Biochemical Engineering Division,
Gesellschaft für Biotechnologische Forschung mbH, 38124 Braunschweig, Germany
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INTRODUCTION |
Azotobacter vinelandii is
an N2-fixing bacterium commonly found in soil. The
biological fixation of dinitrogen depends on the activity of the highly
oxygen-sensitive nitrogenase enzyme complex (25). Despite
this sensitivity, species of the diazotrophic azotobacters are able to
grow under fully aerobic conditions (9, 26, 33). For the
survival of these bacteria under aerated conditions, one of the
priorities of their entire metabolism is to protect the active
nitrogenase from being damaged by oxygen. Protection of this enzyme
from oxygen has been proposed to occur in azotobacters mainly through
two mechanisms: (i) high respiratory activity that removes oxygen
already at the cell surface and (ii) reversible conversion of the
enzyme into a protected inactivated state (24, 26, 29). The
first mechanism is believed to explain the function of nitrogenase when
cells grow diazotrophically in the presence of O2. The
second mechanism is considered to be used to protect the reversibly
inactivated enzyme from O2 damage when the respiratory
protection becomes overburdened, such as with a sudden increase in the
ambient O2 concentration (21, 25) or under
conditions of phosphate limitation (43). In the latter case,
the respiration rate of cells is limited due to shortage of phosphate
for the oxidative phosphorylation. For growing cells which need an
active nitrogenase system to provide their nitrogen requirement, the
second protection mechanism can work only temporarily because it does
not remove O2.
Although the respiratory-protection hypothesis is generally accepted,
Post et al. (33) and Boiardi (3) have questioned it. Those authors found that at O2 concentrations ranging
from 30 to 100% air saturation, A. vinelandii showed almost
constant respiration rates and negligible decreases in nitrogenase
activity. These results are incompatible with the concept of
respiratory protection. Post et al. (32) observed a decrease
in the cellular surface area per cell volume at elevated O2
levels and suggested that this decrease of cell surface may also
provide some protection for the nitrogenase. In addition, it was
postulated that the energy efficiency of respiration is more important
than the respiration rate as a protective mechanism (18).
A. vinelandii is known to produce alginate under aerobic
conditions (1, 2, 7, 8, 16, 19). The formation of alginate
is strongly affected by oxygen tension, especially in nitrogen-free
medium and with limited phosphate (17, 38). A possible link
between alginate formation and protection of nitrogenase in this
organism has not been examined so far in the literature. Studies of the
nitrogenase protection mechanisms of Azotobacter have mostly
been based on either the respiration rates or acetylene reduction
measurements as indications of nitrogenase activity (25, 26,
29). In fact, the biological function of alginate formation in
bacteria is not fully understood. Alginate is important for cyst
formation in A. vinelandii as a coating protective
polysaccharide material (30, 36, 39). This was evidenced by
the fact that noncapsulate mutants of A. vinelandii 12837 were unable to form cysts (11). Such a coating protects the
cells from desiccation and mechanical stress. Under favorable growth
conditions, the coat swells and the cyst germinates, divides, and
releases a vegetative cell. However, the formation of a cyst in
A. vinelandii does not explain the formation of alginate by
vegetative cells under conditions not favoring encystment (7,
41).
For the protection of nitrogenase in nitrogen-fixing microorganisms, a
low intracellular oxygen concentration is essential (29,
33). For A. vinelandii the increase of viscosity of
the culture broth during the course of a cultivation as a result of increasing biomass and alginate concentrations can reduce the oxygen
transfer rate from the gas phase to the aqueous phase and from the bulk
liquid to the cell surface. To avoid a high oxygen transfer rate into
the cell, an effective oxygen barrier on the cell surface can be even
more important. As a matter of fact, the present communication provides
evidence for the importance of alginate capsule formation on the cell
surface for the survival of diazotrophically growing A. vinelandii under aerobic conditions. Variations in the quantity
and quality of the alginate produced are studied under different
culture conditions. Based on the experimental results, a new protection
mechanism for nitrogenase against oxygen is proposed.
 |
MATERIALS AND METHODS |
Microorganism and cultivation conditions.
A.
vinelandii (DSMZ 93-541b, a capsulated nonflagellated strain) was
grown under conditions of dinitrogen fixation. The composition of the
medium per liter of deionized water was as follows: sucrose, 20 g;
MgSO4 · 7H2O, 0.4 g; NaCl, 0.4 g; CaCl2 · 2H2O, 84 mg;
NaMoO4 · 2H2O, 2 mg;
FeSO4 · 7H2O, 6 mg;
H3BO4, 2.9 mg; CoCl2, 1.2 mg; CuSO4 · 5H2O, 0.1 mg;
MnCl2 · 4H2O, 0.09 mg;
ZnSO4 · 7H2O, 1.2 mg;
KH2PO4, 20 mg/liter; and
K2HPO4, 80 mg/liter. Sucrose,
MgSO4, CaCl2, and the phosphate mixture were
separated from the other medium components during sterilization.
