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Applied and Environmental Microbiology, July 2006, p. 5138-5141, Vol. 72, No. 7
0099-2240/06/$08.00+0 doi:10.1128/AEM.00489-06
Copyright © 2006, American Society for Microbiology. All Rights Reserved.
Acetate Oxidation Is the Dominant Methanogenic Pathway from Acetate in the Absence of Methanosaetaceae
Dimitar Karakashev,
Damien J. Batstone,
Eric Trably, and
Irini Angelidaki*
Institute of Environment & Resources DTU, Technical University of Denmark, Building 113, DK-2800 Kgs. Lyngby, Denmark
Received 1 March 2006/
Accepted 8 May 2006

ABSTRACT
The oxidation of acetate to hydrogen, and the subsequent conversion
of hydrogen and carbon dioxide to methane, has been regarded
largely as a niche mechanism occurring at high temperatures
or under inhibitory conditions. In this study, 13 anaerobic
reactors and sediment from a temperate anaerobic lake were surveyed
for their dominant methanogenic population by using fluorescent
in situ hybridization and for the degree of acetate oxidation
relative to aceticlastic conversion by using radiolabeled [2-
14C]acetate
in batch incubations. When
Methanosaetaceae were not present,
acetate oxidation was the dominant methanogenic pathway. Aceticlastic
conversion was observed only in the presence of
Methanosaetaceae.

INTRODUCTION
Acetate is the main precursor for methane production during
anaerobic digestion of organic matter. Two mechanisms for methane
formation from acetate have been described. The first one is
aceticlastic, being carried out by
Methanosarcinaceae or
Methanosaetaceae (
2).
Methanosarcinaceae generally have a higher acetate threshold
but a higher growth rate and yield than
Methanosaetaceae (
2).
The second mechanism encompasses a two-step reaction in which
acetate is first oxidized to H
2 and CO
2 and, with these products,
subsequently converted to methane (
15). This reaction is performed
by acetate-oxidizing bacteria (often
Clostridium spp.) in a
syntrophic association with hydrogenotrophic methanogens (often
Methanomicrobiales or
Methanobacteriales) (
4,
10,
12).
Some important environmental factors influencing the rate of anaerobic aceticlastic activity are temperature, organic acid concentrations, and ammonia concentration (9). At temperatures between 50°C and 65°C, acetate oxidation is favored at low acetate concentrations, while aceticlastic methanogenesis is favored at high acetate concentrations (15). The dominance of acetate oxidation at lower concentrations increases with increased temperature. Syntrophic acetate oxidation is the main mechanism for acetate degradation in the presence of inhibitors, particularly ammonium and volatile fatty acids (VFAs) (13). Syntrophic acetate oxidation has been reported for natural anoxic environments in subtropical lake sediments at temperatures as low as 15°C (8).
It is relatively straightforward to detect acetate oxidation activity by measuring the production of 14CH4 and 14CO2 from acetate labeled in the methyl group (C-2). When aceticlastic methanogens degrade acetate, the labeled methyl group will form only labeled methane (2). During syntrophic acetate oxidation, both carbon atoms of acetate are converted to carbon dioxide, and some of the carbon dioxide is subsequently reduced to methane (13). Therefore, significant levels of labeled carbon dioxide from [2-14C]acetate will be formed only during the oxidation of acetate.
The diversity of environments in which syntrophic acetate oxidation has been found indicates it may also be important for commercial gas production in biogas reactors, digesting wastewater sludge and manure. Aceticlastic activity has generally been considered to be the dominant pathway, with either Methanosarcinaceae or Methanosaetaceae dominating (9, 15). If a second pathway, such as acetate oxidation, dominates, it is necessary to re-evaluate reactor operation and optimization, which are currently based on maintaining Methanosaetaceae populations. The objective of this work was to assess the degree of acetate oxidation relative to aceticlastic conversion in a wide range of industrial anaerobic digesters, fed with either manure or wastewater sludge. A low-temperature environmental sample was also evaluated.

