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Applied and Environmental Microbiology, April 2001, p. 1815-1820, Vol. 67, No. 4
0099-2240/01/$04.00+0 DOI: 10.1128/AEM.67.4.1815-1820.2001
Copyright © 2001, American Society for Microbiology. All rights reserved.
Purification and Characterization of an
X-Prolyl-Dipeptidyl Peptidase from Lactobacillus
sakei
Yolanda
Sanz* and
Fidel
Toldrá
Instituto de Agroquímica y
Tecnología de Alimentos (CSIC), 46100 Burjasot (Valencia),
Spain
Received 6 October 2000/Accepted 18 January 2001
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ABSTRACT |
An X-prolyl-dipeptidyl peptidase has been purified from
Lactobacillus sakei by ammonium sulfate fractionation and
five chromatographic steps, which included hydrophobic interaction,
anion-exchange chromatography, and gel filtration chromatography. This
procedure resulted in a recovery yield of 7% and an increase in
specificity of 737-fold. The enzyme appeared to be a dimer with a
subunit molecular mass of approximately 88 kDa. Optimal activity was
shown at pH 7.5 and 55°C. The enzyme was inhibited by serine
proteinase inhibitors and several divalent cations (Cu2+,
Hg2+, and Zn2+). The enzyme almost exclusively
hydrolyzed X-Pro from the N terminus of each peptide as well as
fluorescent and colorimetric substrates; it also hydrolyzed X-Ala at
the N terminus, albeit at lower rates. Km s for
Gly-Pro- and Lys-Ala-7-amido-4-methylcoumarin were 29 and 88 µM,
respectively; those for Gly-Pro- and Ala-Pro-p-nitroanilide were 192 and 50 µM, respectively. Among peptides,
-casomorphin 1-3 was hydrolyzed at the highest rates, while the relative hydrolysis of
the other tested peptides was only 1 to 12%. The potential role of the
purified enzyme in the proteolytic pathway by catalyzing the hydrolysis
of peptide bonds involving proline is discussed.
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INTRODUCTION |
Lactic acid bacteria constitute one
of the most important group of microorganisms used in food
fermentation. In the last decades, the metabolic traits of these
bacteria have been the object of exhaustive studies, which evidence
promising applications (12). The proteolytic properties of
dairy lactic acid bacteria are among the best characterized to date
(5, 13). This is a consequence of the impact of
proteolysis on the physiology of these organisms as well as on the
development of texture and flavor of dairy products (6,
18). Proteolysis on milk proteins is initiated by a cell wall-associated proteinase, which hydrolyzes caseins into
oligopeptides. The generated peptides are mainly translocated via the
oligopeptide transport system and, further, hydrolyzed by a pool of
intracellular peptidases, which include endopeptidases,
aminopeptidases, dipeptidases, tripeptidases, and dipeptidyl peptidases
(13).
Lactobacillus sakei is the most competitive species in meat
fermentation and therefore constitutes a frequently used starter culture. The proteolytic events that occur during meat processing also
lead to the generation of small peptides and free amino acids, which
are considered to be flavor compounds (1, 31). In
fermented meat products, muscle as well as microbial enzymes are
responsible for the proteolytic changes, but their roles remain elusive
(21, 31). Particularly, the studies on the proteolytic
system of meat lactobacilli are rather limited. It has been shown that
several Lactobacillus spp. exhibit proteolytic activity on
porcine muscle myofibrillar and sarcoplasmic proteins (7, 8,
28). These studies highlighted the potential role of L. sakei in amino acid and peptide generation especially from
sarcoplasmic proteins. Attention has also been focused on intracellular
peptidases of L. sakei, but only a limited number of general
peptidases (a broad-specificity aminopeptidase, dipeptidase, and
tripeptidase) have been purified and characterized so far (23,
24, 25).