FeSO4 solution was sterilized by filtration using a
0.2-µm-pore-size Millipore filter.
Bioreactor and control.
Cultivations were carried out in a
5-liter stirred tank bioreactor (B. Braun Biotechnology, Melsungen,
Germany) with a working volume of 2.5 liters. The control of the volume
was realized by using a balance connected to a real-time operating
computer system, UBICON (Universal Bioprocess Control System; GBF,
Braunschweig, Germany). The reactor was equipped with pH, temperature,
antifoam, and agitation speed controls.
The bioreactor was aerated with a fine-pore gas distributor. Thermal
mass flow meters and controllers were used for the supply of gasses.
The total aeration rate was controlled at a constant value (2 liters/min) with UBICON. The dissolved oxygen tension (partial
O2 pressure [pO2]) was controlled in the
range of 1% ± 1% to 20% ± 1% air saturation by mixing nitrogen
and air in the inlet gas by a proportional-integral controller defined
by the UBICON facilities. The agitation speed was 500 rpm if not otherwise stated.
The oxygen uptake rate, carbon dioxide production rate, and respiratory
quotient (the carbon dioxide production rate divided by the oxygen
uptake rate) were determined by online measurements of O2
and CO2 in the exit gas and compared with measurements
taken at the inlet gas flow rate. Paramagnetic oxygen analyzers (OXYGOR 6N; Maihalk, Hamburg, Germany) and infrared carbon dioxide analyzers (UNOR 6N; Maihalk) were used for CO2 and O2 measurement.
Analytical methods.
Biomass and alginate dry weight were
determined by gravimetrical methods as follows. One milliliter of 0.5 M
EDTA-sodium salt and 0.5 ml of 5 M NaCl were added to a 25-ml sample
of culture broth to separate the capsular alginate. After being stirred
for 5 min, the sample was centrifuged at 38,000 × g
and 20°C for 30 min to precipitate the cells. The cells were washed
twice with distilled water, recentrifuged, and then dried at 80°C for
24 h. The supernatant was cooled, and alginate was then
precipitated by the addition of 3 volumes of ice-cold isopropanol,
which was then recovered by centrifugation at 38,000 × g at 4°C for 30 min. The precipitate was dissolved in water,
precipitated again, centrifuged, and then finally dried at 80°C for
24 h. For each determination, at least two samples were used.
The poly-
-hydroxybutyrate content of cells was determined according
to the method of Senior et al. (40). Sucrose was determined with the test kit combination of Boehringer (Mannheim, Germany). Phosphate was determined colorimetrically by the method of Boltz (4). The ratio of L-guluronic acid to
D-mannuronic acid (G/M ratio) was estimated by colorimetric
reaction of carbazole according to the method of Knutson and Jeanes
(20).
The relative molecular weight of alginate was determined by gel
permeation-high-pressure liquid chromatography as follows (15). The mobile phase used was 0.1 M phosphate buffer (pH
6.9), which was applied to two TSK gel columns (TSK G6000PWHR and then TSK G5000PWHR) arranged in rows. The signal was detected by a differential refractive index detector (Beckman model 156). The columns
were calibrated with broad dextran standards. Before being applied to
the columns, the alginate samples (0.5 g/liter) were prepared with
purified alginate in the same elution buffer and filtered through a
1.2-µm-pore-size Millipore membrane to remove cellular debris.
The morphologies of cells and capsules were routinely examined by
negatively staining the cells with 7% (wt/vol) aqueous nigrosin; the
diameters of cells and capsules were then determined through visualization by dark-phase microscopy. Diameters of the cells were the
means of those of at least 15 to 20 cells. The results agreed
satisfactorily with those from later examination with a computer-aided
image analyzing system from Zeiss.
Electron microscopy.
Transmission electron microscopy was
used to investigate the surface view of alginate around the cells by
negative staining. Samples were picked up with carbon-coated collodion
grids (300 mesh, Cu). The grids were blotted with filter paper, and
alginate was positively contrasted by incubation on freshly prepared
1% aqueous ruthenium red solution for 1 to 2 min at room temperature. The grids were washed three times with distilled water, with care being
taken not to let the surface become dry. Finally, the cells were
negatively stained with 1% uranyl acetate for 10 s, blotted, and
air dried. Electron microscopy was done with a Zeiss CEM 902 microscope
set at 80 kV with a magnification between ×16,000 and ×25,000.
