Regulation of formate dehydrogenase activity in Methanococcus thermolithotrophicus.

Methanococcus thermolithotrophicus can use either H2 or formate as the electron donor for methanogenesis from CO2. Resuspended-cell experiments revealed that the ability to use H2 as the source of electrons for methanogenesis was constitutive; cells grown on formate or H2-CO2 were equally capable of H2-CO2 methanogenesis. The ability to metabolize formate at high rates was observed only in cells previously grown on formate. Two such strains were distinguished: strain F and strain HF. Strain F was repeatedly grown exclusively on formate for over 3 years; this strain showed a constitutive capacity to metabolize formate to methane, even after subsequent repeated transfers to medium containing only H2-CO2. Strain HF could only metabolize formate to methane when grown in the presence of formate with no H2 present; this strain was recently derived from another strain (H) that had been exclusively grown on H2-CO2 and which upon initial transfer to formate medium could only metabolize formate to methane at a very slow rate. Initial adaptation of strain H to growth on formate was preceded by a long lag. The specific activities of hydrogenase and formate dehydrogenase in cell extracts derived from these different strains confirmed these findings. Similar levels of hydrogenase were observed in all strains, independent of the presence of H2 in the growth medium medium. High levels of formate dehydrogenase were also constitutive in strain F. Only low formate dehydrogenase activities were observed in strain H. High levels of formate dehydrogenase were observed in strain HF only when these cells were grown with formate in the absence of H2. In all strains the two- to threefold fluctuations of both hydrogenase and formate dehydrogenase cell-free activities were observed during growth, with peak activities reached in the middle of the exponential phase.     

Characteristics of anaerobic oxalate-degrading enrichment cultures from the rumen.

Enrichment cultures of rumen bacteria degraded oxalate within 3 to 7 days in a medium containing 10% rumen fluid and an initial level of 45 mM sodium oxalate. This capability was maintained in serially transferred cultures. One mole of methane was produced per 3.8 mol of oxalate degraded. Molecular hydrogen and formate inhibited oxalate degradation but not methanogenesis; benzyl viologen and chloroform inhibited both oxalate degradation and methanogenesis. Attempts to isolate oxalate-degrading bacteria from these cultures were not successful. Oxalate degradation was uncoupled from methane production when enrichments were grown in continuous culture at dilution rates greater than or equal to 0.078 h-1. Growth of the uncoupled population (lacking methanogens) in batch culture was accompanied by degradation of 45 mM oxalate within 24 h and production of 0.93 mol of formate per mol of oxalate degraded. Oxalate degradation by the uncoupled population was not inhibited by molecular hydrogen or formate. Cell yields (grams [dry weight]) per mole of oxalate degraded by the primary enrichment and the uncoupled populations were 1.7 and 1.0, respectively.     

Growth substrate effects on acetate and methanol catabolism in Methanosarcina sp. strain TM-1.

When Methanosarcina sp. strain TM-1 is grown in medium in which both methanol and acetate are present, growth is biphasic, with methanol used as the primary catabolic substrate during the first phase. To better understand this phenomenon, we grew cells on methanol or on acetate or on both and examined the abilities of anaerobically washed cells to catabolize these substrates. Washed acetate-grown cells incubated with 10 mM acetate, 10 mM methanol, or both substrates together produced methane at initial rates of 325, 3, and 315 nmol min-1 mg of protein-1, respectively. Although the initial rate of methanogenesis from both substrates was nearly identical to the rate for acetate alone, after several hours of incubation the rate was greater for cells provided with both substrates. Studies with 14C-labeled methanol indicated that methanol was catabolized to methane at increasing rates by acetate-grown cells in a manner reminiscent of an induction curve, but only when cells were provided with acetate as a cosubstrate. Acetate was presumably providing energy and carbon for induction of methanol-catabolic enzymes. Methanol-grown cells showed a pattern of substrate utilization significantly different from that of acetate-grown cells, producing methane from 10 mM acetate, 10 mM methanol, or both substrates at initial rates of 10, 280, and 450 nmol min-1 mg of protein-1, respectively. There was significant oxidation of the methyl group of acetate during metabolism of both substrates. Cells grown on methanol-acetate and harvested before methanol depletion (methanol phase) showed catabolic patterns nearly identical to those of methanol-grown cells, including a low rate of methanogenesis from acetate. Cells harvested from methanol-acetate cultures in the acetate phase were capable of significant methanogenesis from either methanol or acetate alone, and the rate from both substrates together was nearly equal to the sum of the rates for the single substrates. When both 10 mM methanol and 10 mM acetate were presented to the acetate-phase cells, there was a preference for the methanol. These results are consistent with a model for regulation in Methanosarcina sp. strain TM-1 in which methanol represses acetate catabolism while methanol catabolism is inducible.     

