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Food Sci. Biotechnol. 21(2): 497-502 (2012)
DOI 10.1007/s10068-012-0063-8
Development of a Time-Temperature Integrator System Using
Burkholderia cepacia Lipase
Won Kim, Euna Park, and KwangWon Hong
Received: 24 October 2011 / Revised: 24 November 2011 / Accepted: 28 November 2011 / Published Online: 30 April 2012
© KoSFoST and Springer 2012
Abstract A time-temperature integrator (TTI) is a device
used to show a time-temperature dependent change that
reflects the temperature history and quality status of the
food to which it is attached. An enzymatic TTI system
based on the reaction between Burkholderia cepacia lipase
and tricaprylin, which causes a pH change, was developed.
The temperature dependence of the response rate of this
new lipase-type TTI was modeled using the Arrhenius
equation, and the estimated activation energy was calculated
as 70.61±11.10 kJ/mol (±95% confidence interval). The
TTI response was validated under dynamic storage conditions
with independent variable temperature experiments, and a
good agreement was obtained between the predicted and
measured values.
Keywords: time-temperature integrator (TTI), Burkholderia
cepacia lipase, Arrhenius equation, activation energy
Introduction
Temperature is a decisive factor influencing the quality and
safety of a food product during storage and distribution.
Therefore, monitoring and recording the temperature history
for the entire life cycle of food products is very important
for predicting quality and shelf-life of food products (1). A
time-temperature integrator/indicator (TTI) is a simple
device that monitors and records the time-temperature
history of food products to which it is attached as a label
(2). A TTI indicates irreversible visual responses such as
color changes or a moving color front through biological,
chemical, and physical reactions (3). The visual response
of the TTI helps consumers predict the quality and
expiration date of products more easily (4). Many cases of
applying a TTI to food products have been being reported,
as inexpensive and effective TTIs are being developed and
various studies on the quality index of food products have
been conducted. A TTI has been applied to various
refrigerated and frozen food products such as meat, poultry,
dairy products, seafood, and vegetables as well as during
the milk sterilization process (5-10). Generally, the response
of a TTI and decreased food quality must correspond to
successfully apply a TTI to food products. In other words,
the activation energy (Ea), indicating the temperature
sensitivity of the TTI response, should be similar to the Ea
of the quality change in the food product (11,12).
Therefore, systematic kinetic research on food product
deterioration and the response of a TTI is required to use
a TTI as a quality indicator.
TTIs currently being used for commercial purposes can
be classified into diffusion-based TTI, enzymatic TTI,
polymeric TTI, and microbial TTI (4,13). Among these,
the only enzymatic TTI, VITSAB TTI (Vitsab A.B.,
Malmö, Sweden), is based on an irreversible color change
induced by a pH decline resulting from the controlled
enzymatic hydrolysis of a lipid substrate (3,4). The indicator
consists of 2 separate compartments containing an aqueous
solution of a lipolytic enzyme such as pancreatic lipase and
another containing the liquid substrate suspended in an
aqueous medium and a pH indicator mix (4). As substrates
of lipase, various triacylglycerols such as tricaproin,
tripelargonin, and tributyrin can be used (3). When using
these substrates, it is typically difficult to obtain stable
substrates emulsion in low temperature, and thus selection
of proper emulsifier is critical in the process (14).
Nevertheless, as lipase-based TTI can be used with
different combinations of enzymes and substrates, it has a
Won Kim, Euna Park, KwangWon Hong ( )Department of Food Science and Biotechnology, Dongguk University,Seoul 100-715, KoreaTel: +82-2-2260-3369, Fax: +82-2-2260-3369E-mail: [email protected]
RESEARCH ARTICLE
498 Kim et al.
merit that distinct TTI with different activation energy can
be developed and applied to a variety of food quality
change (3,4).
Burkholderia cepacia lipase displays high stability at
different temperatures and pHs and can tolerate various
organic solvents (15). Additionally, developing a TTI using
this lipase would be economical and could be considered a
great commercial utilization value, because this lipase is
secreted outside of the cell and is able to create various
catalytic reactions in liquefied or non-liquefied states.
