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<dc:title>Extracción con agua subcrítica y ultrafiltración para la obtención de pecto-oligosacáridos a partir de residuos de piel cebolla</dc:title>
<dc:creator>Hernández Manchado, Javier</dc:creator>
<dc:contributor>Ruiz Pérez, María Olga</dc:contributor>
<dc:contributor>Benito Román, Oscar</dc:contributor>
<dc:contributor>Universidad de Burgos. Departamento de Química</dc:contributor>
<dc:subject>Subcritical water</dc:subject>
<dc:subject>Oligosaccharide fractionation</dc:subject>
<dc:subject>Ultrafiltration</dc:subject>
<dc:subject>Diafiltration</dc:subject>
<dc:subject>Onion skin waste</dc:subject>
<dc:subject>Biorefinery</dc:subject>
<dc:description>In this work the purification by ultrafiltration using tubular ceramic membranes of pectic&#xd;
oligosaccharides (POS) extracted from onion skin wastes (OSW) was studied.&#xd;
In the first stage of the work, subcritical water was used to promote the hydrolysis of OSW and&#xd;
obtain a liquid hydrolysate rich in POS. For this purpose, three different combinations of&#xd;
temperature and extraction time (115 ºC – 180 min; 125 ºC – 150 min and 135 ºC – 90 min)&#xd;
were used in a batch extractor at 25 bar. In order to consider the combined effect of the&#xd;
temperature and the extraction time, the severity factor (log Ro) was calculated, resulting to be&#xd;
in the range 2.88 to 3.29. The best results in terms of POS concentration (5643 ± 84 mg/L) in&#xd;
the hydrolysate was obtained in the experiment carried out at 125 ºC (log Ro = 3.16). It was&#xd;
also possible to demonstrate that the composition of the liquid hydrolysate was strongly&#xd;
influenced by the extraction conditions: the higher the severity factor the higher the&#xd;
concentration of impurities (organic acids, HMF and furfural) and higher the POS hydrolysis&#xd;
rate. This was demonstrated by the increased concentration of free monosaccharides&#xd;
(glucose, xylose, galactose and arabinose) and the decrease in the POS molecular weight.&#xd;
In the second stage of the work, the aim was to study the separation of POS from the impurities&#xd;
formed during the subcritical water hydrolysis stage, using an ultrafiltration process in&#xd;
diafiltration mode. For this purpose, a 50 kDa tubular membrane was firstly used (Tami&#xd;
Industries, active layer of TiO2 and 132 cm2 of effective area). The fouling mechanism,&#xd;
hydraulic resistance and the purification extent were studied. Important differences in the&#xd;
permeate flux (J) were observed as a function of the subcritical water hydrolysate composition.&#xd;
The permeate flux obtained when filtering the 115 ºC hydrolysate decreased dramatically at&#xd;
the beginning of the experiment to achieve a constant value, whereas the hydrolysates&#xd;
obtained at 125 and 135 ºC exhibited a different behaviour: an initial fast decline of the&#xd;
permeate flux followed by a slower continuous decrease. This result for 125 and 135 ºC&#xd;
hydrolysates can be justified due to the effects of the membrane fouling (fouling mechanism&#xd;
was cake layer formation, according to Hermia’s model). Using this 50 kDa membrane, the&#xd;
POS recovery was 76 % (115 ºC hydrolysate), 58 % for the 125 ºC hydrolysate and 56% for&#xd;
the 135 ºC hydrolysate. In all the cases, a complete removal of the impurities was achieved&#xd;
after the dilution factor of 3.5.&#xd;
To complete the purification experiments, the effect of the removal of the colloidal matter (by&#xd;
centrifugation) present in the 125 ºC hydrolysate was studied using two different membranes&#xd;
(50 and 5 kDa). In the hydrolysate, it was observed the formation of a black precipitate that&#xd;
was responsible for the membrane fouling, hindering the filtration process. The removal of this&#xd;
colloidal matter, which did not affect the POS fraction, was responsible for the reduction of the&#xd;
colour of the hydrolysate by 60 % and the promotion of the filtration process (a faster removal&#xd;
of the impurities was achieved) without loss of the POS fraction. Finally, when a 5 kDa&#xd;
membrane was used, the retention of the POS fraction was higher than 80 % in comparison&#xd;
to the 60 % obtained for the 50 kDa membrane.</dc:description>
<dc:date>2024-05-06T12:15:05Z</dc:date>
<dc:date>2024-05-06T12:15:05Z</dc:date>
<dc:date>2023-06</dc:date>
<dc:type>info:eu-repo/semantics/bachelorThesis</dc:type>
<dc:identifier>http://hdl.handle.net/10259/9132</dc:identifier>
<dc:language>spa</dc:language>
<dc:rights>http://creativecommons.org/licenses/by-nc-nd/4.0/</dc:rights>
<dc:rights>Este documento está sujeto a una licencia de uso Creative Commons, por la cual está permitido hacer copia, distribuir y comunicar públicamente la obra siempre que se cite al autor original y no se haga de él uso comercial ni obra derivada</dc:rights>
<dc:rights>info:eu-repo/semantics/openAccess</dc:rights>
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