Effect of pH on Anaerobic Mild Steel Corrosion by Methanogenic Bacteria

Methanogens can use H₂ produced by cathodic depolarization-mediated oxidation of elemental iron to produce methane. Thermodynamic consideration of the cathodic depolarization mechanism predicts more oxidation of Fe⁰ at lower pH. Methanogenic responses to pH by Methanococcus deltae, Methanococcus thermolithotrophicus, and Methanosarcina barkeri were examined. When grown on H₂-CO₂, these bacteria had pH optima from 6.2 to 7.0, but when all H₂ was supplied from Fe⁰, methanogenic pH optima were lower, 5.4 to 6.5. Corrosion was monitored with and without cultures and at various pHs; more corrosion occurred when cultures were present, biologically induced corrosion was greatest at the pH optima for methanogenesis from Fe⁰, and corrosion without cultures increased with a drop in pH.     

Kinetic study and mathematical modeling of methanogenesis of acetate using pure cultures of methanogens

Kinetics of methanogenesis from acetate was studied using pure cultures of Methanosarcina barkeri and Methanosarcina mazei. Methane formation was found to be associated with cell growth. Nearly equimolar methane was produced from acetate during the methanogenic growth, and about 1.94 g of cells were formed from each mole of acetate consumed. Cell growth can be estimated from methane production. Significant substrate inhibition was found when acetate concentration was higher than 0.12 M. Among the three methanogenic strains studied, M. mazei strain S6 had the highest specific growth rate at all acetate concentrations studied and was least sensitive to environmental factors investigated (e.g., acetate concentration). The maximum specific growth rate found for strain S6 was 0.022 hr(-1) at acetic acid concentration around 7 g/L. The other two strains studied were M. barkeri strain 227 and strain MS. Growth of M. barkeri was completely inhibited at sodium acetate concentrations higher than 0.24 M. The maximum specific growth rate found for strains 227 and MS was 0.019 and 0.021 h(-1) at acetic acid concentrations of 3.6 and 6.8 g/L, respectively. A kinetic model with substrate inhibition was developed and can be used to simulate the methane formation from M. mazei strain S6 grown on acetate at 35 degrees C, pH 7.     

Microbial Methane Formation from Hard Coal and Timber in an Abandoned Coal Mine

About 7% of the global annual methane emissions originate from coal mining. Also, mine gas has come into focus of the power industry and is being used increasingly for heat and power production. In many coal deposits worldwide, stable carbon and hydrogen isotopic signatures of methane indicate a mixed thermogenic and biogenic origin. In this study, we have measured in an abandoned coal mine methane fluxes and isotopic signatures of methane and carbon dioxide, and collected samples for microbiological and phylogenetic investigations. Mine timber and hard coal showed an in-situ production of methane with isotopic signatures similar to those of the methane in the mine atmosphere. Enrichment cultures amended with mine timber or hard coal as sole carbon sources formed methane over a period of nine months. Predominantly, acetoclastic methanogenesis was stimulated in enrichments containing acetate or hydrogen/carbon dioxide. Molecular techniques revealed that the archaeal community in enrichment cultures and unamended samples was dominated by members of the Methanosarcinales. The combined geochemical and microbiological investigations identify microbial methanogenesis as a recent source of methane in abandoned coal mines.     

Methanogenesis from Choline by a Coculture of Desulfovibrio sp. and Methanosarcina barkeri

A sulfate-reducing vibrio was isolated from a methanogenic enrichment with choline as the sole added organic substrate. This organism was identified as a member of the genus Desulfovibrio and was designated Desulfovibrio strain G1. In a defined medium devoid of sulfate, a pure culture of Desulfovibrio strain G1 fermented choline to trimethylamine, acetate, and ethanol. In the presence of sulfate, more acetate and less ethanol were formed from choline than in the absence of sulfate. When grown in a medium containing sulfate, a coculture of Desulfovibrio strain G1 and Methanosarcina barkeri strain Fusaro degraded choline almost completely to methane, ammonia, and hydrogen sulfide and presumably to carbon dioxide. Methanogenesis occurred in two distinct phases separated by a lag of about 6 days. During the first phase of methanogenesis choline was completely converted to trimethylamine, acetate, hydrogen sulfide, and traces of ethanol by the desulfovibrio. M. barkeri fermented trimethylamine to methane, ammonia, and presumably carbon dioxide via dimethyl- and methylamine as intermediates. Simultaneously, about 60% of the acetate expected was metabolized. In the second phase of methanogenesis, the residual acetate was almost completely catabolized.     