Sampling.
Thirteen Danish full-scale anaerobic digesters digesting manure
together with waste from food industries were sampled as described
in reference
5. An anaerobic sediment sample was collected from
a lake situated in Orholm (Sollerod municipality, Denmark) at
a 0.2-m depth with a gravity corer (
6).

Analysis of the samples.
The samples were analyzed for VFAs and ammonia by standard methods
(
1). Microbial ecology was evaluated with fluorescent in situ
hybridization (FISH) using established probes (see Table S1
in the supplemental material) and a previously reported method
(
5). Methanogenic populations not identified by FISH were assessed
using PCR-temporal temperature gradient gel electrophoresis
(PCR-TGGE).

Medium.
Basal anaerobic medium was used for acetic oxidation batch tests
as described previously (
5). The medium was dispensed anaerobically
under a N
2/CO
2 (80%:20%) headspace in 100-ml incubation bottles,
amended with labeled [2-
14C]sodium acetate and nonlabeled sodium
acetate. The medium was reduced with Na
2S · 9H
2O and
supplemented aseptically with a sterilely filtered anaerobic
vitamin solution as described previously (
5). After inoculation
with raw sample, the bottles were closed hermetically and incubated
until methane production ceased. This was considered the end
of the test, and analysis followed.

Radioisotope analyses.
The liquid and headspace of the bottles were sparged with approximately
2 liters of N
2 through a 5 M NaOH trap to collect the
14CO
2.
The
14CH
4 collected after trapping was combusted to
14CO
2 in
a tube furnace at 800°C. The
14CO
2 generated in this furnace
was then trapped in a carbon dioxide absorber for liquid scintillation
counting (Carbosorb-E; Packard Bioscience Company). Radioactivity
measurements of liquid samples were performed using a liquid
scintillation counter (Tri-Carb 1600; PerkinElmer).

Simulation of methane production rates.
A simple kinetic batch model, based on Monod kinetics with zero-order
lag, for conversion of acetate to methane was implemented with
AQUASIM 2.1d (
11). The maximum acetate removal rate and lag
phase were estimated by fitting measured cumulative methane
to modeled cumulative methane. The Secant method, with an objective
function of residual sum of squares, was used to fit the data.
An overview of the results from the acetate oxidation survey experiment is given in Table 1.

Rates of methane production and acetate removal.
Methane production rates varied considerably, with fast samples
(such as Lundtofte and Hillerød) stopping methane production
in 3 days and slow samples (e.g., Nysted and Vegger) requiring
more than 10 days. The anaerobic lake sediment sample (Orholm)
had a lag phase of 31.5 ± 0.8 days. Acetate removal rates
also varied within a factor of approximately 10 (Table
1). These
rates were higher (>4 mM · day
1) for cultures
with a low degree of acetate oxidation than for cultures with
a high degree of acetate oxidation (acetate utilization rates
lower than 4 mM · day
1). Our rates compare with
acetate removal rates in pure culture for mesophilic (
12) and
thermophilic (
4) acetate-oxidizing cultures.

