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J Bacteriol, May 1998, p. 2676-2681, Vol. 180, No. 10
0021-9193/98/$04.00+0
Copyright © 1998, American Society for Microbiology. All rights reserved.
Isolation and Characterization of Methanobacterium
thermoautotrophicum
H Mutants Unable To Grow under
Hydrogen-Deprived Conditions
Jeroen L. A.
Pennings,*
Jan T.
Keltjens, and
Godfried D.
Vogels
Department of Microbiology, University of
Nijmegen, Nijmegen, The Netherlands
Received 9 September 1997/Accepted 18 March 1998
 |
ABSTRACT |
By using random mutagenesis and enrichment by chemostat culturing,
we have developed mutants of Methanobacterium
thermoautotrophicum that were unable to grow under
hydrogen-deprived conditions. Physiological characterization showed
that these mutants had poorer growth rates and growth yields than the
wild-type strain. The mRNA levels of several key enzymes were lower
than those in the wild-type strain. A fed-batch study showed that the
expression levels were related to the hydrogen supply. In one mutant
strain, expression of both methyl coenzyme M reductase isoenzyme I and
coenzyme F420-dependent 5,10-methylenetetrahydromethanopterin dehydrogenase was impaired. The
strain was also unable to form factor F390, lending support to the hypothesis that the factor functions in regulation of
methanogenesis in response to changes in the availability of hydrogen.
 |
INTRODUCTION |
Methanobacterium
thermoautotrophicum grows on molecular hydrogen and
CO2 as its sole energy and carbon source. For several key
reactions involved in the reduction of CO2 to methane,
M. thermoautotrophicum contains two or more isoenzymes or
functionally equivalent enzymes.
The final, methane-forming step in methanogenesis is catalyzed by
methyl-coenzyme M reductase (MCR). Of this enzyme, two differentially expressed isoenzymes (MCR I and MCR II) have been found (1, 7, 8,
10, 13). Expression of MCR II is favored by conditions characterized by excess substrate or energy supply (high gassing rates,
extensive stirring), low temperature (55°C), and alkaline pH (pH 7.5)
and predominates during the exponential growth phase in a fed-batch
culture. MCR I, on the other hand, is preferentially expressed under
the opposite conditions (i.e., low gassing and fermentor impeller
speeds, high temperature [70°C], acidic pH [pH 6.5]) and
predominates in the later stages of growth (1). Differential
expression of these isoenzymes is regulated at the transcriptional
level (7, 8). Similar expression patterns have been found
for the two enzymes that are involved in the reduction of
N5,N10-methylenetetrahydromethanopterin
to
N5,N10-methylenetetrahydromethanopterin.
One of these enzymes, F420-dependent methylenetetrahydromethanopterin dehydrogenase
(F420-MDH), behaves similarly to MCR I. Expression of its
counterpart, hydrogen-using MDH (H2-MDH), proceeds
analogously to that of MCR II (7, 8). The different forms of
each enzyme appear to be genetically distinctly regulated (1, 7,
8, 10, 13, 20).
The metabolic regulation of the enzymes involved in the methanogenic
pathway has been the subject of extensive research, but these studies
have focused mainly on the connection between enzyme expression and
environmental factors such as hydrogen availability. Regulation in
response to variations in the hydrogen supply presumes the presence of
suitable (hydrogen-)sensing and signal transduction systems whose
nature is essentially unclear to us. The obvious strategy for
unraveling such systems is the isolation and characterization of
mutants that are defective in such regulation. M. thermoautotrophicum is well characterized at the DNA level.
However, the direct approach in mutant preparation by using
site-directed mutagenesis of putative regulatory elements is hampered
by the fact that transformation systems for the organism have not been
established. In addition, the more classical approach for making
mutants that are defective in hydrogen regulation by random mutagenesis
has also not been described. In the present study, we developed the
latter method by using chemostat culturing under excess-hydrogen
conditions and selection and testing of suitable clones. The results
are described herein.
 |
MATERIALS AND METHODS |
Materials.
Coenzyme F420-2 and 8-OH adenylated
F420 (factor F390) were prepared as described
previously (19). Synthetic oligonucleotide primers were from
Eurogentec (Seraing, Belgium), Hybond-N+ membranes were from Amersham
(Little Chalfont, United Kingdom), and other molecular biological
reagents were from either Boehringer (Mannheim, Germany) or Eurogentec.