Role of formate in methanogenesis from xylan by Cellulomonas sp. associated with methanogens and Desulfovibrio vulgaris: Inhibition of the aceticlastic reaction

Abstract Different methanogenic defined mixed cultures, including Cellulomonas sp. strain ATCC21399 as a hydrolytic and fermentative bacterium, were used to show that methane production could proceed from larchwood xylan as well as from cellulose. Via the different mixtures of bacteria used, the role of formate is described. It is shown that formate inhibits methanogenesis from acetate by pure cultures of aceticlastic methanogens.     

Relationship of formate to growth and methanogenesis by Methanococcus thermolithotrophicus

Methanococcus thermolithotrophicus is a methanogenic archaebacterium that can use either H2 or formate as its source of electrons for reduction of CO2 to methane. Growth and suspended-whole-cell experiments show that H2 plus CO2 methanogenesis was constitutive, while formate methanogenesis required adaptation time; selenium was necessary for formate utilization. Cells grown on formate had 20 to 100 times higher methanogenesis rates on formate than cells grown on H2-CO2 and transferred into formate medium. Enzyme assays with crude extracts and with F420 or methyl viologen as the electron acceptor revealed that hydrogenase was constitutive, while formate dehydrogenase was regulated. Cells grown on formate had 10 to 70 times higher formate dehydrogenase activity than cells grown on H2-CO2 with Se present in the medium; when no Se was added to H2-CO2 cultures, even lower activities were observed. Adaptation to and growth on formate were pH dependent, with an optimal pH for both about one pH unit above that optimal for H2-CO2 (pH 5.8 to 6.5). When cells were grown on H2-CO2 in the presence of formate, formate (greater than or equal to 50 mM) inhibited both growth and methanogenesis at pH 5.8 to 6.2, but not at pH greater than 6.6. Both acetate and propionate produced similar inhibition. Formate inhibition was also observed in Methanospirillum hungatei.     

Relationship of formate to growth and methanogenesis by Methanococcus thermolithotrophicus.

Methanococcus thermolithotrophicus is a methanogenic archaebacterium that can use either H2 or formate as its source of electrons for reduction of CO2 to methane. Growth and suspended-whole-cell experiments show that H2 plus CO2 methanogenesis was constitutive, while formate methanogenesis required adaptation time; selenium was necessary for formate utilization. Cells grown on formate had 20 to 100 times higher methanogenesis rates on formate than cells grown on H2-CO2 and transferred into formate medium. Enzyme assays with crude extracts and with F420 or methyl viologen as the electron acceptor revealed that hydrogenase was constitutive, while formate dehydrogenase was regulated. Cells grown on formate had 10 to 70 times higher formate dehydrogenase activity than cells grown on H2-CO2 with Se present in the medium; when no Se was added to H2-CO2 cultures, even lower activities were observed. Adaptation to and growth on formate were pH dependent, with an optimal pH for both about one pH unit above that optimal for H2-CO2 (pH 5.8 to 6.5). When cells were grown on H2-CO2 in the presence of formate, formate (greater than or equal to 50 mM) inhibited both growth and methanogenesis at pH 5.8 to 6.2, but not at pH greater than 6.6. Both acetate and propionate produced similar inhibition. Formate inhibition was also observed in Methanospirillum hungatei.     

Effect of H(2)-CO(2) on Methanogenesis from Acetate or Methanol in Methanosarcina spp

Growth of Methanosarcina sp. strain 227 and Methanosarcina mazei on H(2)-CO(2) and mixtures of H(2)-CO(2) and acetate or methanol was examined. The growth yield of strain 227 on H(2)-CO(2) in complex medium was 8.4 mg/mmol of methane produced. Growth in defined medium was characteristically slower, and cell yields were proportionately lower. Labeling studies confirmed that CO(2) was rapidly reduced to CH(4) in the presence of H(2), and little acetate was used for methanogenesis until H(2) was exhausted. This resulted in a biphasic pattern of growth similar to that reported for strain 227 grown on methanol-acetate mixtures. Biphasic growth was not observed in cultures on mixtures of H(2)-CO(2) and methanol, and less methanol oxidation occurred in the presence of H(2). In M. mazei the aceticlastic reaction was also inhibited by the added H(2), but since the cultures did not immediately metabolize H(2), the duration of the inhibition was much longer.     