Anaerobic acetate conversion pathways and environmental conditions.
In all cases, populations dominated by
Methanosaetaceae had
low levels of acetate oxidation (
14CO
2/
14CH
4 < 0.1), while
populations dominated by other methanogenic
Archaea and without
Methanosaetaceae had high levels of acetate oxidation (
14CO
2/
14CH
4 > 1) (Table
1). Results obtained clearly showed a strong
correlation between the absence of
Methanosaetaceae and the
involvement of the acetate oxidation pathway. Other factors
(e.g., source and inoculum temperature) had no influence. Acetate
cleavage has been generally regarded as a bimodal system, dominated
by
Methanosarcinaceae at high acetate concentrations and by
Methanosaetaceae at low acetate concentrations (
2,
14). From
the data presented here, we propose instead a different bimodal
system in mixed cultures, with aceticlastic methanogenesis in
the presence of
Methanosaetaceae and acetate oxidation in their
absence. The absence of this methanogenic phylogenetic group
has been previously investigated in the systems analyzed here
and was linked to the presence of high ammonia and VFA levels
(
5). Most probably, the high ammonia concentrations inhibit
the aceticlastic methanogens much more than the hydrogenotrophic
methanogens, and methane is formed mainly by hydrogen-utilizing
methanogens. This idea is supported by previous studies (
3)
indicating that acetate-utilizing methanogens are more sensitive
to ammonia than are hydrogenotrophic methanogens. The high degree
of acetate oxidation in digested manure at high ammonia and
VFA levels is also in agreement with other results (
13). However,
a large potential for syntrophic acetate oxidation was also
observed at low acetate concentrations (in the Orholm sample).
It is likely that inhibition or other factors prevent growth
of
Methanosaetaceae and allow dominance by acetate oxidation
by default.
The bimodality of the system is also highlighted in Fig. 1, which shows two distinct groups, with hydrogen-utilizing methanogens (Methanobacteriales, Methanococcales, Methanomicrobiales, possibly Methanosarcinaceae, uncultured archaea [Hashøj and Lemvig], and unidentified archaea [Studsgard]) in syntrophic cooperation with acetate oxidizers at low maximum acetate removal rates and the strict aceticlastic methanogen Methanosaetaceae at maximum acetate removal rates. The presence of Methanosarcinaceae as a hydrogen-utilizing syntrophic partner in the acetate-oxidizing cultures is not surprising. In contrast to the Methanosaetaceae species, which are strict aceticlastic methanogens, most Methanosarcinaceae species are mixotrophic, utilizing not only acetate but also hydrogen and carbon dioxide, methanol, and methylamines (2). In addition, Methanosarcinaceae are capable themselves of acetate oxidation (7) and could be therefore be mediating the entire process of acetate oxidation, and subsequent methanogenesis, rather than acting as an acetate sink via aceticlastic reaction.

Methanogenic populations.
The FISH observations showed that dominant methanogenic populations
(see Figure S1 in the supplemental material) of wastewater sludge
samples were consistently
Methanosaetaceae, as previously reported
(
5), while manure samples were phylogenetically more diverse.
In every case, dominance of specific groups as observed by FISH
was clear, and they constituted more than 90% of the archaeal
population, as described previously (
5). Diversity in subdominant
methanogens was limited, except in the Orholm sample (sediment
sample), where archaea belonging to
Methanosaetaceae,
Methanomicrobiales,
and
Methanococcales were observed. Methanogenic population changes
were observed during growth on acetate in the incubations. For
the samples in which
Methanosaetaceae were dominant, the only
change observed during incubation was the elimination of subdominant
populations. In the other samples, there was a shift to known
hydrogen consumers (
Methanobacteriales,
Methanomicrobiales,
or
Methanococcales) or uncultured archaea (samples M2 and M6).
Methanogenic communities in several samples (M2 and M5 before incubation and M2 and M6 after incubation) were not identified by FISH. This was due to the limitations of visual in situ hybridization. FISH is very convenient for the rapid analysis of a large number of environmental samples but is limited when carried beyond the limits of oligonucleotide probes. ARC915 is an effective general probe, and order-level probes have been used in a wide range of systems; however, in complicated systems, such as manure, they might fail to detect all methanogens. Therefore, unidentified methanogens were phylogenetically characterized by PCR-TGGE. Samples not identified by FISH (e.g., M5, Studsgard before inoculation) were found by PCR-TGGE to be far outside known phylogenetic groupings for methanogens. It is likely that these microbes are still methanogens, since bacterial methanogenesis is unknown. These unknown microbial groups are interesting scientifically and deserve further investigation.

Nucleotide sequence accession numbers.
Sequence data for microbes identified in this study have been
submitted to the GenBank database under accession numbers DQ409324
to DQ409326.

ACKNOWLEDGMENTS
We thank Lene Kirstejn Jensen, Birthe Ebert, and Hector Garcia
for technical assistance with the experiments.
This work was supported by a Danish Government Scholarship and the Danish Research Programme (EFP 05).