Despite the fact that proline is not an abundant amino acid in the
major muscle myofibrillar and sarcoplasmic proteins, the unique
structure of proline in the polypeptide chains may restrict their
susceptibility to proteolysis (13). Most peptidases with general specificity are, in fact, unable to split peptide bonds involving proline, and specific enzymes are required to avoid proline-peptide accumulation. The X-prolyl-dipeptidyl aminopeptidase (X-PDP, PepX; EC 3.4.14.5) is the most-studied proline-specific peptidase in dairy lactic acid bacteria (5, 13), but it
has not been described in meat lactobacilli. The enzyme, also know as
dipeptidyl peptidase IV, has its counterpart in mammals; for instance,
it was recently purified from porcine skeletal muscle (29). The X-PDP is able to release specifically X-Pro
dipeptides from the N termini of peptide chains. Proline is one of the
free amino acids required for optimal growth by L. sakei
(22), but its concentration is limited in raw meat
(27). Thus, specific proline-specific peptidases could be
also critical in the proteolytic chain for the supply of amino acids,
which can be essential to support the growth and fermentative
capability of lactobacilli.
In this work, we described the purification and characterization of an
X-PDP from L. sakei. The properties of the purified enzyme
are discussed in relation to those of the dipeptidyl peptidases previously characterized and the conditions inherent to the meat environment. To our knowledge, this is the first report on the presence
of a proline-specific peptidase in a meat Lactobacillus species.
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MATERIALS AND METHODS |
Bacterial strain and growth conditions.
L. sakei
CECE (Colección Española de Cultivos Tipo) 4808, originally
isolated from sausages (26), was routinely grown in MRS
broth or agar (Oxoid, Hampshire, United Kingdom) at 30°C. For
purification purposes, the organism was grown in 1.5-liter batch
cultures of MRS broth (Oxoid) at 30°C, without agitation. The medium
was inoculated with an overnight culture (0.3%) and was incubated to a
final optical density of 3.0 to 3.2 at 660 nm.
Enzyme assay.
X-PDP activity was determined throughout the
purification and characterization work using
L-glycine-L-proline-7-amido-4-methylcoumarin (AMC; Sigma, St. Louis, Mo.) as substrate. The reaction mixture consisted of 250 µl of 50 mM Tris-HCl (pH 7.5) containing 0.2 mM
substrate and 50 µl of enzyme. The release of fluorescence was
determined after 10 min of incubation at 37°C in a multiscan fluorimeter (Fluoroscan II; Labsystems, Oy, Finland) at excitation and
emission wavelengths of 360 and 440 nm, respectively. Three replicas
were measured for each experimental point. One unit of enzyme activity
was defined as the amount of enzyme that hydrolyzes 1 µmol of
substrate per h at 37°C.
Purification.
The cell extract used for purification was
obtained by lysozyme and ultrasonic treatments as described elsewhere
(7, 28). The purification procedure consisted of the
following steps.
(i) Ammonium sulfate fractionation.
The cell extract was
fractionated with ammonium sulfate in two steps by addition of the
reagent at 4°C and further incubation for 20 min. The precipitate
obtained between 50 and 70% saturation was collected by centrifugation
(15,000 × g for 20 min at 4°C) and dissolved in 50 mM Tris-HCl (pH 7.5).
(ii) Hydrophobic interaction chromatography.
The protein
fraction obtained by ammonium sulfate precipitation was applied to a
phenyl-Sepharose Fast Flow column (23 by 1.3 cm; Pharmacia, Uppsala,
Sweden) equilibrated with 50 mM Tris-HCl (pH 7.5) containing 0.5 M
(NH4)2SO4. The retained proteins
were eluted at 4 ml/min, using a linear ammonium sulfate gradient from 0.5 to 0 M (NH4)2SO4 (340 ml) and a
final isocratic step at 0 M
(NH4)2SO4, in 50 mM Tris-HCl (pH
7.5) (160 ml). The eluant was collected in 6-ml fractions.
(iii) First strong anion-exchange chromatography.
The active
sample from the previous chromatographic step was applied to a Resource
Q anion-exchange column (6 ml; Pharmacia) equilibrated with 20 mM
sodium phosphate buffer (pH 6.0). Proteins were eluted at 6 ml/min,
applying an initial isocratic step in the equilibration buffer (18 ml)
followed by a linear gradient from 0 to 0.3 M NaCl in the same buffer
(120 ml). The eluant was collected in 2-ml fractions.
(iv) Weak anion-exchange chromatography.
The active sample
obtained from the first anion-exchange chromatography was applied to a
Biosep-DEAE column (75 by 7.8 mm; Phenomenex, Torrance, Calif.)
equilibrated with 20 mM sodium phosphate buffer (pH 6.0). Proteins were
eluted at 1 ml/min using a linear gradient from 0 to 0.3 M NaCl in the
equilibration buffer, and fractions of 1 ml were collected.