Gelrite was purchased from Kelco (San Diego, Calif.). Hydrogen and
carbon dioxide gases were supplied by Hoek-Loos (Schiedam, The
Netherlands) and freed from traces of oxygen by passage over a BASF
RO-20 catalyst at room temperature. The catalyst was a gift from BASF.
All other chemicals used were obtained from Merck (Darmstadt, Germany)
or Sigma Chemical Co. (St. Louis, Mo.) and were of the highest grade
available.
Media composition.
All media employed contained the
following constituents: KH2PO4, 6.8 g/liter;
Na2CO3, 3.3 g/liter; NH4Cl, 2.1 g/liter; cysteine · HCl · H2O, 0.6 g/liter; a
0.1% (vol/vol) concentration of a trace element stock solution
(14); and resazurin (1 µg/liter) as a redox indicator. In
addition to this, standard (N) medium contained 0.6 g of
Na2S · 2H2O per liter and had a pH of
7.0; MI medium contained 0.5 g of
Na2S2O3 per liter and had a pH of 6.5; and MII medium contained 6.0 g of Tris and 0.6 g of
Na2S · 2H2O, each per liter, and had a
pH of 8.0. The pH values given are those prevailing under culturing
conditions. In the case of MI medium, the pH was adjusted with HCl
before gassing was done; no adjustment of pH was necessary for N and
MII media. To test for conditional auxotrophy, MI medium was
supplemented with 2.5% (vol/vol) sterilized cell extract prepared from
wild-type M. thermoautotrophicum. Chemostat medium was
essentially the same as MII medium but with fivefold less
NH4Cl. Fed-batch medium was the same as MII medium but
contained 0.5 g of Na2S2O3 per
liter and lacked the resazurin and Na2S · 2H2O. Solid media also contained 0.75 g of
MgCl2 · 6H2O and 8 g of Gelrite,
each per liter (6). Growth was carried out under an
H2-CO2 (80%-20% [vol/vol]) atmosphere.
Mutant isolation.
M. thermoautotrophicum
H (DSM
1053) was grown on chemostat medium in a 0.5-liter chemostat at 55°C
with a culture volume of 300 ml, a gassing rate of 12 liters/h, and
magnetic stirring at 400 rpm. The dilution rate was gradually increased
from 0.067 to 0.15 h
1. Three twice-monthly additions of
5-bromo-2'-deoxyuridine were made to a concentration of 2.5 µg/ml.
At regular times, samples were aseptically and anoxically withdrawn and
inoculated into 100-ml serum flasks containing 20 ml of either MI or
MII medium. Cultures were incubated at 68°C without further agitation
(MI medium) or in a rotary incubator (150 rpm) at 55°C (MII medium).
Growth was monitored by measuring methane production. Chemostat
culturing was continued until the samples did not show any detectable
growth on MI medium. Serial dilutions of the culture obtained were
plated on solid MII medium and subsequently incubated at 55°C in an
anaerobic jar pressurized at 0.5 bar (1 bar = 105 Pa).
Individual colonies appeared within a week and were picked and tested
for growth on plates with MII (55°C) and MI (68°C) media. Some of
the clones that grew only on solid MII medium were selected for further
study. Preliminary experiments with the wild type indicated a plating
efficiency of nearly 100% on both MI and MII media.
Physiological characterization.
Cells were grown in 100-ml
serum flasks containing 20 ml of MI, N, or MII medium, pressurized at
1.2 bars with 80% H2-20% CO2. Flasks were
incubated under stationary conditions at 68 or 55°C or in a rotary
incubator (150 rpm) at 55°C. Growth rates were determined by
measuring the methane production at regular intervals. This was done by
analyzing 0.5-ml amounts of the headspace on a Pye Unicam GCD
chromograph equipped with a Porapack Q 100/200 mesh column. Ethane was
used as an internal standard. After cessation of growth, the optical
density at 600 nm (OD600) was determined for dry weight
calculation, at which an OD600 of 1 corresponded to 325 mg
(dry weight) liter
1. All experiments were done at least
in duplicate.
Molecular characterization.
