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Applied and Environmental Microbiology, April 2000, p. 1311-1320, Vol. 66, No. 4
Institute of Biotechnology, Swiss Federal
Institute of Technology, CH-8093 Zürich, Switzerland
Received 14 October 1999/Accepted 20 January 2000
To prepare medium-chain-length poly-3-hydroxyalkanoates (PHAs) with
altered physical properties, we generated recombinant Escherichia
coli strains that synthesized PHAs with altered monomer compositions. Experiments with different substrates (fatty acids with
different chain lengths) or different E. coli hosts failed to produce PHAs with altered physical properties. Therefore, we engineered a new potential PHA synthetic pathway, in which
ketoacyl-coenzyme A (CoA) intermediates derived from the Poly-3-hydroxyalkanoates (PHAs),
which are produced as intracellular storage material by many bacterial
species, have attracted considerable attention due to their potential
applications as biodegradable plastics and as sources of valuable
chiral synthons (13). Based on detailed surveys,
Steinbüchel and coworkers have classified PHAs into two groups
(38), which are synthesized via different pathways (Fig.
1A). One group,
short-chain-length PHAs (scl-PHAs), contains
3-hydroxyalkanoate monomers with chain lengths from C4 to
C5. Another group, medium-chain-length PHAs (mcl-PHAs), are
characterized by 3-hydroxyalkanoate monomers with chain lengths from
C6 to C14.
0099-2240/00/$04.00+0
Copyright © 2000, American Society for Microbiology. All rights reserved.
Properties of Engineered Poly-3-Hydroxyalkanoates
Produced in Recombinant Escherichia coli
Strains
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ABSTRACT
Top
Abstract
Introduction
Materials and Methods
Results
Discussion
References
-oxidation
cycle are accumulated and led to the PHA polymerase precursor
R-3-hydroxyalkanoates in E. coli hosts. By
introducing the poly-3-hydroxybutyrate acetoacetyl-CoA reductase (PhbB)
from Ralstonia eutropha and blocking the ketoacyl-CoA degradation step of the
-oxidation, the ketoacyl-CoA intermediate was accumulated and reduced to the PHA precursor. Introduction of the
phbB gene not only caused significant changes in the
monomer composition but also caused changes of the physical properties of the PHA, such as increase of polymer size and loss of the melting point. The present study demonstrates that pathway engineering can be a
useful approach for producing PHAs with engineered physical properties.
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INTRODUCTION
Top
Abstract
Introduction
Materials and Methods
Results
Discussion
References


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FIG. 1.
General and modified pathways for the synthesis of
mcl-PHA precursors. (A) Possible links between mcl-PHA synthesis and
fatty acid degradation (left) and the general pathway for PHB synthesis
in R. eutropha (right) are outlined. All enzymatic
activities are numbered as indicated on the right. Genes encoding these
enzymes that have not been identified are indicated with an asterisk.
Dashed lines indicate pathways or reactions that are theoretically
possible but might not take place due to limited concentrations of the
-oxidation intermediates. (B) Modified pathway for mcl-PHA synthesis
in the E. coli fadB mutant. The fadB mutation
blocks
-oxidation at the 3-hydroxyacyl-CoA dehydrogenase step
(cross), which channels substrates to mcl-PHA. The introduced
phaC gene enables mcl-PHA synthesis, if sufficient substrate
is available. The thick dashed arrow indicates the PHB acetoacetyl-CoA
reductase activity encoded by phbB, cloned into the host.
Reduction of ketoacyl-CoA intermediates is theoretically possible but
might not take place due to limited 3-ketoacyl-CoA concentrations or
limited enzyme activity for the mcl acyl-CoA
-oxidation
intermediates. (C) Construct analogous to that seen in panel B with the
host E. coli fadA mutant. This modified pathway was designed
to increase the supply of mcl-PHA precursors by introduction of
phbB in addition to blocking
-oxidation at the
3-ketoacyl-CoA thiolase. The cross indicates a block of 3-ketoacyl-CoA
thiolase. The thick solid arrow indicates the postulated channeling of
ketoacyl-CoA from
-oxidation to PHA.
It is known that PHAs are synthesized by polymerization of coenzyme A
(CoA)-linked R-3-hydroxy fatty acids through one of several
PHA polymerases (PhaC) (see a recent review [21]). The synthesis of such CoA substrates can occur by a variety of pathways, the simplest of which uses
-ketothiolase (PhbA) and acetoacetyl-CoA reductase (PhbB) to synthesize precursors for scl-PHA polymerases such
as poly-3-hydroxybutyrate (PHB) synthase (PhbC) in Ralstonia eutropha (25, 26) (Fig. 1A). mcl-PHA CoA-linked
precursors can be generated through fatty acid
-oxidation that
produces acyl-CoA intermediates such as enoyl-CoA, 3-ketoacyl-CoA,
and/or S-3-hydroxyacyl-CoA when fatty acids are used as sole
carbon sources (14, 16, 39, 40) (Fig. 1A).