(v) Gel filtration chromatography.
The active sample
concentrated to 1.5 ml was applied to a Sephacryl 200 HR column (100 by
1.5 cm, Pharmacia) equilibrated with 50 mM Tris-HCl (pH 7.5) containing
0.1 M NaCl. Proteins were eluted at 10 ml/h, and fractions of 2 ml were collected.
(vi) Second strong anion-exchange chromatography.
The active
sample was again applied to a Resource Q anion-exchange column (6 ml;
Pharmacia) equilibrated with 20 mM sodium phosphate buffer (pH 6.0)
containing 0.1 M NaCl. Proteins were eluted at 4 ml/min in a narrower
salt gradient from 0.1 to 0.25 M NaCl (80 ml) in the same buffer.
Fractions of 1 ml were collected.
Every chromatographic separation was carried out in a fast protein
liquid chromatography system (Pharmacia) except for the gel filtration
step, which was performed by classical chromatography. When required,
active fractions from each purification step were concentrated by
ultrafiltration through a 30-kDa-cutoff membrane (Millipore, Bedford,
Mass.). Desalting and buffer exchange of active fractions were carried
out by gel filtration on a PD10 column (Pharmacia).
Determination of protein concentration.
The protein
concentration was determined by the BCA (bicinchoninic acid) method
with the BCA protein assay reagent (Pierce, Rockford, Ill.).
Determination of molecular mass.
Purification was monitored
by polyacrylamide gel electrophoresis (PAGE) under denaturing
conditions, using sodium dodecyl sulfate (SDS), and under native
conditions (14). In both cases, 10% polyacrylamide gels
were used. The molecular mass of the denatured enzyme was estimated by
using a broad-range molecular weight protein standard (Bio-Rad,
Richmond, Calif.). Proteins were visualized after Coomassie brilliant
blue R-250 staining. The relative molecular mass of the native enzyme
was determined by gel filtration on a Sephacryl 200 HR column as
described above. The column was calibrated with the following standard
proteins (Sigma):
-amylase (200 kDa), aldolase (158 kDa), albumin
(68 kDa), chymotrypsinogen A (25 kDa), and cytochrome c
(12.4 kDa).
Dependence of pH and temperature.
The dependence of pH was
determined in the range from 4.0 to 8.5 using the following buffers: 50 mM sodium acetate, pH 4.5 to 5.5; 50 mM sodium phosphate, pH 6.0 to
7.0; and Tris-HCl, pH 7.5 to 8.5. The dependence of temperature was
determined at optimum pH in the range from 5 to 60°C as previously
described (24). In every case, activity was expressed as a
percentage of the activity obtained at either optimum pH or temperature.
Effects of chemical agents and metal cations on activity.
Effects of potential inhibitors on X-PDP activity were assayed by the
addition of several chemical agents and metal salts, at 0.1 or 1 mM, to
the reaction buffer. Activity was assayed as described above and
expressed as a percentage of the activity obtained in the absence of
the added compound.
Substrate specificity.
The relative activity of the X-PDP
against several fluorescent substrates was determined according to the
standard activity assay. The relative hydrolysis of several
dipeptidyl-p-nitroanilide (pNA) substrates was also
determined. The reaction mixture consisted of 250 µl of 50 mM
Tris-HCl (pH 7.5) containing 0.5 mM substrate and 50 µl of enzyme.
Absorbance was determined at 405 nm in a multiplate reader (ELX800;
BioTek Instruments, Madrid, Spain) after 15 min of incubation. The
relative hydrolysis of several peptides was estimated by measuring the
disappearance of the substrate by capillary electrophoresis (24,
25).
Determination of kinetic parameters.
Kinetic parameters of
the purified enzyme were estimated for Gly-Pro-AMC and Lys-Ala-AMC,
using concentrations ranging from 0.005 to 0.06 and 0.01 to 0.15 mM,
respectively; those for Ala-Pro-pNA and Gly-Pro-pNA were also
determined, using concentrations ranging from 0.01 to 1 mM. Activity
was measured continuously at 37°C as described above, and kinetic
parameters were calculated from Lineweaver-Burk plots.
 |
RESULTS |
Purification of the enzyme.
