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Applied and Environmental Microbiology, March 2000, p. 1233-1236, Vol. 66, No. 3
0099-2240/00/$04.00+0
Copyright © 2000, American Society for Microbiology. All rights reserved.
Involvement of Acyl Coenzyme A Oxidase Isozymes in
Biotransformation of Methyl Ricinoleate into
-Decalactone by
Yarrowia lipolytica
Yves
Waché,1,*
Céline
Laroche,1
Karin
Bergmark,1
Charlotte
Møller-Andersen,1
Mario
Aguedo,1
Marie-Thérèse
Le
Dall,2
Huijie
Wang,2
Jean-Marc
Nicaud,2 and
Jean-Marc
Belin1
Laboratoire de Biotechnologie, Ecole
Nationale Supérieure de Biologie Appliquée à la
Nutrition et à l'Alimentation, Université de Bourgogne,
21000 Dijon,1 and Laboratoire de
Génétique des Micro-organismes, INRA-CNRS, URA1925,
78850 Thiverval-Grignon,2 France
Received 25 October 1999/Accepted 22 November 1999
 |
ABSTRACT |
We reported previously on the function of acyl coenzyme A
(acyl-CoA) oxidase isozymes in the yeast Yarrowia
lipolytica by investigating strains disrupted in one or several
acyl-CoA oxidase-encoding genes (POX1 through
POX5) (H. Wang et al., J. Bacteriol. 181:5140-5148, 1999).
Here, these mutants were studied for lactone production. Monodisrupted
strains produced similar levels of lactone as the wild-type strain (50 mg/liter) except for
pox3, which produced 220 mg of
-decalactone per liter after 24 h. The
pox2
pox3 double-disrupted strain, although slightly affected in
growth, produced about 150 mg of lactone per liter, indicating that
Aox2p was not essential for the biotransformation. The
pox2
pox3
pox5 triple-disrupted strain produced and consumed
lactone very slowly. On the contrary, the
pox2
pox3
pox4
pox5 multidisrupted strain did not grow or biotransform methyl
ricinoleate into
-decalactone, demonstrating that Aox4p is essential
for the biotransformation.
 |
TEXT |
The biotransformation of fatty acids
into
-decalactone, a compound with a peach-like aroma, has led to
numerous patents. Most processes are based on the use of yeast strains
to transform ricinoleic acid or its derivatives into lactones, as
reviewed by Endrizzi et al. (4). The development of such
processes initially involves optimizing physical and chemical
conditions for the biotransformation or screening to find new organisms
that produce
-decalactone. This stage of development is continuing,
but finding ways to increase lactone production is increasingly
demanding improvements in our knowledge of the relevant cellular
mechanisms. Endrizzi et al. (2) showed that the
-oxidation pathway is involved in the biotransformation, and studies
of intermediates have intensified (9, 10, 14, 20).
Féron et al. (6, 7) have focused on the toxicity of
lactone for the yeast that produces it, and Endrizzi-Joran
(5) has focused on the reconsumption of lactone. Pagot
(15) has been looking for critical steps and has found two
potentially rate-limiting steps: the entry of fatty acids into
peroxisomes, which is at least partially carnitine dependent (16), and the first and limiting (13, 18)
reaction of peroxisomal
-oxidation (17), involving acyl
coenzyme A (acyl-CoA) thioester oxidation by an acyl-CoA oxidase (Aox)
to yield trans-2-enoyl-CoA derivatives. All these studies
have increased our understanding of the mechanisms involved but have
not substantially increased lactone production.
In Yarrowia lipolytica, acyl-CoA oxidases are encoded by
five genes (POX1 through POX5). An investigation
of the function of the Aox isozymes demonstrated a chain length
specificity for Aox2p (long chain) and Aox3p (short chain). Aox2p and
Aox3p together account for 70 to 80% of global Aox activity
(22). Pagot et al. (17) disrupted POX1
(encoding Aox1p) and observed higher levels of
-oxidation and higher
Aox activities but lower levels of lactone production, thereby
demonstrating that Aox plays a fundamental role in lactone production.