Effort has been devoted in recent years to increasing PHA yields and productivity. Achieving production costs that are in the same range as those of chemically synthesized plastics may be feasible, given the recent creation of PHA-producing transgenic plants (22, 27, 40, 41). Equally important in the production of PHAs is the control of the fundamental properties of the polymer. The production of PHA with specific monomer units has demonstrated that the monomer unit composition significantly affects the final properties of the polymer product (41). To influence rationally these properties in the production of organisms, it is necessary to control and direct the production of PHA precursors. Various approaches have been used to modify PHA monomer compositions. One example is cofeeding of different substrates, such as for the production of poly-3-hydroxybutyrate-co-3-hydroxyvalerate (5), and blending polymer poly(3-hydroxy-5-phenylvalerates) and poly-3-hydroxyalkanoates (19). So far, modification of monomer compositions of mcl-PHAs has not been feasible since mcl-PHA precursors are derived from fatty acid metabolism and their concentrations are difficult to control.
Biosynthesis of these polymers in host organisms that do not naturally produce PHA allows modulation of biosynthetic enzymes and therefore allows one to achieve substrate levels that are difficult to achieve in a native host strain for the study of PHA production (18). In addition, introduction of specific genes into an organism having a suitably modified PHA synthetic pathway may allow extension and regulation of the range of compounds that can be produced. Escherichia coli is one of these useful hosts.
Previously, it has been reported that E. coli strains
defective in the
-oxidation pathway are able to accumulate mcl-PHA when equipped with a PHA polymerase (29, 31). There are two PHA polymerases that are encoded by phaC1 and
phaC2 in Pseudomonas oleovorans and P. aeruginosa (16, 39). The presence of one of these two
polymerases is sufficient for PHA production in E. coli
fatty acid degradation mutants (29, 31). Recently, it was
found that inhibition of the
-oxidation thiolase step resulted in an
increase in the availability of substrate for PHA synthesis (30). Therefore, engineering of E. coli to extend
the range and distribution of precursors which can be channeled into
mcl-PHA may lead to interesting PHA variants for application and
development studies and is likely to extend the available chiral
synthon pool as well.
In this study, we selected two E. coli mutants, JMU193
(fadR fadB) and JMU194 (fadR fadA), to
investigate PHA accumulation. Our results revealed that ketoacyl-CoA
intermediates of the
-oxidation cycle are potential precursors for
PHA synthesis. By modifying relevant enzyme and substrate levels, we
were able to redirect ketoacyl-CoA
-oxidation intermediates into
mcl-PHA, and polymers with altered monomer composition and different
physical properties were obtained.
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MATERIALS AND METHODS |
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Strains and plasmids. The following E. coli strains were used in this study: JMU193 (fadR::Tn10 fadB64) (32) and JMU194 (fadR::Tn10 fadA30) (32). Plasmids pETQ2 (31) and pBTC2 carrying phaC2 and pET901 carrying phbB were used to construct recombinants capable of PHA synthesis. pGEc404 carrying phaC2 (16), pBS20 carrying phbCAB (36), pBCKS (Promega), pUC19 (43), pVLT35 (3), and pCK01 (6) were used for the construction of pBTC2 and pET901. pETQ102, pET104, pBTC2', and pET901' were intermediate plasmids during the construction of pBTC2 and pET901.
Recombinant DNA techniques.
Isolation and analysis of
plasmid DNA were carried out according to the method of Sambrook et al.
(33). Transformations of E. coli competent cells
were done according to standard procedures (33). Plasmids
pBTC2 and pET901 were constructed as illustrated in Fig.
2.
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Media and culture conditions.
E. coli
recombinants were grown at 37°C in complex Luria-Bertani (LB) medium
(33). To allow accumulation of intracellular PHA, 0.1NE2
minimal medium (15) was used, 0.2% (wt/vol) yeast extract
was added to the media as the carbon source to support growth. Fatty
acids were prepared as previously described (17) and
supplied as indicated in the medium for PHA production and possible
carbon sources. Cells were induced with 200 µM
isopropyl-
-D-thiogalactopyranoside (IPTG) at the early
exponential phase. If necessary, the following antibiotics were added:
kanamycin, 50 µg/ml; ampicillin, 100 µg/ml; streptomycin, 50 µg/ml; and chloramphenicol, 30 µg/ml. Cell growth was monitored by
measuring optical density at 450 nm (42).