Trace methane oxidation studied in several Euryarchaeota under diverse conditions

We used (13)C-labeled methane to document the extent of trace methane oxidation by Archaeoglobus fulgidus, Archaeoglobus lithotrophicus, Archaeoglobus profundus, Methanobacterium thermoautotrophicum, Methanosarcina barkeri and Methanosarcina acetivorans. The results indicate trace methane oxidation during growth varied among different species and among methanogen cultures grown on different substrates. The extent of trace methane oxidation by Mb. thermoautotrophicum (0.05 +/- 0.04%, +/- 2 standard deviations of the methane produced during growth) was less than that by M. barkeri (0.15 +/- 0.04%), grown under similar conditions with H(2) and CO(2). Methanosarcina acetivorans oxidized more methane during growth on trimethylamine (0.36 +/- 0.05%) than during growth on methanol (0.07 +/- 0.03%). This may indicate that, in M. acetivorans, either a methyltransferase related to growth on trimethylamine plays a role in methane oxidation, or that methanol is an intermediate of methane oxidation. Addition of possible electron acceptors (O(2), NO(3) (-), SO(4) (2-), SO(3) (2-)) or H(2) to the headspace did not substantially enhance or diminish methane oxidation in M. acetivorans cultures. Separate growth experiments with FAD and NAD(+) showed that inclusion of these electron carriers also did not enhance methane oxidation. Our results suggest trace methane oxidized during methanogenesis cannot be coupled to the reduction of these electron acceptors in pure cultures, and that the mechanism by which methane is oxidized in methanogens is independent of H(2) concentration. In contrast to the methanogens, species of the sulfate-reducing genus Archaeoglobus did not significantly oxidize methane during growth (oxidizing 0.003 +/- 0.01% of the methane provided to A. fulgidus, 0.002 +/- 0.009% to A. lithotrophicus and 0.003 +/- 0.02% to A. profundus). Lack of observable methane oxidation in the three Archaeoglobus species examined may indicate that methyl-coenzyme M reductase, which is not present in this genus, is required for the anaerobic oxidation of methane, consistent with the "reverse methanogenesis" hypothesis.     

Growth characteristics and corrinoid production of Methanosarcina barkeri on methanol-acetate medium

Methanosarcina barkeri strain Fusaro was grown on a mixed substrate medium of methanol and acetate. When 50 mM of acetate was added to the methanol basal medium (250 mM), the rates of methane production, methanol consumption, cell growth and corrinoid production were stimulated 3.2, 2.7, 3.5, and 2.4 times, respectively compared with those in methanol alone. Addition of acetate also has significant influence on corrinoid distribution decreasing the intracellular corrinoid content from 6.8 to 3.0 mg/g dry cell and increasing the extracellular corrinoid concentration from 4.0 to 5.4 mg/l. The carbon balance analysis for methanogenesis and cellular growth with or without acetate addition revealed that about 50% of the utilized acetate carbon might be incorporated in the cellular materials and the remaining might be oxidized to generate the electrons which stimulate the methanol reduction to methane, accelerating the metabolic activities of the methanogenesis from methanol consequently enhancing the rates of methane and corrinoid production, and cell growth.     

Methanogenesis from methanol in Methanosarcina barkeri studied using membrane inlet mass spectrometry

Abstract A mass spectrometer with membrane inlet was used to study methanol metabolism by Methanosarcina barkeri strain MS. The addition of methanol to methanol grown culture samples in the mass spectrometer vessel stimulated methanogenesis and hydrogen production. The apparent K _s for methanol was determined as 0.5 mM and the V _max as 8.14 mmol g (dry weight) h⁻¹. The V _max for methane production was fairly constant during growth of the culture on methanol implying that growth is tightly coupled to methanogenesis. The addition of methanol to culture samples in the mass spectrometer vessel stimulated methanogenesis with no lag which indicated that methanogenesis can be uncoupled from growth. Exposure of the culture sample in the mass spectrometer vessel to an atmosphere of 2 kPa oxygen for 80 min resulted in a decrease in the rate of methanogenesis from methanol but on returning the atmosphere to nitrogen the addition of further methanol stimulated methanogenesis. The effect of other inhibitors of methanogenesis (2-bromoethane sulphonate and monensin); K _j values 21.5 μM and 0.3 mM, respectively) were also studied.     