Cells of the various strains
were grown in 100-ml serum flasks on MII medium (at 55°C with
agitation). After the cells were harvested, RNA was isolated and used
for Northern and dot blot analyses essentially as described previously
(9). Digoxigenin (DIG)-labeled oligonucleotide probes
against F420-MDH, H2-MDH, MCR I, and MCR II
were made by PCR amplification of M. thermoautotrophicum DNA
by using the Boehringer PCR DIG labeling mix and oligonucleotide primers described previously (9). For Northern blot
analyses, RNA preparations and DIG-labeled DNA molecular weight marker
III (Boehringer) were subjected to glyoxal-dimethyl sulfoxide
denaturation and separated on a 1% agarose gel. After electrophoresis,
the nucleic acids were vacuum blotted onto a Hybond-N+ membrane. For dot blot analyses, serial dilutions of formaldehyde-denatured RNA
samples were spotted on the membrane. Membrane-bound RNA was hybridized
with DIG-labeled oligonucleotide probes. After autoradiography, relative amounts of the various types of mRNA were compared, using the
data obtained with the wild-type strain as a reference. The hybridization signal obtained with the 16S rRNA probe was routinely used to check if sample preparation and analyses had taken place properly.
Batch culture experiments.
Strain JB2 was cultured in a
12-liter fed-batch fermentor on 10 liters of fed-batch medium at 55°C
with gassing at 2 liters min
1 with
H2-CO2 (80%-20% [vol/vol]). Growth was
monitored by measuring the OD600. The stirring rate was
modified during growth. Samples were taken regularly from the culture;
this was followed by RNA extraction and further molecular analyses as
described above. The F420-MDH hybridization signal obtained
for the first sample was used as a reference.
Factor F390 analyses.
Serum bottle cultures were
exposed to 5% O2 for 16 h to allow factor
F390 synthesis to proceed (5), after which 1 volume of acetone was added. These mixtures were shaken for 2 h at
room temperature and centrifuged at 20,000 × g at
4°C. The supernatant, containing coenzymes, was concentrated by
rotary evaporation to a volume of 5 ml. The pH of the samples was
adjusted to 5 with 2 M acetic acid. After a brief spin to remove the
precipitate formed, the samples were desalted on a Sep-Pak
C18 cartridge (Waters Associates, Milford, Mass.),
freeze-dried, and redissolved in 1 ml of demineralized water.
Reversed-phase high-pressure liquid chromatography (HPLC) was performed
on a LiChrospher 100 RP-18 column (Merck). Forty millimolar formic acid
(pH 3.0, solvent A) and 80% methanol (solvent B) were used as solvent
systems. Subsequent to injection of the sample, the column was eluted
for 2 min with 5% solvent B, followed by a 15-min linear gradient of 5 to 60% solvent B, a 5-min wash with 60% solvent B, and a 5-min linear
gradient back to 5% solvent B. After a 5-min equilibration with 5%
solvent B, the system was prepared for a further analysis. Eluted
compounds were detected with a fluorescence detector set at an
excitation wavelength of 390 nm and an emission wavelength of 444 nm.
Retention times and UV-visible light spectra of relevant peaks were
compared to those of the coenzyme F420-2 and factor F390 standards.
 |
RESULTS |
Preparation of mutants.
For preparation of mutants of M. thermoautotrophicum that required a high level of hydrogen, we
employed the strategy of using random mutagenesis and enrichment by
chemostat culturing. The use of a chemostat allows for cultivation and
therefore selection for prolonged periods of time without much
additional work. Also, exposures to a mutagenic compound can be easily
done; after this, the compound concentration will gradually decrease
since it will wash out of the culture. The chemostat medium had a
fivefold-reduced concentration of NH4Cl to create a
situation in which hydrogen was nonlimiting for growth (9,
20). This, as well as the other conditions (high
H2-CO2 gassing rate of 12 liters/h, temperature of 55°C, pH of 8.0, sodium sulfide as the medium reductant, high dilution rate of 0.15 h
1), was used to induce selective
pressure for the type of mutants desired. To check whether we had
successfully enriched for the mutants unable to grow under
hydrogen-deprived conditions, samples were collected weekly and
incubated in two different ways. The first incubation was performed on
MII medium (pH 8.0, sulfide as the reductant), at 55°C, in a rotary
incubator to ensure high hydrogen mass transfer. This incubation
corresponds to conditions for preferential expression of MCR II and
H2-MDH (1, 7, 8, 9, 20). The other incubation
took place at 68°C on MI medium (pH 6.5, thiosulfate) with no
agitation, conditions which correspond to a low supply of hydrogen and
preferential expression of MCR I and F420-MDH (1, 7,
9, 20).
