM lactate or butyrate. The cooxidation of 1,2-cis DCE was enhanced less by butyrate than by lactate in butane-grown cells (figure 3.2), and these differences became more exaggerated over time (figure 3.2). For example, 10 to 15 nmoles of 1,2-cis DCE were degraded in 20 mm. when butane-grown cells were supplied butyrate. In contrast, > 40 nmoles of 1 ,2-cis DCE were degraded over the same time interval, when cells were provided with the same concentration of lactate. The electron donors, lactate and butyrate, were tested across a concentration range from 2 to 10 mM (figure 3.1). The differences between the two compounds in supporting ethene dependent ethene oxide production over the ten mm assay was independent of concentration. Evidence was obtained for differences among the pathways responsible for allocating reductant to BMO from different electron donors. In butane-grown cells, acetate, lactate, and butyrate enhanced the rate of ethylene cooxidation, from an endogenous rate of 3.6 nmol/mmn*mg protein' to 17, 20, and 13 nmol/min*mg EI protein', respectively (Table 3.1). The same organic acids were tested for their ability to enhance ethene dependent ethene oxide production in cells grown on propane. The cooxidation of ethene by propane-grown cells was enhanced from an endogenous rate of 1.5 nmol/min*mg protein' to 7.8, 17.2, 8.2, and 5.4 nmol/min*mg protein1 by acetate, lactate, propionate, and butyrate, respectively (Table 3.1). These data clearly illustrate that lactate supported similar rates of cooxidation in both types of cells. In contrast, specific differences in the ability of the other organic acids to support ethene cooxidation were observed between butane and propane-grown cells. Propionate-supported cooxidation was observed to be 5.5 times greater than the background in propane-grown cells, but did not support cooxidation above the background rate in butane-grown cells. Thus, equal concentrations of different organic acids produced unequal rates of cooxidation, and for several organic acids these trends were affected by the alkane used as a growth substrate. In contrast, lactate-supported cooxidation displayed consistent rates of activity regardless of which alkane the cells were grown on. 19 20 215 p 10 - o E >1 5 Butyrate (mM) Lactate (mM) Figure 3.1. Concentration effects of electron donor on the cooxidation of ethene by butane-grown P. butanovora. Paired bars represent different replicates performed with the same culture. 25 C) a. 05 E V S.-. C) VlS 0) C) w C-) 010 U) 9 c.l U) C) E 0 0 tolO mm. 10 to 20 mm. Figure 3.2. Effect of the alternative electron donors, 5mM butyrate (black) or lactate (gray), on the consumption of 1 ,2-cis DCE by butane-grown P. butanovora. The Y-axis depicts the amount of 1 ,2-cis DCE degraded within the two selected time intervals labeled on the X-axis. 21 TABLE 3.1. Reducant enhanced oxidation of ethene to ethene oxide by butane and propane-grown P. butanovora. Reductant (5mM) Ethene oxide produced (nmol/min*mg of protein') (Values in parentheses represent fold-increase above background) Butane-grown Buffer Formate Acetate Propionate Lactate Butyrate 3.6 0.7 17.0 3.4 20.1 13.2 Propane-grown 1.5 0 (4.7) (1.0) (5.9) (3.7) 7.8 8.2 17.2 5.4 * Each reaction mixture contained ethylene (25% vol/vol) and the indicated reductant source. (5.2) (5.5) (11.5) (3.6) 22 3.2. Characteristics of chlorinated ethene degradation in P. butanovora. Butane-grown P. butanovora consumed 1,2-cis DCE 1,1-DCE and 1,2trans DCE (Figure 3.3). Lactate (5mM)-supported cooxidation proceeded at different rates for each of the DCE isomers. The rate of degradation of 1,2-cis DCE and 1,1 -DCE and within 45 mm the degradation of each compound had ceased. Reversible inhibition of oxidative cometabolism was distinguished from irreversible inactivation by resuspending cells in fresh buffer and assaying BMO activity using the ethene oxidation assay described previously. However, decreases in BMO activity due to damage to the BMO enzyme and damage to other cellular processes could not be distinguished. Time-dependent irreversible BMO inactivation was observed upon exposure of butane-grown cells to each DCE. Cooxidation of each of the DCE isomers produced different rates of irreversible inactivation. Half of BMO activity was irreversibly lost after 15 mm, 6 mm, and 0.5 mm exposures to 1,2-cis DCE, 1,2-trans DCE and 1,1-DCE, respectively (figure 3.4). 