Embedding and ultrathin sectioning of A. vinelandii were
done as follows. Cells were preincubated in 0.5% (wt/vol) ruthenium red for 30 min at ambient temperature in the growth medium. Fixation was done by addition of 25% (vol/vol) glutardialdehyde to a final concentration of 1.25% (vol/vol) for 72 h at ambient temperature, followed by fixation at 4°C. After centrifugation, the fixed cells were resuspended in 0.1 M cacodylate buffer (pH 7.2) and washed in
three sedimentation-resuspension cycles for 10 min each at room
temperature. Washed cells were immobilized in 0.1 M cacodylate (pH
7.2)-buffered 2% (wt/vol) agar and were finally fixed with 1%
(wt/vol) OsO4-0.1 M cacodylate (pH 7.2) overnight at
4°C. Cells were dehydrated on ice with an acetone series and embedded
in epoxy resin (42). Ultrathin sections (120-nm thickness)
were poststained with lead citrate, according to the method of Reynolds (35), and were analyzed with a Zeiss model CEM 902 transmission electron microscope set at 80 kV in the primary
magnification range of ×12,000 to ×20,000.
 |
RESULTS |
Specific rates of oxygen consumption and alginate formation and
quality as functions of pO2 in phosphate-limited continuous
culture.
To gain better insight into the inhibitory effect of
oxygen on nitrogenase activity and cell growth and to examine their
relationships with alginate biosynthesis, the respiratory activities of
cells were impaired through phosphate limitation in chemostat culture at different pO2 values over a dilution rate (growth rate)
range of 0.08 to 0.26 h
1. The results of cell growth and
the specific O2 consumption rate (i.e., respiratory rate)
are shown in Fig. 1. Biomass
concentrations showed maxima as a function of pO2 level
except at the highest dilution rate (D = 0.26 h
1)
studied. At high levels of pO2, biomass concentration
declined, confirming an inhibitory effect of O2 on
nitrogenase activity. Unlike cell growth, the specific rate of oxygen
consumption (oxygen quotient [qO2]) increased as
pO2 was elevated from 1 to 5% air saturation but remained
essentially constant when pO2 was above about 5%. In
general, qO2 was higher at higher growth rates. The initial
increase of qO2 with pO2 is consistent with
results expected from study of the respiratory protection mechanism.
However, the behavior of the cells above a pO2 level of 5%
cannot be explained by this mechanism. The leveling off of
qO2 is not due to saturation of the respiratory capacity,
as evidenced by the increase of qO2 with growth rate at
both low and high pO2 levels. Consistent with the
observations of Post et al. (33) and Boiardi (3),
these results suggested that respiration is not the prevailing
mechanism for protecting oxygen inhibition of nitrogen fixation and
hence of cell growth under the experimental conditions.

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FIG. 1.
Effect of O2 tension (percentage of air
saturation) on the biomass production (A) and the specific respiration
rate (qO2) (B) of A. vinelandii in
phosphate-limited chemostat culture at different dilution rates (D).
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As mentioned in the introduction, the formation of alginate may be
involved in the protection of nitrogenase. To test whether alginate
production is up-regulated by increasing oxygen concentration, the
specific formation rate of alginate (qalg) was examined
(Fig. 2). Like biomass concentration,
qalg showed a maximum as a function of pO2. At
pO2 values above 5%, qalg decreased with
increasing pO2. On the other hand, qalg
increased with increasing growth rate. The effect of pO2 on
the formation rate of alginate in continuous culture is in agreement
with the results from pO2-controlled batch cultures with
the same strain (38). Taken together, these results are
useful for the optimization of the alginate production process. However, for understanding the role of alginate formation in the regulation of nitrogen fixation and cell growth, knowing the alginate concentration or formation rate alone is obviously not sufficient.

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FIG. 2.
Specific alginate production rate (qalg) of
A. vinelandii as a function of O2 tension in
phosphate-limited continuous culture at different dilution rates (D).
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Therefore, the quality of alginate produced at different dissolved
oxygen tensions was further examined in terms of molecular weight and
alginate composition. The results are depicted in Fig. 3. It was interesting that both the
molecular weight and the L-guluronic acid content
monotonically increased with pO2. Unlike with the specific
rates of oxygen consumption (Fig. 1) and alginate formation (Fig. 2),
the effect of growth rate on the L-guluronic acid content of alginate was not significant. These results revealed that it is
obviously the quality, not the quantity, of alginate that is the better
determinant for the protection of nitrogenase in A. vinelandii.

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FIG. 3.