The X-PDP of L. sakei
was purified by selective fractionation with ammonium sulfate and five
chromatographic steps. Results of the purification procedure are
summarized in Table 1. The highest X-PDP
activity precipitated at 50 to 70% ammonium sulfate saturation, with a
recovery of almost 90%. From the phenyl-Sepharose column, the unique
peak of X-PDP activity partially coeluted with aminopeptidase activity
at 0 M (NH4)2SO4 (data not shown).
Chromatographic separation on the strong anion-exchange column
(Resource Q) allowed further isolation of X-PDP activity, which eluted
as a unique peak at 0.195 M NaCl (data not shown). In this purification
step, an important enrichment in specific activity was obtained (Table 1). From the Biosep-DEAE column, the enzyme eluted at 0.22 M NaCl. This
chromatographic step resulted in 148-fold purification, but still two
major protein bands coeluted in the active fractions, as shown by
electrophoretic analysis under native (Fig. 1B) and denaturing (Fig.
1A) conditions. Electrophoretic analysis of the active fractions
eluting from the Sephacryl 200 HR gel filtration chromatography showed
almost complete disappearance of the protein band of lower molecular
mass, suggesting that the protein band of approximately 88 kDa
corresponded to the enzyme (Fig. 1). The final chromatographic step on the strong anion-exchange column (Resource Q), using a narrower salt gradient, resulted in a single protein band on both an SDS-containing and a native polyacrylamide gel
(Fig. 1). The complete purification procedure yielded 6.9% of the
total activity, with an increase in specificity of 716.6-fold.

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FIG. 1.
Electrophoretic analysis of X-PDP active fractions
obtained at different purification steps. (A) SDS-PAGE; (B) native
PAGE. Lane 1, molecular weight markers (positions indicated in
kilodaltons); lane 2, cell extract; lane 3, Phenyl-Sepharose
chromatography; lane 4, Resource Q chromatography (0 to 0.3 M NaCl);
lane 5, Biosep-DEAE chromatography; lane 6, Sephacryl 200 HR
chromatography; lane 7, Resource Q chromatography (0.1 to 0.25 M
NaCl).
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Molecular mass.
The molecular mass of the purified enzyme
estimated by SDS-PAGE was approximately 88 kDa (Fig. 1). The relative
molecular mass of the native enzyme estimated by gel filtration was
around 170 kDa, suggesting that the X-PDP is composed of two subunits of equal molecular mass.
Dependence of pH and temperature.
The purified enzyme is
active in a broad pH range from 4.0 to 8.5, with an optimum at pH 7.5 (Fig. 2). Considerable activity (10 to
60%) was retained at pHs between 4.5 and 5.5. The optimum temperature
was 55°C. Enzyme activity decreased significantly below 45°C,
although substantial activity (around 20 to 30%) was observed at 15 to
25°C (Fig. 2).

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FIG. 2.
Effects of pH ( ) and temperature ( ) on X-PDP
activity from L. sakei using Gly-Pro-AMC as substrate. The
activities at optimal pH and temperature were given a value of 100%,
which corresponded to 0.011 and 0.012 U (µmol h 1),
respectively. The degree of purification of the enzyme preparation used
was of 716.6-fold.
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Effects of chemical agents and metal cations.
The presence of
chelating agents such as EDTA and o-phenanthroline had no
effect on activity, indicating that the purified X-PDP is not a
metalloenzyme (Table 2). The reducing
agents dithiothreitol and 2-mercaptoethanol as well as the sulfhydryl
group reagents iodoacetate and
trans-epoxysuccinyl-L-leucylamido-(4-guanidino)butane (E-64) did not have significant effect on activity (Table 2). These
results indicate that sulfhydryl groups are not involved in the
catalytic activity. Activity was reduced to almost 50% in the presence
of phenylmethylsulfonyl fluoride (1.0 mM) and completely abolished in
the presence of 3,4-dichloroisocoumarin, which are both specific
inhibitors of serine proteinases (Table 2). The effects of amastatin,
bestatin, and puromycin, which are typical inhibitors of exopeptidases,
were negligible (Table 2). Pepstatin A, which is an aspartic proteinase
inhibitor, had no effect on activity (Table 2). The presence of
Cu2+, Hg2+, and Zn2+ caused 53 to
78% inhibition, while the other divalent cations tested had no
significant effect on enzyme activity (Table
3).
Substrate specificity.