1,2-cis DCE and 1,2-trans DCE did not completely inactivate BMO. 1 ,2-cis DCE and 1,2-trans DCE were degraded in larger amounts, albeit at different rates, .than was 1,1 DCE. To compensate for these differences among the DCEs, only 25 nmoles/mg protein of each DCE was allowed to be degraded during the determination of non-specific cytotoxic effects. Two aspects of cellular health, namely, lactate-dependent 02 consumption and viability were used to evaluate these cytotoxic effects in butane-grown P. butanovora. Initial rates of 23 lactate dependent 02 consumption were consistently 69 nmoles/min*mg protein in cells either expressing active BMO or inactive BMO (acetylene treated cells). Initial rates of 02 consumption were maintained for 20 mm in cells expressing active BMO in the absence of a cosubstrate, and in acetylene treated cells after the addition of 1 ,2-cis DCE, 1,2-trans DCE and 1,1 -DCE. In contrast, the addition of DCEs increased the rate of lactate-dependent 02 consumption from 27 to 80 nmoles/min*mg protein', or within the range of monooxygenase activity found in butane-grown cells. Following the initial increase in 02 consumption, lactatedependent 02 consumption decreased rapidly after exposure to 1,1 -DCE and no lactate-dependent 02 consumption remained after 20 mm. Lactate-dependent 02 consumption also decreased rapidly during the cooxidation of 1,2-trans DCE and after 20 mm lactate-dependent 02 consumption had dropped from an initial rate of 69 to about 15 nmoles mirilmg protein. In contrast, cells that cooxidized 25 LM 1,2-cis DCE retained 30 nmoles/ mmn*mg protein' of lactate-dependent 02 consumption after 20 mm (figure 3.5). Nonetheless, when 1,2-cis DCE 1,2-trans DCF or 1,1 -DCE was provided as a cosubstrate 90, 95 and >99% of cell viability were lost, respectively. Pretreatment with acetylene eliminated DCE degradation by butane-grown P. butanovora and prevented the loss of viability of cells during exposure to 1,2-cis DCE, 1,2-trans DCE, and 1,1 DCE. The quantities of 1,2-cis DCE and 1,2-trans DCE degraded during the determination of cellular viability was less than the amount degraded in figure 3.1 by the same concentration of cells. These results for 1 ,2-cis DCE and 1,2-trans DCE are consistent with the 24 observations of Yeager et al. (2001), who described the continued cooxidation of TCE by non-viable Burkholderia cepacia G4. In contrast, this method could not identify separate thresholds for the transformation capacity of 1,1 DCE and the loss in cell viability during 1,1 DCE degradation by P. butanovora. 25 Figure 3.3. Time course of 1,2-cis DCE (A), 1,2-trans DCE (B), and 1,1-DCE (C) consumption by butane-grown P. butanovora (closed squares). Assays were performed in 10 ml vials containing 1 ml of phosphate buffer amended with 5mM lactate and 25p.M of the indicated cosubstrate. All assays were initiated with the injection of 100 jLl of concentrated cell suspension. Butane-grown cells pretreated with acetylene, a mechanism based inhibitor of BMO served as the BMO negative control (closed circles). Loss of cosubstrates from the negative control likely represents leakage of the cosubstrate from the vial. Data points represent the mean of three replicates and the error bars represent standard deviations. 26 Fig. 3.3 30 25 w 20 9 15 ('4 10 L 5 10 15 20 15 20 15 20 Mm. F', 30 w 0 25 020 (0 15 '-10 5 5 10 Mm. 30 25 20 0 '- 15 1 -10 5 0 0 5 10 Mm. 27 Figure 3.4. Time course of the irreversible loss of BMO activity during the consumption of 1 ,2-cis DCE (A), 1,2-trans DCE (B), and 1,1 DCE (C) by butanegrown P. butanovora. Incubations were performed as described for the consumption of DCEs except 50 M concentrations were used to ensure that cosubstrate was not limiting. Incubations were stopped by flushing the vials with butane at select time points, and the chlorinated ethenes were subsequently removed by washing the cells three times with phosphate buffer. Cells were then assayed for BMO activity by measuring ethene dependent ethene oxide production. Both the cooxidation of the chlorinated compounds and the ethene were driven by providing 5mM lactate as an electron donor. Butane-grown cells that did not receive cosubstrates served as BMO positive controls (closed circles) and indicated losses of BMO activity that were not attributed to the consumption of cosubstrates. Butane-grown cells that received cosubstrate are represented as closed squares. Data points are the mean of three replicates and error bars represent the standard deviations. 