Changes in the molecular weight (at a D of 0.08 h 1) (A) and the L-guluronic acid content (B)
of alginate produced at different pO2 values. Molecular
weight was based on a dextran standard.
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Effect of shear rate on alginate capsule formation under a
controlled pO2 value.
Based on observations of
capsulated cells in a diazotrophically growing culture of A. vinelandii (38) and in view of the importance of
alginate quality in coping with oxygen stress, as pointed out above,
the formation of an alginate capsule and its quality were further
studied with an elevated shear rate in a bioreactor. Figure
4 shows the results from a
phosphate-limited continuous culture at different agitation speeds (300 to 1,000 rpm) with a controlled pO2 value (5% air
saturation) and a fixed dilution rate of 0.15 h
1. Both
alginate and biomass concentrations first increased with the agitation
speed (up to 600 rpm) and then dropped. Alginate yield on biomass also
reached a maximum at an agitation speed of 600 rpm. On the other hand,
the L-guluronic acid content in alginate increased with
increasing agitation speed and seemed to reach a saturation value of
about 35 to 40%, which is typical for the pO2 value (see
also Fig. 3).

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FIG. 4.
Effect of agitation speed on the biomass production and
the concentration, yield, and composition (expressed as weight
percentages of L-guluronic acid content) of alginate in a
phosphate-limited chemostat culture with a pO2 of 5% air
saturation and a D of 0.15 h 1.
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Microscopic examination of the cells revealed that the higher the shear
rate, the smaller the average cell surface area (and also diameter),
which reached a minimum of 8.9 µm2 at 800 rpm compared to
the minimum of 33.8 µm2 reached at 300 rpm (Fig.
5). A decrease in the cellular surface area per cell volume, which was proposed by Post et al. (32) as a nitrogenase protection mechanism against oxygen, is clearly not
involved in our culture system. In fact, the specific surface area per
cell volume increased in this case.

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FIG. 5.
Cell and capsule area (A) and specific capsule formation
(B) as a function of the agitation speed (culture conditions were as
described in the legend to Fig. 4). Specific capsule formation = capsule area/cell area; capsule area = area of capsule, including
the cell cell area.
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Surprisingly, even in the presence of a high level of mixing intensity
(800 to 1,000 rpm), capsules were always observed around the
diazotrophically grown cells. The specific capsule area (capsule area/cell area) increased with agitation speed up to 600 rpm as shown
in Fig. 5. The presence of a capsule around the cell, even during
growth at a high shear rate in an agitated bioreactor, indicates how
important the alginate capsules are for the survival of
diazotrophically growing cells under phosphate limitation. Moreover,
the results shown in Fig. 4 and 5 are consistent with those shown in
Fig. 2 and 3 in the sense that they also suggest that not only the
quantity but also the quality of the alginate (capsule) seems to be
important for coping with the oxygen stress caused by high turbulence.
In this connection, it is reasonable to assume that the effective
pO2 value on the cell surface is higher at higher agitation
speeds due to reduced O2 transfer resistance in the bulk
liquid and a thinner liquid film and/or alginate capsule on the cell surface.
Morphological and ultrastructural variations of the alginate
capsule.
To gain more information on the development and quality
of the alginate capsule, an O2-controlled chemostat culture
of A. vinelandii was studied at a low pO2 value
(2.5% air saturation) and at a relatively high pO2 value
(20% air saturation). Transmission electron microscopy was used to
investigate the appearance of the alginate layer around the negatively
stained vegetative cell in a surface view as well as in thin sections.
Surface view micrographs of vegetative cells at both pO2
values showed a net-structured polysaccharide capsule around the cell
(Fig. 6). However, the polysaccharide
structure differed distinctly by forming filamentous structures
radiating from the bacterial surface at the low pO2 value
(2.5% air saturation), while a compact dense layer of capsular polysaccharide was generated at a pO2 of 20%, which
totally covered the cell surface.

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FIG. 6.
Surface view electron micrographs of A. vinelandii cells grown at 2.5 and 20% air saturation in a
phosphate-limited chemostat. PHB, poly- -hydroxybutyrate.
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Electron micrographs of negatively stained A. vinelandii
cells seen in ultrathin sections are shown in Fig.
7. A. vinelandii cells grown
diazotrophically at pO2 values of 2.5 and 20% formed capsules with significant differences in the thickness and compactness of the polysaccharide materials. These differences in the
polysaccharide structure are also reflected by large variations in the
G/M ratio of alginate around the cells. The G/M ratios of alginate
formed were determined to be 45 and 88% for the pO2 values
of 2.5 and 20%, respectively.

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FIG. 7.
Thin section of negatively stained A. vinelandii cells grown at low and high pO2 values in a
phosphate-limited chemostat.