The specificity of the purified enzyme
was essentially confined to X-Pro- and X-Ala-AMC or -pNA substrates
(Table 4). Maximal hydrolysis rates were
obtained when proline was in the N-penultimate position. The hydrolysis
of substrates containing alanine in the N-penultimate position was at
best 10% of the activity on X-Pro N-terminal substrates (Table 4). The
enzyme did not show aminopeptidase activity since it did not hydrolyze
amino acyl-AMC substrates (Arg-, Gly-, Leu-, and Pro-AMC [Table 4]).
The lack of hydrolysis of the substrate Ala-Ala-Phe-AMC also indicated
that the purified enzyme did not have tripeptidyl peptidase activity
(Table 4). Among colorimetric substrates, Ala-Pro-pNA was hydrolyzed at
the highest rates. The relative activities toward these substrates showed that the N-terminal residue exerted an effect on the specificity with the following order of preference: alanine, arginine, and glycine.
The activity of the X-PDP against several peptides was analyzed by
capillary electrophoresis (Table 5).
Dipeptidase activity was not detected against Gly-Pro. Several peptides
with sequences X-Pro or X-Ala at the N terminus were hydrolyzed. Among those,
-casomorphin fragment 1-3 was hydrolyzed at the highest rates, while only 1 to 12% relative activity was observed on the other
hydrolyzed peptides (Table 5). In general, the enzyme showed preference
for X-Pro N-terminal peptides (Table 5). Moreover, diprotin A, which
also has been considered as an inhibitor of these enzymes, was
hydrolyzed at a similar rate as tetraalanine. The enzyme did not
display specificity for X-Pro-Pro N-terminal peptides such as
bradykinin. Further studies would be required to distinguish the
influence of the amino acid residue located at every position of a
peptide on hydrolytic rates.
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TABLE 4.
Relative activity of purified (716.6-fold) X-PDP on
various fluorescent (AMC derivatives) and colorimetric (pNA
derivatives) substrates
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Kinetic parameters.
The Km and
Vmax values determined for several fluorescent
and colorimetric substrates are shown in Table
6.
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TABLE 6.
Kinetic parameters of purified (716.6-fold) X-PDP
for fluorescent (AMC derivatives) and colorimetric (pNA
derivatives) substrates
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DISCUSSION |
In this study, we describe the purification and characterization
of an X-PDP from L. sakei, a species commonly involved in meat fermentation. The biochemical properties of this enzyme and its
possible role in nitrogen metabolism are discussed.
X-PDP activity is widely distributed in dairy lactic acid bacteria but
has not been described in meat lactobacilli. The enzyme is the
most-studied proline-specific peptidase, and it has been purified from
lactococci and several dairy Lactobacillus species (5). In L. sakei, a separate enzyme appeared to
be responsible for the majority of Gly-Pro-AMC-hydrolyzing activity, as
the first purification step on the phenyl-Sepharose column resulted in
a unique peak of activity. This substrate could also be sequentially hydrolyzed by the major aminopeptidase of L. sakei described
to date (24). This enzyme eluted as a separated peak at
0.33 M ammonium sulfate (data not shown). However, the low hydrolysis rates of this general aminopeptidase on N-terminal proline and glycine
residues likely prevented the detection of a second peak of activity.
To our knowledge, the complete purification procedure applied in this
study resulted in a specific activity enrichment superior to the one
obtained for previously purified X-PDP from dairy lactic acid bacteria
(5).
The molecular mass of L. sakei X-PDP was in good agreement
with data previously reported for other lactic acid bacteria. Most of
the X-PDP enzymes are considered to be dimers with a subunit molecular
mass of 80 to 95 kDa (3, 11, 15, 16, 32, 33). However, the
enzymes of Lactobacillus casei and of some strains of
Lactobacillus helveticus and Lactobacillus
delbrueckii have been found to be monomers or trimers (2, 9,
17, 19, 20).