Within 2 months after the first addition of 5-bromo-2'-deoxyuridine,
the chemostat sample showed growth on MII medium only. This enrichment
culture was plated, and 20 of 74 colonies that were screened showed
growth on solid MII and not on solid MI medium. These 20 clones were
tested for reversion by repeated plating on MI plates by using a total
of 106 to 108 cells for each clone. We found
that six clones proved to be stable (i.e., did not produce any colonies
on MI medium under repeated plating experiments). These were chosen for
further study.
Physiological characterization.
The various mutant strains
showed a clear difference from the wild-type strain based on
physiological characterization (Table 1).
In general, all of the mutants grew only when incubated at 55°C in a
rotary incubator, whereas the wild-type strain showed exponential
growth under all conditions tested. This indicates that the presence of
agitation, and therefore of gas diffusion, determined whether proper
growth took place. Table 1 also shows that exponential growth took
place in strains on all three culture media when incubated at 55°C
with agitation, whereas only poor growth, if any, was demonstrated by
the mutant strains grown under stationary conditions irrespective of
the culture medium used. The growth rates of the mutant strains do not,
therefore, depend on the medium pH. Nor do they depend on the
temperature, since, of the cultures incubated at 55°C, only those
incubated in a rotary incubator showed exponential growth. Addition of
2.5% (vol/vol) sterilized cell extract to MI medium incubated under
stationary conditions at 68°C did not affect growth of the mutants,
ruling out the possibility of conditional auxotrophy. Thus, the mutant strains were mutated in such a way that they were, as intended, strongly dependent on a high supply of hydrogen.
Whenever exponential growth took place, the mutant strains grew at
rates that were generally lower than those of the wild type under
corresponding conditions. A comparison of the growth yields of the
wild-type strain grown at 55°C with agitation in the three different
media showed an increase, from MII medium to N medium to MI medium.
This increase was not observed for strains JB3, JB4, and JB5.
Especially for strains JB3 and JB4, the growth yields of the cultures
incubated on MI medium at 55°C with agitation were considerably lower
than that of the wild type.
Of all the mutant strains, strain JA1 gave the lowest growth rates. In
addition, its growth yields were also considerably lower than those of
the wild-type strain.
Molecular characterization.
RNA isolated from the various
strains grown on MII medium (at 55°C with agitation) was analyzed to
determine expression levels of the MCR and MDH isoenzymes. Since
Northern blots yielded a specific band of the desired size
(9), quantification was done routinely by using dot blots
(Fig. 1; Table
2). The wild-type strain was found to
express all four of the enzymes examined, with levels of MCR II and
H2-MDH mRNA transcripts being twofold higher than those of
their counterparts. The mRNA levels of the enzymes mentioned were
usually lower in the mutant strains than in the wild type. Also, the
ratios between both forms of MDH and MCR in the mutants were different
from those found in the wild-type strain under corresponding
conditions. Surprisingly, although the enrichment conditions used favor
expression of MCR II and H2-MDH (1, 7), some
strains had higher expression levels of MCR I or F420-MDH
mRNA than did their corresponding counterparts. No MCR I mRNA could be
detected in strain JB2 in the serum bottle cultures, nor in the
chemostat enrichment culture. Strain JA1 lacked both MCR I and
F420-MDH mRNAs. This was substantiated by mass-culturing
JA1 in a fed-batch fermentor. Both mRNA analyses and enzyme analyses,
performed as described by Vermeij et al. (20), showed MCR I
and F420-MDH to be completely absent in strain JA1, whereas
MCR II and H2-MDH were present in high levels (data not
shown).

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FIG. 1.