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 |
DISCUSSION |
The results presented in this work clearly showed that the
respiratory protection of nitrogenase against oxygen stress, a widely
accepted conjecture in the literature for nitrogenase protection in
nitrogen-fixing bacteria, is not the prevailing mechanism involved in
diazotrophically growing A. vinelandii in phosphate-limited culture (Fig. 1). This conclusion is in agreement with the results of
Post et al. (33) and Boiardi (3). Other possible
mechanisms such as reversible conversion of nitrogenase into a
protected inactivated state and reduction of cell-specific surface area cannot explain our experimental results either. These facts and the
observations of alginate formation, its variation in quality, and
especially the varied morphology of the alginate capsule on the cell
surface strongly suggested that the formation of alginate (capsule)
plays an important role in overcoming oxygen stress and regulating the
nitrogenase activity and hence the growth of A. vinelandii,
particularly under phosphate-limited conditions. This conclusion is
also supported by several other previous observations: (i) the
production of alginate takes place mainly in the phosphate-limited phase in batch culture (38), (ii) growth in the presence of ammonium (the final product of nitrogen fixation) inhibits alginate formation in A. vinelandii (5, 37), and (iii)
alginate production is stimulated under conditions of limited synthesis
of nitrogenase caused by limitation of either molybdate or iron
(1, 10; N. F. Ferrala, P. Westervelt, G. A. Mabbott, and F. A. Fekete, Abstr. Annu. Meet. Am. Soc.
Microbiol. 1986, abstr. K-143, 1986). This increased formation of
alginate can better protect the activity of the synthesized nitrogenase
and thus compensate for the limitation of molybdate and/or iron to a
certain extent.
The protective role of alginate has also been demonstrated for
Pseudomonas aeruginosa with respect to growth stresses
caused by antibiotics, virulent phages, and metal toxicity (13,
23). However, for A. vinelandii and P. aeruginosa, the mechanisms by which alginate exerts its protective
role are so far not well understood. We have shown in this work that
alginate production does not linearly increase with increasing
pO2 (Fig. 2). A similar trend was observed for A. vinelandii growing at an increased shear rate (Fig. 4). These
results suggested that alginate formation alone cannot explain the
experimental observations. We therefore looked at the quality of
alginate by measuring the molecular weight and L-guluronic
acid content of alginate released into the culture and the morphology,
thickness, and compactness of the alginate capsule on the cell surface.
The molecular weight of alginate increased monotonically with increased
pO2 (Fig. 3). It is understood that the increase of
molecular weight increases the viscosity of the culture broth and hence
reduces oxygen transport. The high molecular weight may also increase
the density of the alginate capsule on the cell surface. For the
barrier effect of alginate against O2, its guluronic acid
content may play an even more important role. As shown in Fig. 3 and 4,
the guluronic acid content of alginate increased significantly under
both oxidative and shear force stresses. It is known that increasing
the L-guluronic acid fraction of the alginate tends to lead
to the formation of dense gels through a characteristic interaction
between alginate chains, according to the so-called egg-box model
(44), but that alginate with a high D-mannuronic
acid content forms only soft gels with a lower affinity for chain
binding (28). These findings may well explain the formation
of filamentous and loosely structured alginate at a low pO2
(2.5% air saturation), in contrast to the dense and compact alginate
that forms at a high pO2 (20% air saturation) (Fig. 6 and
7). Alginate formed at a pO2 of 2.5% had a much lower L-guluronic acid content (45%) than alginate formed at a
pO2 of 20% (88% of L-guluronic acid). In this
connection, it is interesting that the calcium content of the medium
may also affect the quality of the alginate capsule. It is the calcium
alginate gel that is postulated to have the egg-box-like structure.
Taken together, the results presented in this work allow us to draw the
conclusion that it is the quality, not the quantity, of alginate
that is decisive for the protection of nitrogenase against oxygen for
diazotrophically growing A. vinelandii in phosphate-limited culture. The formation of alginate and, above all, the variation of its
quality and structure seem to help maintain the intracellular oxygen
concentration at a level low enough for an effective nitrogenase system. With the determinant role of alginate quality in mind, we may
now also understand the occurrence of an optimal formation rate of
alginate at pO2 levels between 2.5 and 5% (Fig. 2) and at
an intermediate agitation speed (Fig. 4). Obviously, at high levels of
oxygen stress, cells tend to produce an alginate as the capsule on the
cell surface that is more compact and has a greater guluronic acid
content at the expense of release of alginate into culture broth. In
this connection, it is worth mentioning that the formation of a compact
slime layer or capsule on the cell surface is not common for other
polysaccharide-producing bacterial strains under highly turbulent
conditions in a bioreactor, as was discussed by Peters et al.