PHB acetoacyl-CoA reductase assay. For enzymatic analysis, precultures were grown in LB medium for 8 h at 37°C and then transferred into 0.1NE2 minimal medium with 0.2% (wt/vol) yeast extract with a 1:100 dilution. Cells were induced with 200 µM IPTG at early exponential phase and harvested at late exponential phase, washed once with 0.1 M Tris-HCl (pH 7.5), and resuspended in a 10% volume of the same buffer. Cells were then disrupted in 200-µl aliquots by sonication. Protein concentrations were determined by Bio-Rad protein assay. Acetoacetyl-CoA reductase activity was monitored at 340 nm by the oxidation of NADPH during reduction of acetoacetyl-CoA (35). Then, 25 µl of crude extract and 25 µl of 10 mM NADPH were mixed with 500 µl of buffer (120 mM potassium phosphate [pH 5.5], 24 mM MgCl2, 1 mM dithiothreitol), and 455 µl of H2O. The reaction was started by adding 5 µl of 7 mM acetoacetyl-CoA. One unit is defined as 1 µmol of NADPH depletion/min.
Incorporation of monomers into preexisting PHA. Cells were cultivated on 0.1NE2 minimal medium with 0.2% (wt/vol) yeast extract and 2 mM hexadecanoate as described above. A pulse of 0.5 mM pentadecanoate was added to the culture at the time indicated. PHA compositions were analyzed by gas chromatography as previously described (20), and C7 and C9 monomer incorporation rates in preexisting C-even number PHA were determined.
Extraction of PHA. Lyophilized cells (500 to 1,000 mg) were extracted with 150 ml of methylene chloride (CH2Cl2) for at least 8 h at 50°C. The cell extract was filtered, and the solvent was evaporated (Buechi Rotavapor) until <15 ml of extract remained. PHA was recrystallized by dropping the extract into 10 volumes of well-stirred, ice-cold methanol. Methanol solutions were then filtered through Zetapor filter membranes (CUNO, Inc., Meriden, Conn.). Polymer was recovered from the filters by dissolving it in chloroform and evaporating the solvent. The polymer was stored in the dark at room temperature for further analysis.
Determination of PHA. To determine the presence and composition of PHA, lyophilized cells or isolated PHA were treated with H2SO4-methanol (85/15 [vol/vol]) in CHCl3 (containing 0.1 mg of methyl benzoate/ml) as previously described (20). The methanolyzed PHA monomers were analyzed by using a CP-Sil 5 CB column (Chrompack) on a gas chromatograph (Fison) (20). Splitless injection, an attenuation of 1, and a range of 0 were used to reach maximum sensitivity.
Molecular weight determination. The molecular weight measurements were done by gel permeation chromatography. Samples were dissolved in tetrahydrofuran and run through a PL-Gel C 5-µm column. Signals were detected using capillary viscosimetry (Viscotek 502), light scattering (small angle laser light scattering detector, KMX-6), and light refraction (differential high-temperature refractometer [Knauer]) measurements. The column was calibrated with polystyrene standards.
DSC measurement.
Differential scanning calorimetry (DSC)
spectra (melting temperatures [Tm], enthalpy
of fusion (
Hm), and glass transition temperatures
[Tg]) were recorded in a temperature range of
60 to 80°C on a Netzsch DSC 200 Perkin-Elmer model DSC-4 equipped with a cooling accessory under a nitrogen flow of 30 ml/min. PHA samples of 3 mg were encapsulated in aluminum pans and heated from
60
to 80°C at a rate of 10°C/min. The Tg was
taken as the midpoint of the heating capacity change.
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RESULTS |
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In this study E. coli fadR fadA and fadR
fadB mutants (JMU194 and JMU193, respectively) were used through
the whole study. The fadR gene encodes a protein that exerts
negative control over genes necessary for fatty acid oxidation (2,
4, 17, 23). A mutation in fadR derepresses
transcription of these genes, as a result of which the fad
genes are constitutively expressed, rendering E. coli
capable of growth on mcl fatty acids (2, 4). The
fadA gene encodes 3-ketoacyl-CoA thiolase (Fig. 1), and the
fadB gene encodes four enzyme activities (Fig. 1): enoyl-CoA hydratase, 3-hydroxyacyl-CoA dehydrogenase,
3-cis-
2-trans-enoyl-CoA
isomerase (not included in Fig. 1), and 3-hydroxyacyl-CoA epimerase
(2, 4, 17, 23). Mutations in fadA or
fadB block fatty acid oxidation and result in accumulation
of specific intermediates.
Utilization of different substrates for PHA formation in a
fadR fadB negative recombinant E. coli.
The
E. coli fatty acid catabolism mutant JMU193, which lacks
3-hydroxyacyl-CoA dehydrogenase (24, 37) (Fig. 1B), was
equipped with the PHA polymerase 2 from P. oleovorans GPo1
(16) and analyzed for PHA formation from a number of
different fatty acids ranging from C6 to C18.
Table 1 shows that the highest PHA
contents (ca. 4% of cell dry weight [cdw]) were obtained during
growth in the presence of longer-chain-length alkanoates of
C16 to C18. However, the composition of PHAs
formed from the tested alkanoates did not vary significantly with
changes of alkanoate chain length. The polymer produced from
odd-chain-length fatty acids consisted mainly of 3-hydroxyheptanoate
(C7) and 3-hydroxynonanoate (C9), while the
dominant even-chain-length monomers are 3-hydroxyhexanoate (C6), 3-hydroxyoctanoate (C8), and
3-hydroxydecanoate (C10).