In this study, a lipase-type TTI system was developed
based on the reaction in which the B. cepacia lipase
hydrolyzes tricaprylin. The kinetic parameters of this TTI
were calculated through a color change at various constant
temperatures. Additionally, a dynamic model was developed
based on the calculated kinetic parameters to investigate
the accuracy of the TTI and its applicability to food
products.
Materials and Methods
Preparation of a B. cepacia lipase (BCL)-based TTI
The lipase used in this study was commercially available as
Amano Lipase PS (Sigma-Aldrich, St. Louis, MO, USA),
which is the lipase from B. cepacia. The TTI reaction
mixture was formed with 4 mM tricaprylin (C8:0), 0.1%
Triton X-100, 2.5% Mcilvaine’s buffer (0.2 M Na2HPO4,
0.1 M citric acid, pH 7.5) and an 8.5% pH indicator
solution (mixture of 0.1% of bromothymol blue, methyl
red, and neutral red at 12:4:1 ratio). The pH indicator led
to an irreversible color change from green to orange and
finally to red (the endpoint), indicating a progressive
decline from pH 8.0 to 6.0. The TTI reaction mixture was
emulsified by a homogenizer (Diax-900; Heidolph, Kelheim,
Germany) for 3 min at 26,000 rpm.
Determining BCL-TTI kinetic parameters The reaction
was started in 50 mL of BCL-TTI reaction mixture by
adding 1 unit of BCL to each mixture that had reached
constant temperature after pre-storing the incubator at 5
different temperatures (5, 10, 15, 20, and 26oC) for 3 h.
The ∆E value of the BCL-TTI reaction mixture was
measured under the conditions of D65 illumination and a
2o observation angle using a colorimeter (Minolta CM-
2500d; Minolta Co., Ltd., Osaka, Japan). All experiments
were repeated 3 times and reported as the mean and
standard deviation (SD).
The chromaticity change (∆E value) was measured using
CIE Lab color space coordinates to objectively describe the
irreversible BCL-TTI color change. The BCL-TTI reaction
rate was determined using the ∆E value change per unit
time at different constant temperatures, and the ∆E value
was expressed by the following equation.
(1)
where, L* is the difference in brightness (white-black)
change between t=0 and measured unit time. a* is the
difference in redness-greenness, and b* is the difference in
yellowness-blueness (16).
The TTI response function according to the ∆E value
can be expressed as follows (1).
(2)
where, F(X) is total TTI color difference, in other words
the ∆E value. The response rate constant under each storage
temperature was determined through linear regression
analysis of the ∆E value against time t (h). The temperature
dependence of the TTI response was described with the
Arrhenius equation and expressed as follows.
(3)
where, k0 is the Arrhenius pre-exponential factor (1/h)
value, Ea is activation energy (kJ/mol), R is the ideal gas
constant (8.314×10−3 kJ/kmol), and T is absolute
temperature (K).
Measurement of the BCL-TTI color change under
dynamic storage conditions For the dynamic storage
experiments, 4 non-isothermal temperature storage profiles
were used. Temperature profile 1 (TP.1) involved storage
for 18 h at 8oC, 2 h at 13oC, 2 h at 18oC, 2 h at 23oC, and
finally 24 h at 12oC. Temperature profile 2 (TP.2) included
a step wise changing profile of 3 h at 25oC and 3 h at 18oC.
Temperature profile 3 (TP.3) and profile 4 (TP.4) included
a periodically alternating 6 h cycles of (2 h at 20oC, 2 h at
15oC and 2 h at 10o) and (2 h at 20oC, 2 h at 12oC, 2 h at
5oC), respectively. BCL was added to 50 mL of the BCL-
TTI reaction mixture at a concentration of 0.02 units/mL to
measure the change in ∆E per unit time during storage in
a programmable incubator. All samples were measured 6
times. The response rate k for each temperature profile was
calculated using a linear regression analysis based on the
measured ∆E value. This was compared and analyzed with
the predicted value to check for significance and correlation.
