Please use this identifier to cite or link to this item: https://open.uns.ac.rs/handle/123456789/7468
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dc.contributor.authorPetković, Milicaen
dc.contributor.authorŠereš, Zitaen
dc.contributor.authorPajin, Biljanaen
dc.contributor.authorBanjac, Vojislaven
dc.date.accessioned2019-09-30T09:02:12Z-
dc.date.available2019-09-30T09:02:12Z-
dc.date.issued2014-01-01en
dc.identifier.issn13886150en
dc.identifier.urihttps://open.uns.ac.rs/handle/123456789/7468-
dc.description.abstractThe purpose of this study is to research the thermal properties of spreads with maltitol. Thermal characteristics of spreads depend on process parameters (temperature, mixer speed rotation). Spreads are produced at different temperatures (30, 35, and 40 °C) and mixer speed rotation (1, 1.33, and 1.67 Hz). The thermogravimetric method shows the peak position and determinate the spread composition. The temperature decomposition of sucrose and maltitol is two stages (two peaks), and palm fat has a single stage decomposition (one peak). Maltitol peak is dominant for spreads containing 100 and 70 % maltitol as a sweetener. This peak is sharper than sucrose peak and the inflection point is more expressed. Shape and the position of these peaks in spreads are modified. Peaks of maltitol, palm fat, and sucrose in spreads are lower and wider because of the grinding process and the interaction between spread ingredients. Increasing the process parameters (temperature, mixer speed rotation), temperatures of these peaks are higher (closer to temperature peak of pure ingredients). The dominant parameter is mixer speed rotation. The most thermally stable spreads with any amount of maltitol are produced at a temperature of 40 °C and high mixer speed rotation (1.33 and 1.67 Hz), while the least stable maltitol spreads are produced at minimum process parameters (30 °C, 1 Hz). © 2014 Akadémiai Kiadó, Budapest, Hungary.en
dc.relation.ispartofJournal of Thermal Analysis and Calorimetryen
dc.titleThermal decomposition of maltitol spreadsen
dc.typeJournal/Magazine Articleen
dc.identifier.doi10.1007/s10973-014-3659-9en
dc.identifier.scopus2-s2.0-84904470223en
dc.identifier.urlhttps://api.elsevier.com/content/abstract/scopus_id/84904470223en
dc.relation.lastpage284en
dc.relation.firstpage277en
dc.relation.issue1en
dc.relation.volume117en
item.grantfulltextnone-
item.fulltextNo Fulltext-
crisitem.author.deptFakultet tehničkih nauka, Departman za energetiku, elektroniku i telekomunikacije-
crisitem.author.deptTehnološki fakultet, Katedra za inženjerstvo ugljenohidratne hrane-
crisitem.author.deptTehnološki fakultet, Katedra za inženjerstvo ugljenohidratne hrane-
crisitem.author.deptNaučni institut za prehrambene tehnologije u Novom Sadu-
crisitem.author.orcid0000-0001-8384-7562-
crisitem.author.orcid0000-0002-4552-7880-
crisitem.author.parentorgFakultet tehničkih nauka-
crisitem.author.parentorgTehnološki fakultet-
crisitem.author.parentorgTehnološki fakultet-
crisitem.author.parentorgUniverzitet u Novom Sadu-
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