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PHA formation by E. coli recombinants defective in
different steps of the
-oxidation.
Since the metabolic status,
including the concentrations of metabolites and the rate of metabolite
formation, may differ from one strain to another, it is plausible that
the intracellular content and the composition of mcl-PHAs formed from
such intermediates will vary from strain to strain. Thus, E. coli JMU194 (fadR fadA), a mutant which lacks
3-ketoacyl-CoA thiolase activity (24, 37) (Fig. 1C), was
compared with JMU193 for PHA formation. To control the expression of
phaC2, plasmid pBTC2 (Fig. 2A) containing phaC2 of P. oleovorans GPo1 expressed through the Ptac
promoter was introduced in JMU193 and JMU194, and the recombinants were
cultivated on medium containing hexadecanoate.
1.
However, E. coli JMU194(pBTC2) showed a sevenfold-higher
monomer incorporation rate (60 nmol/mg of cdw/min) after 36 h of
cultivation than did E. coli JMU193(pBTC2) (Table
2). There was also a significant difference in the PHA formed by the two recombinants: JMU194(pBTC2) accumulated 15% PHA, while JMU193(pBTC2) produced only 5% PHA after
36 h of cultivation. Furthermore, the PHA formed by E. coli JMU194(pBTC2) contained significantly more C6 and
C10 monomers than did the PHA produced by JMU193(pBTC2)
(Table 2).
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Redirecting of ketoacyl-CoA intermediates from
-oxidation into
the mcl-PHA synthetic pathway in E. coli JMU193 and JMU194
recombinants.
As illustrated in Fig. 1C, it might be possible to
redirect the carbon flux from the
-oxidation pathway to mcl-PHA
synthesis by blocking step 8 to accumulate 3-ketoacyl-CoA intermediates and amplifying step 7 to permit the reduction of these intermediates to
R-(
)-3-hydroxyacyl-CoA. It is known that the ketoacyl-CoA reductase encoded by phbB of R. eutropha (step 11 in Fig. 1A) has a substrate range of C4 to C6
acyl-CoAs (12), permitting it to convert ketohexyl-CoA to
R-(
)-3-hydroxyhexyl-CoA, which might be channeled into
mcl-PHA by PHA polymerase.
-oxidation cycle in these recombinants.
The effect of addition of pET901 on the characteristics of the PHA
formed by JMU193 recombinants was slight. When hexadecanoate was
supplied, with IPTG-induced phaC2 and phbB
expression, JMU193(pBTC2, pET901) produced 6% PHA, similar to the 5%
PHA seen for JMU193(pBTC2, pCK01), and the expression of
phbB in JMU193(pBTC2, pET901) hardly changed the PHA
composition compared to JMU193(pBTC2, pCK01) (Table 2).
The results for JMU194(pBTC2, pET901), which synthesized PHA to 20%,
were more interesting. Not only did this recombinant produce more PHA
than the closely related strain JMU194(pBTC2, pCK01) (15% PHA), but it
also produced a hexanoate-rich PHA. The higher PHA content can be
attributed to different precursor concentrations since the monomer
incorporation rates of the polymerase in both JMU194 recombinants were
similar (Table 2). The increased hexanoate content, with a
C6:C8:C10 ratio that changed from
20:57:23 to 42:38:20 in JMU194(pBTC2, pET901) clearly depended on the
expression of phbB (Table 2). To verify that this change was
not caused by the accumulation of free C6 monomers in the
PHA samples, we also tested E. coli recombinants carrying
only PhbB (pET901) and no PHA polymerase (with just pVLT35). Table 2
shows that no PHA and no C6 monomers were detected in
either the JMU194 or JMU193 recombinants.
Heptadecanoate was also tested to determine whether the presence of
PhbB led to PHAs with different monomer compositions. This was not the
case: no significant difference was observed in the content and
composition of PHAs produced by JMU194(pBTC2, pET901) and JMU194(pBTC2,
pCK01). As expected, when the acyl source was heptadecanoate,
JMU193(pBTC2, pCK01) and JMU193(pBTC2, pET901) again synthesized PHA
with a similar monomer composition.
Physical properties of polymers produced by E. coli recombinants. PHAs produced by the E. coli recombinants used in this study were isolated by complete solvent extraction from lyophilized cells. The monomer compositions of the purified PHAs were essentially identical to the values estimated by gas chromatography analysis after methanolysis of whole cells.