0 N) (Ti (J1 0 0 (71 0 Cl - 0 N) /mg protein) (TI N) (nmoles ethene oxide/mm Remaining BMO activity 0 () 0 N) cJ1 0 0 0 (TI 0 (TI - 0 N) (71 N) Remaining BMO activity (nmoles ethene oxide/mm 1mg protein) 0 () 0 N) ()i r (J1 0 0 Remaining BMO activity (TI 0 - (Ti - 0 N) /mg protein) (TI N) (nmoles ethene oxide/mm 0 () 29 Figure 3.5. Time course of lactate-dependent 02 consumption by butane-grown P. butanovora during the cooxidation of 1,2-cis DCE (A), 1,2-trans DCE (B), and 1,1 -DCE (C). Assays were performed in a Clark style 02 electrode containing 1.75 ml of air-saturated phosphate buffer. Additions to the electrode after capping, were made by injections in the following order: butane-grown cells, lactate, and cosubstrate. This allowed for the sequential determination of abiotic 02 consumption (0 nmoles/min), resting cell 02 consumption (about 40 nmole 1mm *mg protein), lactate dependent 02 consumption (69 nmoles/ min*mg protein1), and the effect of cosubstrate over the 20 mm time interval. Addition of the cosubstrate occurred immediately following the determination of lactate-dependent 02 consumption at time zero. Cooxidation-dependent effects may be discriminated from DCE-dependent effects by comparing butane-grown cells incubated with cosubstrate (squares) with the acetylene treated, BMO negative controls (closed circles). Furthermore, DCE dependent effects may be discriminated from DCE independent effects by comparison with the buffer control (open circles) that consists of butane-grown cells not supplied with cosubstrate. Ni C 01 - C CI - 0) CD Ni C C C C C CC 0Ni Lactate dependent oxygen consumption (nmoles consumed! min*mg protein1) C'j C NJ -s 01 C 01 . 0) 0) - Ni C C C C C CC CNi _& actate aepenaent oxygen consumption (nmoles consumed! min*mg protein1) Ni 0 0 0 0) 0) Ni C 0 C C 0 CC 0Ni Lactate dependent oxygen consumption (nmoles consumed! min*mg protein1) w e 32 3.3. Induction of BMO activity in P. butanovora by chlorinated ethenes. Residual BMO activity was preserved better than cell viability during the degradation of 1,2-trans DCE. The possibility that 1,2-trans DCE induced production of new BMO enzyme was explored. The same concentrations of 1,2trans DCE that were used to characterize cytotoxic effects (25-50 jIM) were tested for their ability to induce BMO using a resting cell assay (Sayavedra-Soto et al. 2001). Lactate-grown P. butanovora, with no detectable BMO activity, gained BMO activity after exposure to 1,2-trans DCE concentrations between 20 and 50 M (figure 3.7). Concentrations of 1,2-trans DCE between 20 and 50 M induced BMO expression to about 50 % that of the butane control. The range of chlorinated compounds able to induce BMO activity was examined using the resting cell assay. 50 /LM 1,2-trans DCE, 1 ,2-cis DCE, and 1 ,2-DCA were found to induce 47, 25, and 29% of the activity of butane controls, respectively (see table 3.2). In contrast, PCE, TCE and 1,1 DCE did not induce expression of BMO. Fusion of lacZ to the BMO promoter, with consequent knock out of BMO activity, provided the opportunity to assess gene expression without the confounding effects of BMO inactivation or product induction of BMO gene expression. These data provide evidence that products of the BMO enzyme (1butanol and ethene oxide) may act as inducers of BMO gene expression. The natural substrate, butane, and the chlorinated cosubstrates, 1,2 DCA and 1 ,2-cis DCE induced the expression of BMO in the wild type but were unable to induce expression in the lacZ. These data indicate that the products of cooxidation may 33 be responsible for the induction of the BMO enzyme by 1,2 DCA and 1 ,2-cis DCE. In contrast, 1,2-trans DCE was able to induce lacZ expression without the involvement of BMO activity. Butane could not induce expression from the BMO catabolic promoter in the reporter strain (figure 3.8). In contrast, 1 -butanol, a downstream intermediate in butane metabolism, was able to induce lacZ expression (figure 3.8). 