Anaerobic Degradation of Lactate by Syntrophic Associations of Methanosarcina barkeri and Desulfovibrio Species and Effect of H(2) on Acetate Degradation

When grown in the absence of added sulfate, cocultures of Desulfovibrio desulfuricans or Desulfovibrio vulgaris with Methanobrevibacter smithii (Methanobacterium ruminantium), which uses H(2) and CO(2) for methanogenesis, degraded lactate, with the production of acetate and CH(4). When D. desulfuricans or D. vulgaris was grown in the absence of added sulfate in coculture with Methanosarcina barkeri (type strain), which uses both H(2)-CO(2) and acetate for methanogenesis, lactate was stoichiometrically degraded to CH(4) and presumably to CO(2). During the first 12 days of incubation of the D. desulfuricans-M. barkeri coculture, lactate was completely degraded, with almost stoichiometric production of acetate and CH(4). Later, acetate was degraded to CH(4) and presumably to CO(2). In experiments in which 20 mM acetate and 0 to 20 mM lactate were added to D. desulfuricans-M. barkeri cocultures, no detectable degradation of acetate occurred until the lactate was catabolized. The ultimate rate of acetate utilization for methanogenesis was greater for those cocultures receiving the highest levels of lactate. A small amount of H(2) was detected in cocultures which contained D. desulfuricans and M. barkeri until after all lactate was degraded. The addition of H(2), but not of lactate, to the growth medium inhibited acetate degradation by pure cultures of M. barkeri. Pure cultures of M. barkeri produced CH(4) from acetate at a rate equivalent to that observed for cocultures containing M. barkeri. Inocula of M. barkeri grown with H(2)-CO(2) as the methanogenic substrate produced CH(4) from acetate at a rate equivalent to that observed for acetate-grown inocula when grown in a rumen fluid-vitamin-based medium but not when grown in a yeast extract-based medium. The results suggest that H(2) produced by the Desulfovibrio species during growth with lactate inhibited acetate degradation by M. barkeri.     

Conversion of glucose to fatty acids and methane: roles of two mycoplasmal agents.

Two species of obligately anaerobic mycoplasmas were the major components of a methanogenic glucose-limited enrichment culture. In pure culture, one of these organisms, tentatively named Anaeroplasma sp. strain London, was shown to be responsible for the fermentation of glucose to fatty acids, hydrogen, and carbon dioxide; the other mycoplasma was shown to produce methane from hydrogen and carbon dioxide and was named Methanoplasma elizabethii. This same methanogenic mycoplasma contained a low-molecular-weight fluorescent cofactor which had a maximum light absorbance at 430 nm. When both species of mycoplasmas were grown together on glucose, fermentation products included fatty acids and methane. For the first time, mycoplasmas are implicated as agents of anaerobic degradation and methanogenesis in a sewage sludge digester.     

A methyl-CoM methylreductase system from methanogenic bacterium strain G? 1 not requiring ATP for activity

Crude inside-out vesicles from the methanogenic strain G?1 were prepared via protoplasts. These vesicles catalyzed methane formation from methyl-CoM and H2 at a maximal rate of 35 nmol/min.mg protein. Methane formation by the vesicles did not depend on the addition of ATP. This was in contrast to conventionally prepared crude extracts from the same organism or from Methanosarcina barkeri which exhibited strict ATP dependence of methanogenesis. ATP analogues inhibited methanogenesis by extracts to a much higher extent than that by vesicles. Both, particulate and soluble components prepared from the crude vesicles by ultracentrifugation were necessary for ATP-independent methane formation from methyl-CoM and H2. Hydrogenase activity was mainly associated with the particulate fraction whereas methyl-CoM methylreductase could be assigned to the soluble fraction. The detergent sulfobetaine inhibited methane formation from methyl-CoM without affecting hydrogenase or titanium citrate-dependent methylreductase activities, indicating that an additional membraneous component is involved in methanogenesis for methyl-CoM and H2.     