The relative error between the predicted and measured
reaction rates were calculated using the following equation.
Applicability was examined by setting the relative error
limit of the predicted and measured values as <20%
(17,18).
(4)
Statistical analysis All linear regression analyses were
conducted using PASW statistics 18.0 (SPSS Inc., Chicago,
∆E ∆L∗( )2
∆a∗( )2
∆b∗( )2
+ +[ ]=
F X( ) ktti t⋅=
k k0exp
Ea
R T⋅---------–⎝ ⎠
⎛ ⎞⋅=
%RE kmeasured kpredicted–( ) kmeasured⁄ 100×=
A TTI System Using Burkholderia cepacia Lipase 499
IL, USA). Additionally, the 95% confidence interval of the
BCL-TTI Ea value was calculated. All data points are
indicated as mean values and SD indicated by error bars.
Results and Discussion
BCL-TTI color changes The changes in pH and color
after starting the TTI reaction were measured. Figure 1
shows a good correlation between pH and the TTI
chromaticity change (∆E value) at 25oC. The pH of the TTI
decreased proportionally from 8.0 to 5.88±0.05, whereas
the ∆E value increased proportionally from 0 to 27.13±
0.31. The TTI-specific color change is indicated in Fig. 2.
The distinct color change to the red was obtained when the
∆E response reached a value of 25, and that time was
selected as the end point of the BCL-TTI system.
Arrhenius analysis of the BCL-TTI The TTI was
stored at different constant temperatures (5, 10, 15, 20, and
26oC) to determine the reaction order and the reaction rate
k by measuring the ∆E value changes according to time.
The times to reach the endpoint (∆E=25) were 10.73 h at
26oC, 15.93 h at 20oC, 27.71 h at 15°C, 49.34 h at 10oC,
and 90.38 h at 5oC (Fig. 3). As a result of the linear
regression analysis, the response rate k was 2.32 (R2=
0.995) at 26oC, 1.56 (R2=0.997) at 20°C, 0.90 (R2=0.996)
at 15oC, 0.48 (R2=0.990) at 10oC, and 0.24 (R2=0.961) at
5oC, and all coefficient of determinations (R2) were ≥0.96
(Table 1). The TTI activation energy (Ea) can be calculated
by plotting a curve between 1/T and lnk (Fig. 4). The BCL-
TTI Ea was 70.61±11.10 kJ/mol at the 95% confidence
interval. Among the commercially available TTIs, the Ea
values of the VITSAB Type M, Fresh Check Indicator
Type A6, and Fresh Check Indicator TJ2 were 68.70±9.03,
83.60±10.71, and 92.67±9.76 kJ/mol, respectively (12,19),
so the BCL-TTI had similar Ea values as these TTIs.
Fig. 2. Color response of the Burkholderia cepacia lipase (BCL)-based time temperature integrator (TTI) from activation to endpoint at 25oC.
Fig. 3. Response of the Burkholderia cepacia lipase (BCL)-based time temperature integrator (TTI) stored under isothermalconditions.
Fig. 1. pH and ∆E values changes in the Burkholderia cepacia
lipase (BCL)-based time temperature integrator (TTI) at 25oC.
500 Kim et al.
Generally, the difference in Ea between a food product and
TTI must be <±20 kJ/mol to apply TTI to food products
(3).
The quality loss in various food products was measured
using an Arrhenius analysis, and the Ea values are reported.