1,2-trans DCE was the only chlorinated ethene, and the only BMO substrate, able to induce the reporter strain. Increasing concentrations of 1,2-trans DCE produced increasing levels of induction in the reporter strain, and the induction phenomenon was observed at concentrations of 1,2-trans DCE <20 iiM. Lac Z activity levels in the reporter strain were limited to about a five-fold induction over background even at high concentrations of DCE. This provided an upper limit to the induction assays that could eventually be reached even by lower concentrations of 1,2-trans DCE (see figure 3.8). 34 0.5 0.4 w 0 0. 0.3 C I0.2 0 E C 0.1 Butane Buffer 5 10 20 30 40 50 1,2-trans DCE (pM) Figure 3.7. Induction of BMO activity in lactate-grown cells of P. butanovora in response to exposure to butane or varying concentrations of 1,2-trans DCE. BMO activity was measured after four hours using the ethene oxidation assay and is expressed on the Y-axis as nmoles EtO produced/mini mg protein. 35 Figure 3.8. Induction of lac Z in the reporter strain by varying concentrations of 1-butanol (.), 1,2-trans DCE (.), 1,2-cis DCE (o), and 1,1-DCE (A). Betagalactosidase activities were determined by end-point assays taken at select time intervals of 2 h (A) and 4 h (B) as described in the materials and methods. Data points are the means of three replicates and error bars represent standard deviation. 36 A Fig. 3.8 35000 30000 25000 Cl) 20000 :D 15000 10000 5000 0 0 20 40 60 80 100 60 80 100 pM B 35000 30000 25000 U) 20000 15000 10000 5000 0 0 20 40 pM 37 Table 3.2. Induction of BMO activity in P. butanovora and lacZ activity in the lacZ-BMO fusion in response to various substrates and products of BMO. Compound Concentration BMO Activity as a % of Butane control 50 50 100 >10 15880 0 Butane 1-Butanol Butyrate Reporter Strain Miller Units Above Background 0 50 0 % headspace 10 % headspace 0 0 ND 4751 50 0 0 50 0 0 1,2-trans DCE 50 47 5068 1 ,2-cis DCE 50 25 0 1,1-DCE 50 50 0 0 29 0 Ethylene Ethylene Oxide PCE TCE 1 ,2-DCA 10 Chapter 4. DISCUSSION Previous reports have shown that the roles of natural substrates as inducers of monooxygenase genes and generators of reductant to support monooxygenase activity may be replaced by chlorinated ethenes and other organic sources (Heald and Jenkins 1994; Leahy et al. 1996; McClay et al. 1995; Ryoo et al. 2001; Yeager Ct al In press 2004). This study extends the concept to cooxidation of DCEs by the alkane-oxidizing bacterium, 'Pseudomonas butanovora'. We believe this particular example could have applied significance because it is well recognized that partly dechlorinated products like DCEs may accumulate in sites experiencing reductive dechlorination, (Freedman et al. 2001; Kastner 1991; Semprini 1995). In situ generation of fermentative end products might facilitate further degradation of DCEs by oxidative cometabolism in downstream parts of the contaminated plume where conditions are aerobic. The use of exogenous electron donors has allowed researchers to examine the substrate range and kinetic parameters of oxidative cometabolism, while avoiding the competitive effects that occur when natural substrates are provided as electron donors (Dolan and McCarty 1995; Chu and Alvarez-Cohen 1999; Hamamura et al. 1997, Hamamura et al. 1999, Yeager et al. Biodegradation In press). For example, whole cell kinetic studies of TCE degradation in methanotrophic bacteria used formate as the alternative electron donor (Dolan and McCarty 1995; Chu and Alvarez-Cohen 1999; Henry and Grbic-Galic 1991; Johan et al. 1997), and by analogy, studies carried out on butane-oxidizing bacteria routinely used butyrate as an electron donor (Hamamura et al. 1997; Hamamura et al. 1999). My data showed that while various organic acids enhanced BMO activity in P. butanovora, differences existed in the maximum rate of cooxidation that could be supported by different organic acids and in the duration that those rates of cooxidation could be sustained. Indeed, the