PHAs synthesized by JMU193(pBTC2, pCK01) and JMU193(pBTC2, pET901) had similar compositions, and their molecular weights and polymerization degree (PD) were also similar (Table 2). The PHA isolated from JMU194(pBTC2, pCK01) had a molecular weight of about 70,000, whereas JMU194(pBTC2, pET901) formed a polymer with two molecular weight peaks at about 1,100,000 and about 97,000 (Fig. 3, Table 2). Furthermore, the PD for PHA with molecular weight at 97,000 was almost 2.5-fold higher than that for PHA synthesized by JMU194(pBTC2, pCK01) (Table 2).
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Hm), and glass transition temperature
(Tg) (Table 2), whereas PHAs from two JMU194
recombinants exhibited a different DSC pattern: the PHAs isolated from
JMU194(pBTC2, pCK01) showed Tm and
Hm, while the PHAs isolated from JMU194(pBTC2, pET901),
which contained an active PHB acetoacyl-CoA reductase, did not show a
melting endotherm (Fig. 4 and Table 2).
Furthermore, this PHA exhibited a Tg value that
was about 2.6°C higher than that for PHA from JMU194(pBTC2, pCK01)
(Table 2).
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DISCUSSION |
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The monomer composition of PHAs can affect the properties of the
polymer (41). The development of mcl-PHA variants depends, therefore, on the range of monomers that can be incorporated into PHA.
Consequently, it is of interest to attempt to control rationally the
monomer composition of new mcl-PHAs. This requires a better understanding of pathways involved in mcl-PHA synthesis and of the
basic metabolic pathways that may provide PHA precursors. In this
study, we set out to address two questions. One was whether ketoacyl-CoA of the
-oxidation can serve as precursor source for PHA
synthesis. The second question was how the mcl-PHA monomer composition
could be modified. Among the approaches we tested, pathway engineering
by amplification of one potential PHA precursor supply route gave the
most promising result. Other approaches, such as varying the
substrates, did not lead to significant changes in PHA composition or
physical properties (Table 2).
The
-oxidation intermediate ketoacyl-CoA is a potential
precursor for PHA synthesis in E. coli.
Introduction of the
PHA polymerase into E. coli results in utilization of
3-hydroxyacyl-CoA precursors for the synthesis of PHA (29, 31, 34,
36). As illustrated in Fig. 1, when the
-oxidation is blocked
at the last step (ketothiolase [FadA]), all upstream intermediates
will accumulate (Fig. 1C). 3-Ketoacyl-CoA could be reduced to
R-(
)-3-hydroxyacyl-CoA through a 3-ketoacyl-CoA reductase
(step 7), S-(+)-3-hydroxyacyl-CoA may be epimerized (step 6, fadB), and enoyl-CoA may be hydrated to the corresponding R-(
)-3-hydroxyacyl-CoA (step 3, fadB). When the
-oxidation is blocked at step 5, catalyzed by 3-hydroxyacyl-CoA
dehydrogenase (FadB), one of these possible mcl-PHA precursors,
3-ketoacyl-CoA, will not accumulate (Fig. 1B). In this study, we found
that E. coli JMU194 (fadR fadA)
phaC+ recombinant incorporated more
C6 and C10 monomers into PHAs than the JMU193
(fadR fadB) phaC+ recombinant under
the same growth conditions (Tables 1 and 2). The relative monomer
content of PHA depends on the precursor concentration and the
specificity of the PHA polymerase for each precursor. Since the
specificity profile of the PHA polymerase is presumably identical in
both recombinants, differing PHA compositions must reflect the
differences in relative intracellular precursor concentrations.
-oxidation as described previously (7-9), which are available for PHA synthesis in
E. coli.
In contrast, introduction of phbB into the JMU194
(fadR fadA) phaC+ recombinant (Fig.
1C) resulted in increased PHA accumulation and a PHA which contained
twofold-higher C6 monomer than the PHA from the fadR
fadA recombinant carrying only phaC (Table 2). This is
compatible with the notion that in the JMU194 (fadR fadA) phaC+ recombinant there was accumulation of
C6 ketoacyl-CoA, which was then reduced by the PHB
acetoacyl-CoA reductase and incorporated into mcl-PHA. These data
strongly indicate that the 3-ketoacyl-CoA intermediate of the
-oxidation is a potential precursor source for PHA synthesis.
When grown on heptadecanoate, no C5 monomers were found in
the PHAs of E. coli fadR fadA strains carrying
phaC and phbB (Table 2), although
3-hydroxypentanoyl-CoA (C5) could in principle be formed
via
-oxidation from the intermediate 3-ketopentanoyl-CoA by the PHB
acetoacyl-CoA reductase. This is probably due to the low affinity of
the PHA polymerase for C5 monomers (15),
resulting in limited incorporation into PHA.
Physical properties of PHA can be changed by pathway engineering. We found significant differences in the physical properties of PHA isolated from fadR fadA E. coli JMU194 carrying phaC and from the same recombinant carrying additional phbB (Table 2).