The optimum pH of L. sakei X-PDP was in the pH range (6.5 to
7.5) reported for the corresponding enzymes of other lactic acid bacteria (2, 3, 9, 10, 11, 16, 19, 20, 30, 32). The
activity of L. sakei X-PDP at acidic pH may favor its implication in peptide hydrolysis during meat fermentation. Remarkably, this activity is even higher than the activity displayed by the muscle
dipeptidyl peptidase IV at acidic pH (29). The purified peptidase showed a relatively high optimal temperature (55°C), as it
was detected for the corresponding peptidase from Lactobacillus lactis (16). However, most of these enzymes have an
optimum between 45 and 50°C (2, 3, 9, 11, 16, 19, 20, 30, 32,
33). The purified X-PDP retained substantial activity at
temperatures around those used in meat fermentation processes (15 to
25°C). This fact makes also feasible the participation of L. sakei X-PDP in degradation of muscle-derived peptides during meat fermentation.
The use of inhibitors of the different classes of proteases indicated
that the purified X-PDP belongs to the serine protease group. The
corresponding enzymes purified from dairy lactic acid have been
unequivocally assigned to the same protease class. Analysis of the
active site of the enzyme from L. lactis revealed that the
consensus sequences differ from those of other serine protease families. The lactococcal enzyme and the mammalian dipeptidyl peptidase
IV were proposed to be classified in a new group of serine proteases
related to prolyl endopeptidases (4). Several divalent
cations behaved as inhibitors of the purified enzyme from L. sakei. The same cations (Cu2+, Hg2+, and
Zn2+) have also been reported to be strong inhibitors of
the X-PDP activity of L. helveticus CNRZ 32, L. delbrueckii subsp. bulgaricus, and L. acidophilus (3, 10).
The enzyme hydrolyzed almost exclusively substrates with an X-Pro
N-terminal sequence. The slight hydrolysis of X-Ala N-terminal substrates seems to be also a general characteristic of this enzyme (5, 29). In fact, the affinity of L. sakei
X-PDP for Gly-Pro-AMC was three times higher than the affinity for
Lys-Ala-AMC, as deduced from Kms. The X-PDP of
other lactic acid bacteria showed Kms for Gly-Pro-AMC and Lys-Ala-AMC of the same order of magnitude (15, 16). The highest activity of the X-PDP from dairy organisms has
been reported to be against substrates with N-terminal uncharged (Ala
or Gly) or basic (Arg) residues. Specificity studies of L. sakei X-PDP on pNA derivatives indicated that the nature of the N-terminal residue exerts an important effect on activity. Thus, the
rate of hydrolysis of Gly-Pro-pNA was fourfold lower than that of
Ala-Pro-pNA, likewise, the Kms reflected about
fourfold-higher affinity for the last substrate. This is not in
agreement with what has been stated by other authors (15).
The differences between the Kms for Gly-Pro-AMC
and Gly-Pro-pNA were even higher (more than sixfold), indicating that
the affinity greatly depends on the C-terminal group as well. The
influence of this C-terminal group on Kms was
also pointed out by Lloyd et al. (15). The substrate
bradykinin, which contains a X-Pro-Pro sequence, was not hydrolyzed,
confirming the specificity of the enzyme (15). Comparison
of the specificities of L. sakei X-PDP and the porcine muscle dipeptidyl peptidase IV (29) reveals important
differences. While Kms for fluorescent and
colorimetric substrates are similar, Vmaxs, and
therefore maximum catalytic activities, are higher with L. sakei X-PDP. Nevertheless, the significance of these differences in peptide degradation should be determined by systematic specificity studies.
Overall, this study provides substantial information on the potential
role of the X-PDP from L. sakei in peptide degradation on
the basis of its biochemical properties. It is also anticipated that
this activity may have two major consequences during meat fermentation:
(i) physiological, through the release of essential or stimulating
amino acids required for optimal growth, and (ii) technological, by
accelerating the whole process and modifying the composition of flavor compounds.
 |
ACKNOWLEDGMENTS |
This work was supported by grant ALI97-0353 from CICYT (Spain).
The postdoctoral contract to Y. Sanz from MEC (Spain) is acknowledged.
 |
FOOTNOTES |
*
Corresponding author. Mailing address: Instituto de
Agroquímica y Tecnología de Alimentos (CSIC), Apartado
73, 46100 Burjasot (Valencia), Spain. Phone: 34 96 3900022. Fax: 34 96 3636301. E-mail: yolsanz{at}iata.csic.es.
 |
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Applied and Environmental Microbiology, April 2001, p. 1815-1820, Vol. 67, No. 4
0099-2240/01/$04.00+0 DOI: 10.1128/AEM.67.4.1815-1820.2001
Copyright © 2001, American Society for Microbiology. All rights reserved.
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