Dot blot analysis of MCR I mRNA levels in wild-type
M. thermoautotrophicum, the chemostat enrichment culture,
and mutant strains. Organisms were grown in 100-ml serum bottles under
MII medium conditions. The analysis was performed as described in
Materials and Methods.
|
|
Batch culture experiments.
mRNA levels were much lower in the
mutant strains isolated than in the wild type (Table 2). This could be
due to a global impairment in RNA synthesis or to an increase in RNase
activity. To exclude the possibility of a general malfunctioning in the RNA housekeeping, strain JB2 was cultured in a fed-batch fermentor. We
varied the hydrogen supply to the cells by changing the impeller speeds
(Fig. 2). Under conditions of extensive
gassing and rapid stirring (1,250 rpm) strain JB2 grew exponentially
with a doubling time (Td) of 3.5 h. mRNA
levels of H2-MDH and MCR II were now fully comparable to
those of the wild type (Td = 3 h) grown
under the same conditions. During the exponential growth phase, the mRNA level of H2-MDH clearly predominated over that of
F420-MDH. Now, MCR I mRNA transcripts could be detected,
albeit only at very low levels. A change in the stirring rate from
1,250 to 250 rpm, which causes a sudden decrease in hydrogen
availability (7), was accompanied by a sharp drop in the
growth rate. Simultaneously, F420-MDH and MCR I mRNA levels
were increased at least 20- and 40-fold, respectively, whereas
H2-MDH and MCR II mRNA levels were decreased. When the
original impeller rate (1,250 rpm) was subsequently restored, growth
resumed and the mRNAs returned to approximately their original levels.
The experiment demonstrates that the low levels of mRNA found in the
serum flask incubations (Table 2) were most likely the result of a
limitation in hydrogen mass transfer.

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FIG. 2.
Fed-batch culture of strain JB2. The cell density is
plotted against time. Changes in impeller speed are indicated by
arrows. The inset shows mRNA levels (arbitrary units) at the different
time points (A, B, and C) estimated by dot blot analyses; 1 AU is
defined as the amount of F420-MDH RNA at time point A.
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|
Factor F390 analyses.
Previous research has led to
the hypothesis that factor F390 might function as a signal
molecule of the reduction-oxidation state of the cell and as an
effector in regulation of expression (19-21). To examine
whether the mutant strains were affected in their factor
F390 synthesis, the various strains were subject to
analyses of factor F390 levels formed upon oxygen exposure. HPLC analyses (Fig. 3) revealed that most
of the strains obtained were capable of forming factor
F390. No significant variation in factor F390
levels was found among most of the strains, with the exception of
strain JA1. In this strain, factor F390 remained absent. In
agreement herewith, no factor F390 synthetase activity could be detected in cell extract from strain JA1 mass cultured in a
fed-batch fermentor.

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FIG. 3.
HPLC analyses of coenzyme extracts. (A) Wild-type
M. thermoautotrophicum; (B) strain JA1. Cofactor isolation
and HPLC analyses were performed as described in the text. The
chemostat enrichment culture and the other mutant strains showed
patterns similar to that in panel A.
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|
 |
DISCUSSION |
Methanogenic members of the domain Archaea respond in a
number of ways to changes in the supply of the energy source hydrogen. It has been known for quite some time that hydrogenotrophic
methanogens, including M. thermoautotrophicum, the organism
used in this study, partly uncouple growth from methane formation under
conditions of high hydrogen availability (3, 7, 15, 17). In
other words, growth yields tend to increase under hydrogen limitation. The rationale behind the hydrogen-dependent coupling and uncoupling is
not understood. In addition, M. thermoautotrophicum appears to contain sets of isoenzymes and functionally equivalent enzymes in
the central methanogenic pathway that are differentially expressed in
response to variations in the hydrogen supply, in particular MCR I, MCR
II, F420-MDH, and H2-MDH (7, 8, 10,
20). The differential expression is enhanced by other factors
like the growth temperature, the medium pH, and the nature of the
medium reductant (1, 9). It may be noted that the
temperature and medium pH are, to an extent, related to the hydrogen
potential. The solubility of the gas will be lower at higher
temperatures. Moreover, according to the Nernst equation, the reducing
power of hydrogen will depend on the pH (and temperature).