So far, no technological applications have resulted from the research
of yeast acyl-CoA oxidases apart from that of Picataggio et al.
(19), who blocked
-oxidation by sequential disruption of
Aox genes in Candida tropicalis to redirect fatty acids to
the
-oxidation pathway, leading to the production of long-chain
dicarboxylic acids.
We decided to focus on this step with the goal of significantly
increasing lactone production. We used the set of disrupted strains for
the POX genes described previously (22), with the aim of determining their role in lactone production. We found that Aox
composition affects lactone production, either positively or
negatively. Particularly, mutants disrupted for the POX3
gene encoding the short-chain-specific enzyme (Aox3p) had increased lactone productions.
The Y. lipolytica strains used in this study are derived
from the wild-type Y. lipolytica W29 (ATCC 20460). Their
constructions have been described elsewhere (21, 22). All
strains were cultured for 48 h on malt extract agar (Difco) at
27°C and used to inoculate a 500-ml baffled Erlenmeyer flask
containing 200 ml of glucose medium (15 g of glucose/liter, 2.5 g
of ammonium chloride/liter, 0.1 g of yeast extract/liter, 2.1 g of monopotassium phosphate/liter, 4.51 g of disodium
phosphate/liter, 0.2 g of magnesium sulfate/liter, 0.1 g of
sodium chloride/liter, 9.14 mg of iron (II) sulfate heptahydrate/liter, 0.5 mg of zinc chloride/liter, 1.56 mg of copper sulfate/liter) to an
optical density at 600 nm (OD600) of 0.25 (6 × 106 cells/ml). Flasks were shaken at 140 rpm for 18 h
until the cultures reached the late logarithmic growth phase. Cells
were harvested (10,000 × g, 5 min), washed twice with
phosphate buffer (50 mM, pH 7.4), and resuspended in MD medium (6.7 g
of yeast nitrogen base/liter, 5 g of ammonium chloride/liter,
1 g of methyl decanoate/liter) (OD600 = 0.25) for
growth experiments or in MR medium (MD medium with 0.2 g of Tween
80/liter and with 1 g of methyl decanoate/liter replaced with
5 g of methyl ricinoleate/liter [Dubois, Boulogne, France])
(OD600 = 0.25) for growth and lactone production
kinetic experiments.
Cells grown in MR or MD medium were counted in a Malassez cell. Slide
Write+ (Advanced Graphics Software Inc., Carlsbad, Calif.) was used to
fit curves and to calculate the parameters corresponding to the
Gompertz model as modified by Zwietering et al. (23): Xmax, the maximal amount of biomass;
µmax, the maximal growth rate (h
1); and
, the lag phase (h).
For
-decalactone extraction and analysis, 1.5 ml was removed and
centrifuged. The supernatant (both aqueous and oil phases) was mixed,
and its pH was lowered to 2 with HCl (6 N). The internal standard
(
-undecalactone) was added, and the mixture was extracted with 1.5 ml of diethyl ether in 4-ml glass vials by shaking for 1.5 min. The
ether phase was then analyzed in an HP6890 gas chromatograph with
an HP- INNOWax capillary column (30.0 m by 320 µm by 0.25 µm) using N2 as a carrier gas at a linear flow rate of
4.3 ml/min. The split injector (split ratio, 7.1:1) temperature was set
to 250°C, and that of the flame ionization detector to 300°C. The oven temperature was programmed to increase from 60 to 145°C at a
rate of 5°C/min and then at a rate of 2°C/min to 180°C.
Contributions of each Aox isozyme to the global acyl-CoA oxidase
activity can be deduced from Fig. 1,
which represents the effect of gene disruption on the activity of the
remaining enzymes in the cell extracts depending on substrate chain
length (21, 22). As shown in Table
1, a POX monodisruption had no
significant effect on the growth characteristics of the mutant strains.