(31) for the formation of xanthan by Xanthomonas
campestris and by Lobas et al. (27) for the production
of gellan by Sphingomonas paucimobilis. Both X. campestris and S. paucimobilis are
non-O2-sensitive strains and form no slime layer at high
shear rates. These findings underline again the importance of the
alginate capsule for the survival of A. vinelandii under
particular growth conditions.
Of course, the respiratory protection and enzyme conversion mechanisms
may still be involved in A. vinelandii, especially in
nonslimy variants (6), but do not play a decisive role under the experimental conditions considered in this work. The overall mechanisms for the protection of nitrogenase against O2 in
A. vinelandii are schematically shown in Fig.
8. Depending on the growth conditions,
the relative importance of the different protection mechanisms may
vary.

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FIG. 8.
Summation of protection mechanisms for nitrogenase
against O2 in A. vinelandii. The formation of a
compact alginate capsule is proposed in this work as the decisive
protection mechanism for A. vinelandii grown under
phosphate-limited conditions.
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It should be mentioned that several questions related to the formation
of alginate and its role in A. vinelandii remain to be
answered. It is not known, for example, if the alginate capsule represents also a strong barrier for the transport of other essential nutrients necessary for growth. Such a barrier effect may explain the
observed decline of biomass concentration in our culture (Fig. 1). An
earlier study showed that free alginate in medium limits the diffusion
of O2 in culture of P. aeruginosa, thereby
restricting its growth (14). It is, however, also possible
that the protection of nitrogenase by the formation of alginate has its
limitation at relatively high pO2 levels and that the
activity of nitrogenase will still be impaired, leading to a decrease
in cell growth. To address this issue, a measurement of intracellular
oxygen concentration and a quantitative knowledge of the sensitivity of
nitrogenase toward oxygen are necessary. From fundamental and
application points of view, it is also important to ask the question of
how the quantity and quality of alginate at different O2
concentration are regulated at physiological and genetic levels. Oxygen
concentration can regulate several alginate biosynthetic enzymes and
genes (22). From our results, an oxygen-dependent
up-regulation of epimerase enzymes and especially of the gene
algE2, which is responsible for introducing guluronic acid
blocks into alginate, may be inferred since compact alginate with a
high guluronic acid content was characteristic at high pO2
values (Fig. 6). Answers to these questions and the possibility of
physiologically and genetically altering alginate synthesis and its
quality will certainly help to improve the microbial production of
alginate, which is of increasing industrial interest (12,
34).
We thank G. Skjak-Braek for supplying alginate samples with
different G/M ratios. We also thank T. Gäbel for the excellent assistance with the computer control system UBICON.
W. A. Sabra gratefully acknowledges financial support by DAAD.
| 1.
|
Annison, G., and I. Couperwhite.
1986.
Effect of limiting substrate concentration, growth rate and aeration on alginate composition and production by Azotobacter vinelandii in continuous culture.
Food Hydrocoll.
1:101-111.
|
| 2.
|
Annison, G., and I. Couperwhite.
1986.
Influence of calcium on alginate production and composition in continuous cultures of Azotobacter vinelandii.
Appl. Microbiol. Biotechnol.
25:55-61.
|
| 3.
|
Boiardi, J. L.
1994.
Metabolic cost of nitrogen incorporation by N2-fixing Azotobacter vinelandii is affected by the culture pH.
Biotechnol. Lett.
16:1195-1198[CrossRef].
|
| 4.
|
Boltz, D. F.
1972.
Total phosphorus, p. 1-31.
In
M. H. Holmann (ed.), Analytical chemistry of phosphorus compound. H. Wiley Interscience, New York, N.Y.
|
| 5.
|
Brivonese, A., and W. I. Sutherland.
1989.
Polymer production by a mucoid strain of Azotobacter vinelandii in batch culture.
Appl. Microbiol. Biotechnol.
30:97-102.
|
| 6.
|
Bush, J. A., and P. W. Wilson.
1959.
A non-gummy chromogenic strain of Azotobacter vinelandii.
Nature
184:381.
|
| 7.
|
Clementi, F.
1997.
Alginate production by Azotobacter vinelandii.
Crit. Rev. Biotechnol.
17:327-361[Medline].
|
| 8.
|
Deavin, L.,
T. R. Jarman,
C. J. Lawson,
R. C. Richelato, and S. Slocombe.
1977.
The production of alginic acid by Azotobacter vinelandii in batch and continuous culture, p. 14-26.
In
P. A. Sanford, and A. Laskin (ed.), Extracellular microbial polysaccharides. American Chemical Society, Washington, D.C.
|
| 9.
|
Drozd, J., and J. R. Postgate.