choice of butyrate as electron donor might have compromised interpretation of previously published data from our own laboratory that indicated 1, 2-trans DCE was not degraded by butane- grown P. butanovora when butyrate was provided as an alternative electron donor (Hamamura et al. 1997). In the current study the data clearly showed that 1,2-trans DCE was degraded with lactate as the electron donor. Although it remains unclear why lactate is a superior reductant for driving cooxidation in P. butanovora, several possibilities should be mentioned. First, the rate of butyrate-supported 1,2cis DCE cooxidation decreased more rapidly than did lactate-supported cooxidation, indicating that enzymes involved in generating reductant from butyrate might be differentially sensitive to the cooxidation process. In this context, it is interesting that pyruvate, an intermediate in lactate metabolism and known antioxidant, was able to offset some of the damage that occurred during TCE cooxidation in B. cepacia G4 (Yeager et al. 2001). Secondly, initial reactions in the metabolism of lactate in P. butanovora, and formate in methanotrophic bacteria directly generate reductant, whereas, initial energy investments are required in butyrate metabolism before net generation of reductant occurs. Furthermore, it is possible that butyrate is preferentially metabolized for biosynthetic purposes or carbon storage and not to oxidative metabolism via a monooxygenase. Thus, while removal of the natural substrate conceptually relieves competition between substrate and cosubstrate for the BMO active site, oxidative cometabolism remains in competition with other aspects of metabolism for reductant. Propionate was not able to enhance the cooxidation of ethene in butanegrown P. butanovora, but did enhance cooxidation in propane-grown cells. Competitive inhibition between the intermediates of butane metabolism (1butanol, butyraldehyde, and butyrate) and three carbon structural analogs suggests that enzymes involved in butane metabolism have high affinities for 1-propanol, propanaldehyde, and propionate, (Arp 1999) and it is likely that the oxidation of propane and butane to propionate and butyrate, respectively, is carried out by the same enzymes. Although the alkane substrates, butane and propane, appear to be oxidized to their respective acids by the same pathway, different downstream pathways are probably involved in the continued metabolism of the organic acids. Although acetate and formate are known products of propane metabolism in M vaccae (Coleman and Perry 1885; Vanderberg and Perryl98S), propane-grown P. butanovora cells could not use formate to support BMO activity and acetate supported BMO activity was less in propane than butane-grown cells. Additionally, propionate was not an identified intermediate in propane metabolism 41 in Lvi. vaccae, propionate supported BMO activity was specifically observed in propane-grown P. butanovora. Further investigation lead to several observations that were inconsistent with the model of propane metabolism described in M. vaccae. These results suggest that P. butanovora uses both even and odd chained 13-oxidation pathways in the metabolism of alkanes, and that even and odd chained 13-oxidation pathways are regulated in response to the chain-length of the alkane used for growth. Although the substrate range of BMO overlaps with the substrate range of other non-specific oxygenases (Arp et al. 2001; Sluis et al. 2002), kinetic parameters of substrate oxidation often differ between enzymes. For example, acetylene is a potent mechanism-based inhibitor of BMO (Hamamura et al. 1999), but the related toluene monooxygenase of B. cepacia G4 is unaffected by acetylene at similar concentrations (Yeager 1999). Cooxidation of 1,1-DCE, 1,2trans DCE, and 1 ,2-cis DCE led to different cytotoxic effects in P. butanovora. Cytotoxicity associated with the cooxidation of chlorinated ethenes was observed in several organisms including Burkholderia cepacia G4 (Yeager et al. 2001), a mixed methanotrophic culture (Dolan and McCarty 1995), and in Methylosinus trichosporium OB3b (Johan et al. 1997). B. cepacia G4 demonstrated a toxicity threshold in which cell viability decreased before TCE cooxidation capacity was reached (Yeager et al. 2001). Underlying metabolic processes responsible for the allocation of reductant to the monooxygenase remained intact longer than did the viability of the cells, making the B. cepacia G4 example unique. 