E. coli JMU194 carrying phaC accumulated PHA with a molecular weight of about 70,000. After introduction and expression of the phbB gene, PHA with two molecular weight ranges was found (Fig. 3). This is probably not caused by formation of different groups of polymers (e.g., one group is mcl-PHA, another is poly-3-hydroxyhexanoate), since only one glass transition temperature was observed (Fig. 4) and, furthermore, only one functional polymerase was introduced into the recombinant. The most likely reason for the formation of the high-molecular-weight peak is changes in the polymer chain length. PHB chains typically contain 7,000 to 23,000 monomers (see review [1]), which is 5- to 10-fold more than that found in mcl-PHAs (24). Perhaps the increased C6 content of JMU194 carrying phaC and phbB somehow alters the ratio of chain elongation to chain termination events, resulting in longer PHA chains, comparable to the PHB formed in R. eutropha and other PHB-producing organisms. Another possibility, however, is that the 1,100,000 peak of Fig. 3 is due not to longer polymer chains but to polymer aggregates due to the presence of stretches of C6 monomers in the PHA chains. These stretches could perhaps facilitate strong noncovalent interactions among PHA chains and thus result in the formation of microgels as shown in Fig. 5. These microgels may not be able to dissolve in tetrahydrofuran completely, resulting in the high-molecular-weight peak. Further experiments have to be carried out to distinguish between these two possibilities.
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-oxidation of fatty acids from acyl-CoA to 3-hydroxyacyl-CoA via
enoyl-CoA (7-9), following the
-oxidation cycle
clockwise. The second, illustrated in the present study, involves an
extension of the same cycle followed by formation of 3-hydroxyacyl-CoA
via 3-ketoacyl-CoA. By engineering the second pathway in E. coli, PHAs with altered monomer compositions were produced.
Physical characterization of the isolated polymers shows that the
monomer composition plays an important role in controlling the physical properties of PHAs. This suggests that it will be possible to obtain
PHAs with altered properties by modifying and regulating fatty acid
metabolic genes and PHA synthetic genes in E. coli. The
experience gained with precursor enrichments in E. coli will undoubtedly support the development of suitable mcl-PHA-producing transgenic plants.
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ACKNOWLEDGMENTS |
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We thank M. Colussi for measuring molecular weight, D. Dennis for providing strains JMU193 and JMU194, and M. Held and K. Jung for helpful discussions.
This work was supported by grants from the Swiss Federal Office for Education and Science (BBW no. 96.0348) to Q.R.
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FOOTNOTES |
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* Corresponding author. Mailing address: Institute of Biotechnology, ETH Hönggerberg, CH-8093, Zürich, Switzerland. Phone: 41-1-6333286. Fax: 41-1-6331051. E-mail: bw{at}biotech.biol.ethz.ch.
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REFERENCES |
|---|
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|
|---|
| 1. | Ballistreri, A., G. Montaudo, G. Impallomeni, R. W. Lenz, Y. B. Kim, and R. C. Fuller. 1990. Sequence distribution of beta-hydroxyalkanoate units with higher alkyl groups in bacterial copolyesters. Macromolecules 23:5059[CrossRef]. |
| 2. | Black, P. N., and C. C. DiRusso. 1994. Molecular and biochemical analyses of fatty acid transport, metabolism, and gene regulation in Escherichia coli. Biochim. Biophys. Acta 1210:123-145[Medline]. |
| 3. | de Lorenzo, V., L. Eltis, B. Kessler, and K. N. Timmis. 1993. Analysis of Pseudomonas gene products using lacIq/Ptrp-lac plasmids and transposons that confer conditional phenotypes. Gene 123:17-24[CrossRef][Medline]. |
| 4. |
DiRusso, C. C., and W. D. Nunn.
1985.
Cloning and characterization of a gene (fadR) involved in regulation of fatty acid metabolism in Escherichia coli.
J. Bacteriol.
161:583-588 |
| 5. | Doi, Y., A. Tamaki, M. Kunioka, and K. Soga. 1987. Biosynthesis of terpolyesters of 3-hydroxybutyrate, 3-hydroxyvalerate, and 5-hydroxyvalerate in Alcaligenes eutrophus from 5-chloropentanoic and pentanoic acids. Macromol. Chem. Rapid Commun. 8:631-635. |
| 6. | Fernández, S., V. de Lorenzo, and J. Pérez-Martin. 1995. Activation of the transcriptional regulator XylR of Pseudomonas putida by release of repression between functional domains. Mol. Microbiol. 16:205-213[CrossRef][Medline]. |
| 7. |
Fukui, T., and Y. Doi.
1997.
Cloning and analysis of the poly(3-hydroxybutyrate-co-3-hydroxyhexanoate) biosynthesis genes of Aeromonas caviae.
J. Bacteriol.
179:4821-4830 |
| 8. |
Fukui, T.,
N. Shiomi, and Y. Doi.
1998.
Expression and characterization of (R)-specific enoyl coenzyme A hydratase involved in polyhydroxyalkanoate biosynthesis by Aeromonas caviae.