The complex adaptations described above presume the existence of a
global regulatory mechanism or the presence of specific, cooperatively
acting regulatory systems, whose nature(s) is still unknown. To
elucidate the mechanism(s) underlying regulation of methanogenesis,
mutants are indispensable. The aim of the present study was to develop
a method for obtaining mutants that are defective in this regulation,
in particular, mutants that had lost the ability to adapt to
hydrogen-limited conditions. The method consisted of random
mutagenesis, enrichment by chemostat culturing under the selective
pressure of excess-hydrogen (MCR II) conditions, and subsequent
selection of suitable clones on solid media. The reasoning behind the
approach was the following. Mutants that due to modification of a
regulatory element(s) fail to express, or that more or less completely
down-regulate, the type of enzymes that are specifically required under
hydrogen limitation (e.g., MCR I, F420-MDH) have a
selective advantage over the wild type expressing those enzymes to some
basic levels: no (or limited) energy has to be invested in their
synthesis. An even minimal selective advantage is fully exploited
during prolonged continuous culturing at high dilution rates. The
consequence is that the mutants have to lose their ability to grow
under low-hydrogen conditions.
By the method outlined, a number of stable mutants were obtained that,
indeed, strictly required a high level of hydrogen for exponential
growth. If this condition was not met by agitation of the cultures, no
or only slow linear growth occurred. Another characteristic of the
mutants was that if growth was permitted under hydrogen-limited
conditions, their growth yields were significantly reduced (Table 1).
Yields were especially low during stationary incubation at 68°C in MI
medium, which represents the most hydrogen-limiting situation. In
contrast, growth yields of wild-type M. thermoautotrophicum increase under hydrogen limitation (3, 7, 15, 17;
also this study). The mutant strains, thus, at least seem to be
affected in the (regulation of) coupling between growth and
methanogenesis.
The finding that the mutants were unable to grow or to form
methane under hydrogen limitation could imply that they lacked the appropriate methanogenic enzymes, notably, MCR I and
F420-MDH. This idea is only partially supported by mRNA
analyses (Table 2). In all except one of the mutants, MCR I and
F420-MDH transcripts could be detected. Strain JB2, for
example, which was able to down-regulate MCR I far below the levels of
the wild type (Table 2), dramatically increased the mRNA levels of this
enzyme and of F420-MDH in response to hydrogen limitation
(Fig. 2). A comparison of the wild type and the mutants shows
remarkable differences with respect to the contents and ratios of both
MCRs and MDHs, indicating that the regulation of expression in the
mutants was modified to an extent. The presence, however, of MCR I and
F420-MDH does not offer an explanation for why the
organisms were unable to grow under low-hydrogen conditions.
The most notable mutant is JA1. This strain showed only poor growth and
poor growth yields. In addition, both F420-MDH and MCR I
were absent, while the organism contained H2-MDH and MCR II. The absence of F420-MDH and MCR I represents, to our
knowledge, the first example of mutagenic defects in the methanogenic
machinery. Previous research involving mutants of methanogenic bacteria
has been mainly restricted to auxotrophic mutants or resistance to antibiotics (4, 11, 16). The combination of defects suggests that the mutation must be located in a common regulatory element. Interestingly, strain JA1 was also unable to form factor
F390. This factor has been suggested to act as a signal
metabolite for hydrogen limitation and to operate in the regulation of
expression (19-21). It may be noted that factor
F390 is found in members of distantly related lineages like
the families Methanobacteriaceae and the
Methanosarcinaceae but is absent in members of the family Methanococcaceae, which represents a separate and very
ancient branch within the methanogens (2, 5, 12, 18). The
findings here that strain JA1 lacks the ability to synthetize factor
F390 and fails to express both F420-MDH and MCR
I lend further support to the hypothesis described above that the
compound is involved in the regulation of hydrogen-dependent
methanogenesis. However, this may be a partial answer to the regulation
phenomenon. Additional or alternative mechanisms cannot be ruled out,
especially in methanogens that lack factor F390.
 |
ACKNOWLEDGMENTS |
The investigations of J.L.A.P. were supported by the Life
Sciences Foundation, which is subsidized by the Netherlands
Organization for Scientific Research (NWO).
 |
FOOTNOTES |
*
Corresponding author. Mailing address: Department of
Microbiology, Faculty of Science, University of Nijmegen, Toernooiveld 1, NL-6525 ED Nijmegen, The Netherlands. Phone: 31-24-3653219. Fax:
31-24-3553450. E-mail: pennings{at}sci.kun.nl.
 |
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J Bacteriol, May 1998, p. 2676-2681, Vol. 180, No. 10
0021-9193/98/$04.00+0
Copyright © 1998, American Society for Microbiology. All rights reserved.
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