1970.
Effect of oxygen on acetylene reduction, cytochrome content and respiratory activity of Azotobacter chroococcum.
J. Gen. Microbiol.
63:63-73[Medline].
|
| 10.
|
Duyvis, M.,
H. Wassink, and H. Haaker.
1998.
Nitrogenase of Azotobacter vinelandii: kinetic analysis of the Fe protein redox cycle.
Biochemistry
37:17345-17354[CrossRef][Medline].
|
| 11.
|
Fyfe, J. A. M., and J. R. W. Govan.
1983.
Synthesis, regulation and biological function of bacterial alginate.
Prog. Ind. Microbiol.
18:45-83.
|
| 12.
|
Gacesa, P.
1998.
Bacterial alginate biosynthesis recent progress and future prospects.
Microbiology
144:1122-1143.
|
| 13.
|
Govan, J. R. W.,
J. A. M. Fyfe, and T. R. Jarman.
1981.
Isolation of alginate producing mutants of Pseudomonas fluorescens, Pseudomonas putida and Pseudomonas mendocina.
J. Gen. Microbiol.
125:217-220[Medline].
|
| 14.
|
Hassett, D. J.
1996.
Anaerobic production of alginate by Pseudomonas aeruginosa: alginate restricts diffusion of oxygen.
J. Bacteriol.
178:7322-7325[Abstract/Free Full Text].
|
| 15.
|
Herbst, H.,
U. H. Peters,
S. I. Suh,
A. Schumpe, and W.-D. Deckwer.
1988.
Monitoring xanthan quality during fermentation by size exclusion chromatography.
Biotechnol. Tech.
2:101-104.
|
| 16.
|
Horan, N. J.,
T. R. Jarman, and E. A. J. Dawes.
1981.
Effect of carbon source and inorganic phosphate concentration on the production of alginic acid by a mutant of Azotobacter vinelandii and on the enzyme involved in its biosynthesis.
J. Gen. Microbiol.
127:185-191.
|
| 17.
|
Horan, N. J.,
T. R. Jarman, and A. J. Dawes.
1983.
Studies on some enzymes of alginic acid biosynthesis in Azotobacter vinelandii grown in continuous culture.
J. Gen. Microbiol.
129:2985-2990.
|
| 18.
|
Iwahashi, H., and J. Someya.
1992.
Oxygen sensitivity of nitrogenase is not always a limiting factor of growth under nitrogen fixing conditions in Azotobacter vinelandii.
Biotechnol. Lett.
14:227-232[CrossRef].
|
| 19.
|
Jarman, T. R.
1979.
Bacterial alginate synthesis, p. 35-50.
In
U. S. Barkeley (ed.), Microbial polysaccharides and polysaccharases. Academic Press, London, United Kingdom.
|
| 20.
|
Knutson, C. A., and A. Jeanes.
1968.
Determination of the composition of uronic acid mixtures.
Anal. Biochem.
24:482-490[CrossRef][Medline].
|
| 21.
|
Kuhla, J., and J. Oelze.
1988.
Dependence of nitrogenase switch-off upon oxygen stress on the nitrogenase activity in Azotobacter vinelandii.
J. Bacteriol.
170:5325-5329[Abstract/Free Full Text].
|
| 22.
|
Leitäo, J. H., and I. Sä- Correia.
1997.
Oxygen dependent upregulation of transcription of alginate genes algA, algC and algD in Pseudomonas aeruginosa.
Res. Microbiol.
148:37-43[Medline].
|
| 23.
|
Leitäo, J. H., and I. Sä- Correia.
1997.
Effect of growth inhibitory concentrations of copper on alginate biosynthesis in highly mucoid Pseudomonas aeruginosa.
Microbiology
143:481-488.
|
| 24.
|
Linkerhägner, K., and J. Oelze.
1995.
Cellular ATP level and nitrogenase switchoff upon oxygen stress in chemostat cultures of Azotobacter vinelandii.
J. Bacteriol.
177:5289-5293[Abstract/Free Full Text].
|
| 25.
|
Linkerhägner, K., and J. Oelze.
1997.
Nitrogenase activity and regeneration of the cellular ATP pool in Azotobacter vinelandii adapted to different oxygen concentrations.
J. Bacteriol.
179:1362-1367[Abstract/Free Full Text].
|
| 26.
|
Liu, J. K.,
F. T. Lee,
C. S. Lin,
X. T. Yao,
J. W. Davenport, and T. Y. Wong.
1995.
Alternative function of the electron transport system in Azotobacter vinelandii: removal of excess reductant by the cytochrome d pathway.
Appl. Environ. Microbiol.