Metabolism of Formate in Methanobacterium formicicum

Methanobacterium formicicum strain JF-1 was cultured with formate as the sole energy source in a pH-stat fermentor. Growth was exponential, and both methane production and formate consumption were linear functions of the growth rate. Hydrogen was produced in only trace amounts, and the dissolved H₂ concentration of the culture medium was below 1 μM. The effect of temperature or pH on the rate of methane formation was studied with a single fermentor culture in mid-log phase that was grown with formate under standard conditions at 37°C and pH 7.6. Methane formation from formate occurred over the pH range from 6.5 to 8.6, with a maximum at pH 8.0. The maximum temperature of methanogenesis was 56°C. H₂ production increased at higher temperatures. Hydrogen and formate were consumed throughout growth when both were present in saturating concentrations. The molar growth yields were 1.2 ± 0.06 g (dry weight) per mol of formate and 4.8 ± 0.24 g (dry weight) per mol of methane. Characteristics were compared for cultures grown with either formate or H₂-CO₂ as the sole energy source at 37°C and pH 7.6; the molar growth yield for methane of formate cultures was 4.8 g (dry weight) per mol, and that of H₂-CO₂ cultures was 3.5 g (dry weight) per mol. Both formate and H₂-CO₂ cultures had low efficiencies of electron transport phosphorylation; formate-cultured cells had greater specific activities of coenzyme F₄₂₀ than did H₂-CO₂-grown cultures. Hydrogenase, formate dehydrogenase, chromophoric factor F₃₄₂, and low levels of formyltetrahydrofolate synthetase were present in cells cultured with either substrate. Methyl viologen-dependent formate dehydrogenase was found in the soluble fraction from broken cells.     

Pollutant degradation by a Methylocystis strain SB2 grown on ethanol: bioremediation via facultative methanotrophy

A facultative methanotroph, Methylocystis strain SB2, was examined for its ability to degrade chlorinated hydrocarbons when grown on methane or ethanol. Strain SB2 grown on methane degraded vinyl chloride (VC), trans-dichloroethylene (t-DCE), trichloroethylene (TCE), 1,1,1-trichloroethane (1,1,1-TCA), and chloroform (CF), but not dichloromethane (DCM). Growth on methane was reduced in the presence of any chlorinated hydrocarbon. Strain SB2 grown on ethanol degraded VC, t-DCE, and TCE, and 1,1,1-TCA, but not DCM or CF. With the exception of 1,1,1-TCA, the growth of strain SB2 on ethanol was not affected by any individual chlorinated hydrocarbon. No degradation of any chlorinated hydrocarbon was observed when acetylene was added to ethanol-grown cultures, indicating that this degradation was due to particulate methane monooxygenase (pMMO) activity. When mixtures of chlorinated alkanes or alkenes were added to cultures growing on methane or ethanol, chlorinated alkene degradation occurred, but chlorinated alkanes were not, and growth was reduced on both methane and ethanol. Collectively, these data indicate that competitive inhibition of pMMO activity limits methanotrophic growth and pollutant degradation. Facultative methanotrophy may thus be useful to extend the utility of methanotrophs for bioremediation as the use of alternative growth substrates allows for pMMO activity to be focused on pollutant degradation.     

Dependence of tetrachloroethylene dechlorination on methanogenic substrate consumption by Methanosarcina sp. strain DCM.

Tetrachloroethylene (perchloroethylene, PCE) is a suspected carcinogen and a common groundwater contaminant. Although PCE is highly resistant to aerobic biodegradation, it is subject to reductive dechlorination reactions in a variety of anaerobic habitats. The data presented here clearly establish that axenic cultures of Methanosarcina sp. strain DCM dechlorinate PCE to trichloroethylene and that this is a biological reaction. Growth on methanol, acetate, methylamine, and trimethylamine resulted in PCE dechlorination. The reductive dechlorination of PCE occurred only during methanogenesis, and no dechlorination was noted when CH4 production ceased. There was a clear dependence of the extent of PCE dechlorination on the amount of methanogenic substrate (methanol) consumed. The amount of trichloroethylene formed per millimole of CH4 formed remained essentially constant for a 20-fold range of methanol concentrations and for growth on acetate, methylamine, and trimethylamine. These results suggest that the reducing equivalents for PCE dechlorination are derived from CH4 biosynthesis and that the extent of chloroethylene dechlorination can be enhanced by stimulating methanogenesis. It is proposed that electrons transferred during methanogenesis are diverted to PCE by a reduced electron carrier involved in methane formation.