J. Bacteriol.
180:667-673 |
| 9. | Fukui, T., S. Yokomizo, G. Kobayashi, and Y. Doi. 1999. Co-expression of polyhydroxyalkanoate synthase and (R)-enoyl-CoA hydratase genes of Aeromonas caviae establishes copolyester biosynthesis pathway in Escherichia coli. FEMS Microbiol. Lett. 170:69-75[CrossRef][Medline]. |
| 10. |
Gerngross, T. U.,
P. Reilly,
J. Stubbe,
A. J. Sinskey, and O. P. Peoples.
1993.
Immunocytochemical analysis of poly-beta-hydroxybutyrate (PHB) synthase in Alcaligenes eutrophus H16: localization of the synthase enzyme at the surface of the PHB granules.
J. Bacteriol.
175:5289-5293 |
| 11. | Gross, R. A., C. DeMello, R. W. Lenz, H. Brandl, and R. C. Fuller. 1989. Biosynthesis and characterization of poly(beta-hydroxyalkanoates) produced by Pseudomonas oleovorans. Macromolecules 22:1106-1115[CrossRef]. |
| 12. | Haywood, G. W., A. J. Anderson, L. Chu, and E. A. Dawes. 1988. The role of NADH- and NADHP-linked acetoacetyl-CoA reductases in the poly-3-hydroxybutyrate synthesizing organism Alcaligenes eutrophus. FEMS Microbiol. Lett. 52:259-264[CrossRef]. |
| 13. |
Hrabak, O.
1992.
Industrial production of poly- -hydroxybutyrate.
FEMS Microbiol. Rev.
103:251-256[CrossRef].
|
| 14. |
Huijberts, G. N. M.,
T. C. de Rijk,
P. de Waard, and G. Eggink.
1995.
13C nuclear magnetic resonance studies of Pseudomonas putida fatty acid metabolic routes involved in poly(3-hydroxyalkanoate) synthesis.
J. Bacteriol.
176:1661-1666 |
| 15. |
Huisman, G. W.,
O. de Leeuw,
G. Eggink, and B. Witholt.
1989.
Synthesis of polyhydroxyalkanoates is a common feature of fluorescent pseudomonads.
Appl. Environ. Microbiol.
55:1949-1954 |
| 16. |
Huisman, G. W.,
E. Wonink,
R. Meima,
B. Kazemier,
P. Terpstra, and B. Witholt.
1991.
Metabolism of poly(3-hydroxyalkanoates) (PHAs) by Pseudomonas oleovorans.
J. Biol. Chem.
266:2191-2198 |
| 17. |
Jenkins, L. J., and W. D. Nunn.
1987.
Genetic and molecular characterization of the genes involved in short-chain fatty acid degradation in Escherichia coli: the ato system.
J. Bacteriol.
169:42-52 |
| 18. | Kidwell, J., H. E. Valentin, and D. Dennis. 1995. Regulated expression of the Alcaligenes eutrophus pha biosynthesis genes in Escherichia coli. Appl. Environ. Microbiol. 61:1391-1398[Abstract]. |
| 19. | Kim, Y. B., R. W. Lenz, and R. C. Fuller. 1991. Preparation and characterization of poly(beta-hydroxyalkanoates) obtained from Pseudomonas oleovorans grown with mixtures of 5-phenylvaleric acid and n-alkanoic acids. Macromolecules 24:5256-5260[CrossRef]. |
| 20. |
Lageveen, R. G.,
G. W. Huisman,
H. Preusting,
P. Ketelaar,
G. Eggink, and B. Witholt.
1988.
Formation of polyesters by Pseudomonas oleovorans: effect of substrates on formation and composition of poly-(R)-3-hydroxyalkanoates and poly-(R)-3-hydroxyalkenoates.
Appl. Environ. Microbiol.
54:2924-2932 |
| 21. |
Madison, L. L., and G. W. Huisman.
1999.
Metabolic engineering of poly(3-hydroxyalkanoates): from DNA to plastic.
Microbiol. Mol. Biol. Rev.
63:21-53 |
| 22. |
Nawrath, C.,
Y. Poirier, and C. Somerville.
1994.
Targeting of the polyhydroxybutyrate biosynthetic pathway to the plastids of Arabidopsis thaliana results in high levels of polymer accumulation.
Proc. Natl. Acad. Sci. USA
91:12760-12764 |
| 23. | Nunn, W. D. 1986. Two-carbon compounds and fatty acids as carbon sources, p. 285-301. In F. C. Neidhardt, et al. (ed.), Escherichia coli and Salmonella typhimurium. American Society for Microbiology, Washington, D.C. |
| 24. | Overath, P., G. Pauli, and H. U. Schairer. 1969. Fatty acid degradation in Escherichia coli: an inducible acyl-CoA synthetase, the mapping of old-mutations, and isolation of regulatory mutants. Eur. J. Biochem. 7:559-574[Medline]. |
| 25. |
Peoples, O. P., and A. J. Sinskey.