61:3998-4003[Abstract].
|
| 27.
|
Lobas, D.,
S. Schumpe, and W.-D. Deckwer.
1992.
The production of gellan polysaccharide with Sphingomonas paucimobilis E2 (DSM 6314).
Appl. Microbiol. Biotechnol.
37:411-415.
|
| 28.
|
Matsumoto, T.,
M. Kawal, and T. Masuda.
1992.
Influence of concentration and mannuronate/guluronate ratio on steady flow properties of alginate aqueous systems.
Biorheology
29:411-417[Medline].
|
| 29.
|
Moshiri, F.,
B. R. Crouse,
M. K. Johnson, and R. J. Maier.
1995.
The 'nitrogenase protective' FeSII protein of Azotobacter vinelandii: overexpression, characterisation and crystallization.
Biochemistry
34:12973-12982[CrossRef][Medline].
|
| 30.
|
Nunez, C.,
S. Moreno,
G. Soberon-Chavez, and G. Espin.
1999.
The Azotobacter vinelandii response regulator AlgR is essential for cyst formation.
J. Bacteriol.
181:141-148[Abstract/Free Full Text].
|
| 31.
|
Peters, H.-U.,
H. Herbst,
P. G. M. Hesselink,
H. Lünsdorf,
A. Schumpe, and W.-D. Deckwer.
1989.
The influence of agitation rate on xanthan production by Xanthomonas campestris.
Biotechnol. Bioeng.
34:1393-1397[CrossRef].
|
| 32.
|
Post, E.,
J. R. Golecki, and J. Oelze.
1982.
Morphological and ultrastructural variations in Azotobacter vinelandii growing in oxygen-controlled continuous culture.
Arch. Microbiol.
133:75-82[CrossRef].
|
| 33.
|
Post, E.,
D. Kleiner, and J. Oelze.
1983.
Whole cell respiration and nitrogenase activities in Azotobacter vinelandii growing in oxygen controlled continuous culture.
Arch. Microbiol.
134:68-72[CrossRef][Medline].
|
| 34.
|
Rehm, H. A., and S. Valla.
1997.
Bacterial alginate: biosynthesis and applications.
Appl. Microbiol. Biotechnol.
48:281-288[CrossRef][Medline].
|
| 35.
|
Reynolds, E. S.
1963.
The use of lead citrate at high pH as an electron-opaque stain in electron microscopy.
J. Cell Biol.
17:208-212[Free Full Text].
|
| 36.
|
Ruppen, M.,
G. Garner, and L. H. Sadoff.
1983.
Protein turnover in Azotobacter vinelandii during encystment and germination.
J. Bacteriol.
156:1243-1248[Abstract/Free Full Text].
|
| 37.
|
Sabra, W. A.
1999.
Microaerophilic production of alginate by Azotobacter vinelandii. Ph.D. dissertation.
Technische Universität Braunschweig, Braunschweig, Germany.
|
| 38.
|
Sabra, W. A.,
A.-P. Zeng,
S. Sabry,
S. Omar, and W.-D. Deckwer.
1999.
Effect of phosphate and oxygen concentrations on alginate production and stoichiometry of metabolism of Azotobacter vinelandii under microaerobic conditions.
Appl. Microbiol. Biotechnol.
52:773-780[CrossRef].
|
| 39.
|
Sadoff, H. L.
1975.
Encystment and germination in Azotobacter vinelandii.
Bacteriol. Rev.
39:516-539[Free Full Text].
|
| 40.
|
Senior, P. J.,
G. A. Beech,
G. A. F. Ritchie, and E. A. Dawes.
1972.
The role of oxygen limitation in the formation of poly- -hydroxybutyrate during batch and continuous culture of Azotobacter beijerinckii.
Biochem. J.
128:1193-1201[Medline].
|
| 41.
|
Skjak-Braek, G.
1992.
Alginate: biosynthesis and some structure function relationships relevant to biomedical and biotechnological applications.
Biochem. Soc. Trans.
20:27-33[Medline].
|
| 42.
|
Spurr, A. R.
1969.
A low viscosity epoxy resin embedding medium for electron microscopy.
J. Ultrastruct. Res.
26:31-43[CrossRef][Medline].
|
| 43.
|
Tsai, J. C.,
S. L. Aladegbami, and G. R. Vela.
1979.
Phosphate-limited culture of Azotobacter vinelandii.
J. Bacteriol.
139:639-645[Abstract/Free Full Text].
|
| 44.
|
Valla, S., and G. Skjak-Braek.
1996.
Alginate: a target molecule for genetic engineers and a versatile material for the biotechnologist.
In
Food Ingred. Eur. 1996(September):38-41.
|