<?xml version="1.0" encoding="UTF-8"?><?xml-stylesheet type="text/xsl" href="static/style.xsl"?><OAI-PMH xmlns="http://www.openarchives.org/OAI/2.0/" xmlns:xsi="http://www.w3.org/2001/XMLSchema-instance" xsi:schemaLocation="http://www.openarchives.org/OAI/2.0/ http://www.openarchives.org/OAI/2.0/OAI-PMH.xsd"><responseDate>2026-07-11T07:22:49Z</responseDate><request verb="GetRecord" identifier="oai:riubu.ubu.es:10259/5081" metadataPrefix="dim">https://riubu.ubu.es/oai/request</request><GetRecord><record><header><identifier>oai:riubu.ubu.es:10259/5081</identifier><datestamp>2022-04-20T12:29:24Z</datestamp><setSpec>com_10259_4244</setSpec><setSpec>com_10259_5086</setSpec><setSpec>com_10259_2604</setSpec><setSpec>col_10259_4569</setSpec></header><metadata><dim:dim xmlns:dim="http://www.dspace.org/xmlns/dspace/dim" xmlns:doc="http://www.lyncode.com/xoai" xmlns:xsi="http://www.w3.org/2001/XMLSchema-instance" xsi:schemaLocation="http://www.dspace.org/xmlns/dspace/dim http://www.dspace.org/schema/dim.xsd">
<dim:field mdschema="dc" element="contributor" qualifier="author" authority="59" confidence="500" orcid_id="0000-0002-4418-0045">Benito Román, Oscar</dim:field>
<dim:field mdschema="dc" element="contributor" qualifier="author" authority="530" confidence="500" orcid_id="">Sanz Díez, Mª Teresa</dim:field>
<dim:field mdschema="dc" element="contributor" qualifier="author" authority="296" confidence="500" orcid_id="">Illera Gigante, Alba Ester</dim:field>
<dim:field mdschema="dc" element="contributor" qualifier="author" authority="357" confidence="500" orcid_id="">Melgosa Gómez, Rodrigo</dim:field>
<dim:field mdschema="dc" element="contributor" qualifier="author" authority="57" confidence="500" orcid_id="">Beltrán Calvo, Sagrario</dim:field>
<dim:field mdschema="dc" element="date" qualifier="accessioned">2019-03-20T12:46:10Z</dim:field>
<dim:field mdschema="dc" element="date" qualifier="available">2019-03-20T12:46:10Z</dim:field>
<dim:field mdschema="dc" element="date" qualifier="issued">2018</dim:field>
<dim:field mdschema="dc" element="identifier" qualifier="uri">http://hdl.handle.net/10259/5081</dim:field>
<dim:field mdschema="dc" element="description" lang="en">Trabajo presentado en: 6th International Congress on Green Process Engineering (GPE 2018), 3 a 6 de junio de 2018, Toulouse</dim:field>
<dim:field mdschema="dc" element="description" qualifier="abstract" lang="en">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.</dim:field>
<dim:field mdschema="dc" element="description" qualifier="sponsorship">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</dim:field>
<dim:field mdschema="dc" element="format" qualifier="mimetype">application/pdf</dim:field>
<dim:field mdschema="dc" element="language" qualifier="iso" lang="es">eng</dim:field>
<dim:field mdschema="dc" element="subject" lang="en">PPO</dim:field>
<dim:field mdschema="dc" element="subject" lang="en">PME</dim:field>
<dim:field mdschema="dc" element="subject" lang="en">juice</dim:field>
<dim:field mdschema="dc" element="subject" lang="en">Supercritical Carbon Dioxide</dim:field>
<dim:field mdschema="dc" element="subject" lang="en">green process</dim:field>
<dim:field mdschema="dc" element="subject" lang="en">food technology</dim:field>
<dim:field mdschema="dc" element="subject" qualifier="other" lang="es">Ingeniería química</dim:field>
<dim:field mdschema="dc" element="subject" qualifier="other" lang="en">Chemical engineering</dim:field>
<dim:field mdschema="dc" element="title" lang="en">Polyphenol Oxidase (PPO) and Pectin Meth ylesterase (PME) inactivation by means of High Pressure Carbon Dioxide (HPCD)</dim:field>
<dim:field mdschema="dc" element="type">info:eu-repo/semantics/conferenceObject</dim:field>
<dim:field mdschema="dc" element="rights" qualifier="accessRights">info:eu-repo/semantics/openAccess</dim:field>
</dim:dim></metadata></record></GetRecord></OAI-PMH>