1989.
Poly-beta-hydroxybutyrate biosynthesis in Alcaligenes eutrophus H16. Characterization of the genes encoding beta-ketothiolase and acetoacetyl-CoA reductase.
J. Biol. Chem.
264:15293-15297 |
| 26. |
Peoples, O. P., and A. J. Sinskey.
1989.
Poly-beta-hydroxybutyrate biosynthesis in Alcaligenes eutrophus H16. Identification and characterization of the PHB polymerase gene (phbC).
J. Biol. Chem.
264:15298-15303 |
| 27. | Poirier, Y., C. Nawrath, and C. Somerville. 1995. Production of polyhydroxyalkanoates, a family of biodegradable plastics and elastomers, in bacteria and plants. Bio/Technology 13:142-150[CrossRef][Medline]. |
| 28. | Preusting, H., A. Nijenhuis, and B. Witholt. 1990. Physical characteristics of poly(3-hydroxyalkanoates) and poly(3-hydroxyalkenoates) produced by Pseudomonas oleovorans grown on aliphatic hydrocarbons. Macromolecules 23:4220-4224[CrossRef]. |
| 29. | Qi, Q., B. H. A. Rehm, and A. Steinbüchel. 1997. Synthesis of poly(3-hydroxyalkanoates) in Escherichia coli expressing the PHA synthase gene phaC2 from Pseudomonas aeruginosa: comparison of PhaC1 and PhaC2. FEMS Microbiol. Lett. 157:156-162. |
| 30. | Qi, Q. S., A. Steinbüchel, and B. H. A. Rehm. 1998. Metabolic routing towards polyhydroxyalkanoic acid synthesis in recombinant Escherichia coli (fadR): inhibition of fatty acid beta-oxidation by acrylic acid. FEMS Microbiol. Lett. 167:89-94[Medline]. |
| 31. | Ren, Q. 1997. Biosynthesis of medium chain length poly-3-hydroxyalkanoates: from Pseudomonas to Escherichia coli. Ph.D. thesis. Swiss Federal Institute of Technology, Zürich, Switzerland. |
| 32. | Rhie, H. G., and D. Dennis. 1995. Role of fadR and atoC(Con) mutations in poly(3-hydroxybutyrate-co-3-hydroxyvalerate) synthesis in recombinant pha+ Escherichia coli. Appl. Environ. Microbiol. 61:2487-2492[Abstract]. |
| 33. | Sambrook, J., E. F. Fritsch, and T. Maniatis. 1989. Molecular cloning: a laboratory manual, 2nd ed. Cold Spring Harbor Laboratory Press, Cold Spring Harbor, N.Y. |
| 34. |
Schubert, P.,
A. Steinbüchel, and H. G. Schlegel.
1988.
Cloning of the Alcaligenes eutrophus genes for synthesis of poly- -hydroxybutyrate (PHB) and synthesis of PHB in E. coli.
J. Bacteriol.
170:5837-5847 |
| 35. | Senior, P. J., and E. A. Dawes. 1973. The regulation of poly-3-hydroxybutyrate metabolism in Azotobacter beijerinckii. Biochem. J. 134:225-238[Medline]. |
| 36. |
Slater, S. C.,
W. H. Voige, and D. E. Dennis.
1988.
Cloning and expression in E. coli of the Alcaligenes eutrophus H16 poly- -hydroxybutyrate biosynthetic pathway.
J. Bacteriol.
170:4431-4436 |
| 37. |
Spratt
1984.
Cloning, mapping, and expression of genes involved in the fatty acid-degradative multienzyme complex of Escherichia coli.
J. Bacteriol.
158:535-542 |
| 38. | Steinbüchel, A., and H. E. Valentin. 1995. Diversity of bacterial polyhydroxyalkanoic acids. FEMS Microbiol. Lett. 128:219-228[CrossRef]. |
| 39. | Timm, A., and A. Steinbüchel. 1992. Cloning and molecular analysis of the poly(3-hydroxyalkanoic acid) gene locus of Pseudomonas aeruginosa PAO1. Eur. J. Biochem. 209:15-30[Medline]. |
| 40. | van der Leij, F. R., and B. Witholt. 1995. Strategies for the sustainable production of new biodegradable polyesters in plants: a review. Can. J. Microbiol. 41:222-238. |
| 41. | Williams, S. F., and O. P. Peoples. 1996. Biodegradable plastics from plants. Chemtech 26:38-44. |
| 42. |
Witholt, B.
1972.
Method for isolating mutants overproducing nicotinamide adenine dinucleotide and its precursors.
J. Bacteriol.
109:350-364 |
| 43. | Yanisch-Perron, C., J. Vieira, and J. Messing. 1985. Improved M13 phage cloning vectors and host strains: nucleotide sequences of the M13mp18 and pUC19 vectors. Genes 33:103-119[CrossRef][Medline]. |
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