FOOTNOTES
* Corresponding author. Mailing address: Institute of Environment & Resources DTU, Technical University of Denmark, Building 113, DK-2800 Kgs. Lyngby, Denmark. Phone: (45) 45251429. Fax: (45) 45932850. E-mail:
ria{at}er.dtu.dk.

Supplemental material for this article may be found at http://aem.asm.org/. 

REFERENCES
1 - American Public Health Association. 1985. Standard methods for the examination of waste and wastewater. American Public Health Association, Washington, D.C.
2 - Ferry, J. 1993. Fermentation of acetate, p. 305-334. In J. G. Ferry (ed.), Methanogenesis. Ecology, physiology, biochemistry and genetics. Chapman and Hall, New York, N.Y.
3 - Garcia, J. L., B. K. C. Patel, and B. Ollivier. 2000. Taxonomic, phylogenetic, and ecological diversity of methanogenic Archaea. Anaerobe 6:205-226.
4 - Hattori, S., Y. Kamagata, S. Hanada, and H. Shoun. 2000. Thermacetogenium phaeum gen. nov., sp. nov., a strictly anaerobic, thermophilic, syntrophic acetate-oxidizing bacterium. Int. J. Syst. Evol. Microb. 50:1601-1604.
5 - Karakashev, D., D. J. Batstone, and I. Angelidaki. 2005. Influence of environmental conditions on methanogenic compositions in anaerobic biogas reactors. Appl. Environ. Microbiol. 71:331-338.[Abstract/Free Full Text]
6 - Kelts, K. U., K. Briegel, K. Ghilardi, and K. Hsu. 1986. The limnogeology-ETH coring system. Schweitz. Z. Hydrol. 48:104-116.
7 - Lovley, D. R., and J. G. Ferry. 1985. Production and consumption of H2 during growth of Methanosarcina spp. on acetate. Appl. Environ. Microbiol. 49:247-249.[Abstract/Free Full Text]
8 - Nusslein, B., K.-J. Chin, W. Eckert, and R. Conrad. 2001. Evidence for anaerobic syntrophic acetate oxidation during methane production in the profundal sediment of subtropical Lake Kinneret (Israel). Environ. Microbiol. 3:460-470.[CrossRef][Medline]
9 - Pavlostathis, S. G., and E. Giraldo-Gomez. 1991. Kinetics of anaerobic treatment: a critical review. Crit. Rev. Environ. Control 21:411-490.
10 - Petersen, S., and B. Ahring. 1991. Acetate oxidation in a thermophilic anaerobic sewage-sludge digestor: the importance of non-aceticlastic methanogenesis from acetate. FEMS Microbiol. Ecol. 86:149-158.[CrossRef]
11 - Reichert, P. 1994. AQUASIM: a tool for simulation and data analysis of aquatic systems. Water Sci. Technol. 30:21-30.
12 - Schnurer, A., B. Svensson, and B. Schink. 1997. Enzyme activities in energetics of acetate metabolism by the mesophilic syntrophically acetate-oxidizing anaerobe Clostridium ultunense. FEMS Microbiol. Lett. 154:331-336.[CrossRef]
13 - Schnurer, A. G., G. Zellner, and B. Svensson. 1999. Mesophilic syntrophic acetate oxidation during methane formation in biogas reactors. FEMS Microbiol. Ecol. 29:249-261.[CrossRef]
14 - Speece, R. E. 1996. Anaerobic biotechnology for industrial wastewaters. Archae Press, Nashville, Tenn.
15 - Zinder, S., and M. Koch. 1984. Non-aceticlastic methanogenesis from acetate: acetate oxidation by a thermophilic syntrophic coculture. Arch. Microbiol. 138:263-272.[CrossRef]
Applied and Environmental Microbiology, July 2006, p. 5138-5141, Vol. 72, No. 7
0099-2240/06/$08.00+0 doi:10.1128/AEM.00489-06
Copyright © 2006, American Society for Microbiology. All Rights Reserved.
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