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<field name="value">Benito Román, Oscar</field>
<field name="authority">59</field>
<field name="confidence">500</field>
<field name="orcid_id">0000-0002-4418-0045</field>
<field name="value">Sanz Díez, Mª Teresa</field>
<field name="authority">530</field>
<field name="confidence">500</field>
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<field name="value">Illera Gigante, Alba Ester</field>
<field name="authority">296</field>
<field name="confidence">500</field>
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<field name="value">Melgosa Gómez, Rodrigo</field>
<field name="authority">357</field>
<field name="confidence">500</field>
<field name="orcid_id"/>
<field name="value">Beltrán Calvo, Sagrario</field>
<field name="authority">57</field>
<field name="confidence">500</field>
<field name="orcid_id"/>
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<element name="none">
<field name="value">2019-03-20T12:46:10Z</field>
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<field name="value">2019-03-20T12:46:10Z</field>
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<element name="issued">
<element name="none">
<field name="value">2018</field>
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<field name="value">http://hdl.handle.net/10259/5081</field>
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<field name="value">Trabajo presentado en: 6th International Congress on Green Process Engineering (GPE 2018), 3 a 6 de junio de 2018, Toulouse</field>
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<field name="value">HPCD is a promising technology to inactivate the enzymes responsible for the juice spoilage, such as PPO and PME. In&#xd;
order to understand the mechanism that induces this inactivation, a study using two commercial enzymes (PPO from&#xd;
mushroom and PME from Aspergillus niger) was carried out. The effect of pressure, temperature, exposure time and ratio&#xd;
CO2/enzyme ratio loaded in the reactor were studied. The experimental results (residual activity) were fitted to a kinetic&#xd;
model that served to develop a complete kinetic study: the kinetic constants, activation volume and activation energy were&#xd;
calculated, as well as the pressure and temperature sensitivity parameters (ZP and ZT, respectively). The changes in the&#xd;
tertiary structure of the enzymes after different treatments were analyzed by fluorescence spectroscopy running different&#xd;
tests: intrinsic fluorescence measurement, KI quenching and ANS binding experiments.&#xd;
In the case of PPO, the experimental results revealed that this enzyme inactivation kinetics fitted the two fraction model,&#xd;
which indicates the presence of labile and stable isoenzymes. Exposure time (2 to 15 minutes), temperature (25 to 45°C)&#xd;
and pressure (50 to 200bar) were the studied experimental conditions that led to different physical states for the CO2 (gas,&#xd;
liquid and supercritical). Despite the different experimental combinations of pressure and temperature tried, a similar&#xd;
inactivation pattern was observed: a sudden decrease in activity (more than 75% of the total activity loss was observed&#xd;
within the first 2 minutes) was followed by a slowed decay. At constant temperature, higher inactivation rates were observed&#xd;
the higher the pressure, obtaining an almost complete inactivation at 200bar after 5 minutes regardless the temperature.&#xd;
When temperature was increased, much faster inactivation rates were observed. ZP and ZT were in the range 69-78bar and&#xd;
27-40°C, respectively.&#xd;
In the case of the commercial PME, the use of supercritical CO2 (pressure 60-180bar, temperature 40-55°C and times up to&#xd;
75 minutes) increased dramatically the PME inactivation rate, showing that pressure had a limited effect on PME inactivation&#xd;
but temperature had an important effect. The pressure and temperature sensitivity parameters (ZP and ZT) confirmed that&#xd;
trend, being in the range from 276 to 450bar and 8.7°C, respectively. The experimental data fitted the first order model and&#xd;
the inactivation kinetics study of PME was completed with the calculations of the activation energy and volume of activation.&#xd;
The ratio CO2/volume of enzyme (g/mL) loaded in the reactor was found to be critical for both enzymes. It was seen that&#xd;
ratios higher than 3 did not improve the inactivation kinetics, being a waste of CO2 from the economic point of view. Bellow&#xd;
that critical value, the inactivation of the enzyme strongly depended on pressure and temperature. In both cases the&#xd;
structure of the enzyme was dramatically affected after exposure to HPCD, as revealed by the fluorescence spectroscopy&#xd;
analysis that showed significant changes in the tertiary structure of the enzyme, which were compatible with the losses in&#xd;
activity observed.</field>
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<element name="sponsorship">
<element name="none">
<field name="value">Spanish Governme nt (MINECO) and the European Regional Development Fund (ERDF) for financial support of&#xd;
project CTQ2015-64396-R and A.E. Illera’s contract. To Junta de Castilla y León and ERDF for financial support of project&#xd;
BU055U16 and O.Benito-Román’s Post-doctoral contract</field>
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<element name="es">
<field name="value">eng</field>
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</element>
<element name="subject">
<element name="en">
<field name="value">PPO</field>
<field name="value">PME</field>
<field name="value">juice</field>
<field name="value">Supercritical Carbon Dioxide</field>
<field name="value">green process</field>
<field name="value">food technology</field>
</element>
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<element name="es">
<field name="value">Ingeniería química</field>
</element>
<element name="en">
<field name="value">Chemical engineering</field>
</element>
</element>
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<element name="title">
<element name="en">
<field name="value">Polyphenol Oxidase (PPO) and Pectin Meth ylesterase (PME) inactivation by means of High Pressure Carbon Dioxide (HPCD)</field>
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