Consistent with Aox2 and Aox3 playing the major roles, the growth of
the double-disrupted strain,
pox2
pox3, was altered,
with a lower µmax (0.07 h
1 compared to 0.15 h
1 for the wild type) and a longer
(3.7 h, compared
to 2.2 h). However, there were no significant differences in
Xmax (results not shown) except for
pox2
pox3
pox4
pox5 cells, which did not grow at
all due to the lack of activity of the enzyme encoded by
POX1 in those conditions.

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FIG. 1.
Acyl-CoA oxidase activity profiles of mutant strains as
a function of substrate chain length. Activity was measured
independently with C6-CoA, C10-CoA, and
C14-CoA substrates and was standardized for protein
concentration (21). The strains presented here are the wild
type, pox2, pox3, pox2
pox3, and pox2 pox3 pox5.
|
|
To determine whether particular Aox isozymes were involved in
C10 consumption, we studied the growth of various mutants
on the C10 substrate methyl decanoate instead of the toxic
-decalactone (Table 2).
µmax was significantly higher for
pox2 and
lower for
pox3 than for the wild type. At least one of
the two enzymes (Aox2p and Aox3p) must be present if the yeast is to
grow in MD medium, as the double-disrupted strain,
pox2
pox3, cannot grow on this substrate.
Figure 2 shows lactone production
kinetics of various strains for the first 24 h of culture in MR
medium. We can distinguish the mutants with
pox3
(
pox3 and
pox3
pox5) and
pox2
pox3 disruptions (Fig. 2B) from those with another disruption
(
pox2,
pox5) or no disruption (wild type)
(Fig. 2A). The strains with POX2 and POX3
produced
-decalactone in the first 12 h, and thereafter, the
reconsumption rate was at least equal to the production rate. For
strains containing the POX3 deletion, lactone was produced during the first 24 h of culture to higher levels. The rate of productivity for
pox3 and
pox3
pox5 in
the first 12 h was significantly higher (more than 12.5 mg/liter/h) than that of all the other strains (between 3 and 7 mg/liter/h). However, strains with
pox2
pox3
disruptions produced lactone more slowly, with maximal production occurring, as for the maximal biomass production, between 12 and 24 h.

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FIG. 2.
Lactone production by the various strains. (A)
Monodisrupted strains other than pox3: pox2
( ); pox5 ( ), and wild type ( ). (B)
pox3 strains: pox3 ( ); pox2
pox3 ( ); pox3 pox5 ( ), and wild type
( ). Lactone concentration was determined in the culture medium after
extraction.
|
|
Table 1 shows the maximal rate of lactone production
[(dP/dt)max] and maximal rate of specific
production [qpmax = (dP/dt X)max].
pox2
pox3
pox4
pox5
cells did not grow or produce any lactone. The rates of production (6.1 mg/liter/h) and specific production were the lowest in wild-type cells.
The strain with
pox2
pox3 simultaneously disrupted had
a slightly higher rate of lactone production (9.4 mg/liter/h). Higher
rates (twice that of the wild type) were obtained with
pox2 and
pox5 strains, and the highest rate
was obtained with the
pox3-disrupted strains, which had
rates of production four to five times that of the wild type (22.0 mg/liter/h for
pox3
pox5 and 31.1 mg/liter/h for
pox3). The qpmax for
pox3 strains was also three to four times higher than
that of the wild type: 1.3 mg/106 cells/h for
pox3 and 1.22 mg/106 cells/h for
pox3
pox5. For the double-disrupted strain
pox2
pox3, qpmax was only
slightly higher than that of the wild type: 0.48 mg/106
cells/h instead of 0.34 mg/106 cells/h, but the period of
(dP/dt X)max was much longer.
