2006
DOI: 10.1205/fbp06027
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Effect of Preheating on Fouling of a Pilot Scale UHT Sterilizing Plant by Recombined, Reconstituted and Fresh Whole Milks

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Cited by 14 publications
(6 citation statements)
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“…Indirect ESL treatment resulted in a large increase in viscosity, from 3.42 to 9.02 mPa s, compared with both direct heat treatments and to the indirect UHT treatment, despite the higher final heating temperature. This may be due to the effect of preheating temperature, which has been shown to impact the heat stability of protein dispersions, stabilising against heat-induced physical changes during high temperature processing (Drapala, Auty, Mulvihill, & O'Mahony, 2016;Dumpler & Kulozik, 2016;Srichantra, Newstead, McCarthy, & Paterson, 2006). In this study, no such effect was seen when direct heat treatment was applied, suggesting that preheat treatment may have a less significant effect during direct heating compared with indirect.…”
Section: Discussionmentioning
confidence: 62%
“…Indirect ESL treatment resulted in a large increase in viscosity, from 3.42 to 9.02 mPa s, compared with both direct heat treatments and to the indirect UHT treatment, despite the higher final heating temperature. This may be due to the effect of preheating temperature, which has been shown to impact the heat stability of protein dispersions, stabilising against heat-induced physical changes during high temperature processing (Drapala, Auty, Mulvihill, & O'Mahony, 2016;Dumpler & Kulozik, 2016;Srichantra, Newstead, McCarthy, & Paterson, 2006). In this study, no such effect was seen when direct heat treatment was applied, suggesting that preheat treatment may have a less significant effect during direct heating compared with indirect.…”
Section: Discussionmentioning
confidence: 62%
“…In this present study, CIP was done immediately when fouling rate reach 0.8 o C/h. Srichantra et al [7] reported that CIP was done to ensure the cleanliness of plate heat exchanger.…”
Section: Resultsmentioning
confidence: 99%
“…The hot water inlet temperature and the milk outlet temperature in heat exchanger (Alva Laval, Lund, Sweden) of pasteurization process were recorded. This was calculated by using formula of Srichantra et al [7] as below:…”
Section: Methodsmentioning
confidence: 99%
“…Estos esquemas de reacciones cinéticas pueden ser llevadas a ecuaciones diferenciales reuniendo todos los parámetros cinéticos necesarios para el modelo de reacción de despliegue y agregación [49].…”
Section: ) Modelos De Ensuciamiento Combinadosunclassified