The growth Ea values for Pseudomonas spp. and
psychrotrophic microorganisms in refrigerated beef were
74.29 and 85.50 kJ/mol, respectively (20). The growth Ea
values of Pseudomonas spp. and total aerobic bacteria of
poultry products were 78.7±18.8 and 91.2±6.7 kJ/mol
(±95%, confidence interval, CI), respectively, so applying a
TTI with an Ea of 79.9±7.5 kJ/mol (±95% CI) represented
poultry spoilage (21). Additionally the growth Ea values of
Pseudomonas spp. in fish such as turbot and bouqe were
86.10 and 81.6±11.6 kJ/mol (±95% CI), respectively
(12,22). The quality change in these fish can be represented
by TTIs such as the Fresh Check Indicator type A6
(83.60±10.71 kJ/mol), the VITSAB type M (68.70±9.03
kJ/mol) or the VITSAB type S (102.1±6.2 kJ/mol) with
similar Ea values (12,22). Thus, the BCL-TTI can also be
applied as an indicator to show temperature variations in
these food products.
Dynamic modeling of the BCL-TTI The kinetic
parameters of BCL-TTI were verified under non-isothermal
conditions, simulating temperature fluctuations which may
occur in the chill chain. BCL-TTIs were stored under
dynamic temperature profiles. The comparison of the
actual ∆E values and the predicted ∆E values by dynamic
modeling of each temperature profile are shown in Fig. 5.
The time it took to reach the endpoint (∆E=25) for each
profile was 46.12 h in TP.1, 14.60 h in TP.2, 30.15 h in
TP.3, and 36.08 h in TP.4. The ∆E values actually measured
from these times (tend) were 24.71±0.85, 23.1±0.45,
22.66±0.78, and 24.42±0.64 (±SD), respectively. These
∆E values were very close to the endpoint value of 25, so
we determined that the predicted value and the actually
measured value closely matched.
Table 2 shows the response rate k (1/h) predicted and
measured for the 4 temperature profiles along with their
relative errors (% RE). Each response rate k (1/h) was
calculated using linear regression analysis after predicting
and measuring the ∆E value according to tend. All
correlation coefficients (R2) were 0.970. Additionally, the
relative errors between the predicted and measured values
for each temperature profile were 4.05, 6.95, 10.92, and
3.75%, respectively, indicating a very high correlation. The
results showed that dynamic modeling through kinetic
parameter and numerical analysis worked well.
In conclusion, various kinetic parameters were calculated
through the steady state and 4 types of temperature profiles
were used to verify these variables to determine the
usability of the BCL-TTI developed in this study. As a
result of comparing the measured and predicted values
using a dynamic modeling numerical analysis, we verified
that all 4 types of models were very highly correlated.
Therefore, it seems that a BCL-based TTI [70.61±11.10
kJ/mol (±95% CI)] will become an effective tool to
evaluate food quality in products with similar Ea values.
Acknowledgments This research was supported by the
Agriculture Research Center (ARC, 710003-03-1-SB110)
program of the Ministry for Food, Agriculture, Forestry
and Fisheries, Korea.
Fig. 4. Arrhenius plot of the Burkholderia cepacia lipase(BCL)-based time temperature integrator (TTI) response rate.
Table 1. Arrhenius kinetic parameters of the Burkholderia
cepacia lipase (BCL)-based time temperature integrator (TTI)
Temperature(oC)
k (1/h) R2 Ea±95% CI1)
(kJ/mol)R2
26 2.32 0.995
70.61±11.10 0.993
20 1.57 0.997
15 0.90 0.996
10 0.51 0.982
5 0.28 0.910
1)Ea, activation energy; CI, confidence intervals
Table 2. Correlation between the dynamic modeling and theBurkholderia cepacia lipase (BCL)-based time temperatureintegrator (TTI) response by regression analysis at differenttemperature profiles
Predicted Measured% RE1)
k (1/h) R2 k (1/h) R2
TP1 0.59 0.983 0.57 0.977 4.05
TP2 1.62 0.995 1.51 0.994 6.95
TP3 0.83 0.999 0.74 0.990 10.92
TP4 0.69 0.998 0.67 0.993 3.75
1)RE, relative error
A TTI System Using Burkholderia cepacia Lipase 501
Fig
. 5.
Pre
dic
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an
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easu
red
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502 Kim et al.
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