1,2-trans DCE and 1 ,2-cis DCE, might represent potential tools for comparative structure function studies in these enzymes, and to address aspects of gene regulation. In the case of 1,2-cis DCE, Johan et al. (1997) determined that its cooxidation by M trichosporium OB3b was more toxic to cell viability than the degradation of 1,2-trans DCE. The authors suspected that decreased viability and enzyme activity appeared to be associated with the turnover of 1 ,2-cis DCE epoxide, while 1,2-trans DCE epoxide was not actively degraded. In contrast, P. butanovora incurred loss of viability >90% after the cooxidation of only 25 nmoles /mg protein of either 1,2-trans DCE, 1,2-cis DCE, or 1,1 DCE. Discrepancies between M trichosporium OB3b and P. butanovora could be attributed to differential activity of the monooxygenase enzymes towards the epoxides or differential sensitivity of the organisms to oxidative metabolism. TCE consumption by toluene-grown B. cepacia G4 was not enhanced by exogenous electron donors. However, the overall respiration of toluene-grown cells could be enhanced by acetate. During TCE cooxidation B. cepacia G4 retained the ability to allocate reductant from endogenous energy stores to oxidative cometabolism longer than acetate was able to enhance the overall respiration of the cells (Yeager et al. 2001). This indicated differential sensitivity of these metabolic pathways to the cooxidative process. Similarly, lactatedependent oxygen consumption (figure 3.5) and cell viability (figure 3.6) decreased more rapidly than did the rate of DCE consumption (figure 3.3) or BMO activity (figure 3.4) in cells treated with either 1 ,2-cis DCE or 1,2-trans DCE. 43 Previous research from our laboratory showed that butane-monooxygenase can be up-regulated and down regulated in P. butanovora. Sayavedra-Soto et al. (2001) demonstrated that butane was the most effective inducer of BMO activity. However, downstream metabolites of butane oxidation, 1-butanol and butyraldehyde, were also inducers of BMO and it remains unclear if the substrate or products are the more significant inducers. Xanthobacter Py2 possesses a related monooxygenase (Zhou et al 1999) enzyme that is induced during growth on alkenes and during the cooxidation of some chlorinated ethenes (Ensign 1996; Krum and Ensign 2000). Correlation between the substrate range and the range of compounds able to act as inducers of the monooxygenase lead to the proposal that products induced the monooxygenase of Xanthobacter Py2 and not the substrates themselves (Ensign 1996). In my study, the range of compounds able to induce monooxygenase activity correlated with the substrate range of BMO. A reporter strain, BMO insertional knockout, highlighted the trend of product induction in P. butanovora. Butane, 1 ,2-cis DCE, and ethylene were unable to induce the reporter. In contrast, the BMO products, 1-butanol and ethylene oxide induced the reporter strain. 1,2-trans DCE was unique among these compounds in its ability to induce expression of 3-ga1actosidease from the BMO promoter of the reporter strain. Although a clear explanation for reporter strain induction by 1,2-trans DCE cannot be made, others have proposed that separate mechanisms were responsible for the induction of toluene-monooxygenase in response to toluene and TCE in P. stutzeri OX1 (Ryoo 2001). Researchers in our lab have speculated that 44 downstream regulatory proteins may also bind upstream of the BMO promoter (Sayavedra-Soto et al. 2001), and thereby provide an independent mechanism of induction. In summary, the findings presented in this thesis have provided some new insights into the properties of hydrocarbon oxidation in P. butanovora regarding the molecular regulation of hydrocarbon oxidation genes in P. butanovora, and into the mechanisms that control the competing requirements for reductant of monooxygenase reductant and biosynthesis. 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