Aox2 and Aox3 combined provide the main Aox activity (70 to 80% of the
total) (Fig. 1), but the other three Aox proteins are involved in
-oxidation. For some gene disruptions, cells compensate for the lack
of the corresponding Aox, most probably through regulation of the other
POX gene(s), resulting in global Aox activity higher than
that of the wild type (22). One of the genes causing an enhanced Aox activity (POX1) was not functional or not
expressed in our conditions, but its disruption affected not only the
level of Aox activity but also the lactone productivity of the mutant strain (17). The double disruption of POX2 and
POX3 clearly shows that at least one other gene product is
involved in the production pathway. Aox5p may be functional, as the
triple-disrupted strain (
pox2
pox3
pox5) had no
detectable activity but grew and biotransformed methyl ricinoleate into
-decalactone. Another gene product, Aox4p, is functional in
Yarrowia cells because the
pox2
pox3
pox4
pox5 mutant did not grow or produce lactone, contrary to
pox2
pox3
pox5. Methyl ricinoleate
biotransformation in yeast utilizes the peroxisomal
-oxidation
pathway (2). The search for intermediates established that
ricinoleyl-CoA is shortened by two carbons four times, resulting in the
accumulation of
-decalactone (9, 14, 20). The precursor
of this lactone is 4-hydroxydecanoyl-CoA, or 4-hydroxydecanoic acid
(6), which can be oxidized in one cycle, leading to
2-hydroxyoctanoic acid (14). Alternatively, it may be
oxidized in half a cycle, yielding 3,4-dihydroxydecanoic acid and
3-hydroxy-
-decalactone (9). 4-Hydroxydecanoic acid and
its CoA form give rise easily to the more stable lactone form,
accounting for the accumulation of
-decalactone (9, 14).
However, a decrease in lactone concentration has often been observed
because some yeasts are able to reconsume this metabolic product
(3, 8, 14). One mechanism which could be implicated in the
reconsumption is
-oxidation followed by the
-oxidation of the
carbon chain extremity (5), but other possibilities include
delactonization by a lactonase producing a hydroxy acid which is fed
into the
-oxidation pathway (1, 11, 12).
The significant increase in the lactone production of
pox3 strains most likely results from two effects, as
schematically presented in Fig. 3.
Reconsumption is particularly evident because for
POX3-possessing strains, lactone concentration in the
culture medium drastically decreases after 12 h. Presumably,
disrupting the short-chain-specific Aox gene slows down
-oxidation
cycles at the C10 level as the growth of
pox3
strains is greatly affected on C10 substrate. This will
increase the size of the 4-hydroxydecanoic acid pool and therefore
slightly increase
-decalactone production, and it will also stop any
-oxidation following the possible
-oxidation or delactonization
and, hence, will lower the rate of decalactone disappearance. The
initial step of lactone reconsumption may involve an
-oxidation
reaction or opening of the lactone ring, and the Aox step only affects
the fluxes. We added
-decalactone to the medium in the presence of
the wild type,
pox2,
pox3, and
pox2
pox3 and monitored its disappearance. We found no
significant differences between the strains in 4 h of reaction
(results not shown).
This study, showing a fivefold increase in the production rate,
demonstrates that mastering the control of Aox, particularly lowering
the impact of short-chain-specific Aox, is a promising way to increase
lactone production. However, it will still be necessary to overcome
lactone toxicity and to inhibit reconsumption.
 |
FOOTNOTES |
*
Corresponding author. Mailing address: Laboratoire de
Biotechnologie, Ecole Nationale Supérieure de Biologie
Appliquée à la Nutrition et à l'Alimentation,
Université de Bourgogne, 1, esplanade Erasme, 21000 Dijon,
France. Phone: 33 3 80 39 66 80. Fax: 33 3 80 39 66 41. E-mail:
ywache{at}u-bourgogne.fr.
 |
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Applied and Environmental Microbiology, March 2000, p. 1233-1236, Vol. 66, No. 3
0099-2240/00/$04.00+0
Copyright © 2000, American Society for Microbiology. All rights reserved.
This article has been cited by other articles:
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