2006
DOI: 10.1016/j.jfoodeng.2005.05.014
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Modelling coupled heat–water transfers during a decontamination treatment of the surface of solid food products by a jet of hot air. I. Sensitivity analysis of the model and first validations of product surface temperature under constant air temperature conditions

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Cited by 26 publications
(19 citation statements)
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“…Until now, engineers have used practical know-how and rules of thumb in chiller design and operation, with all the inherent risks of making mistakes (Mirade & Picgirard, 2006). Non uniform air distribution in blast refrigeration systems is one of the major factors that result in significant spatial temperature variability (Becker & Fricke, 2004;Dincer, 1994;Kondjoyan et al, 2006;Wooton, 1986). Lack of accounting for these variations may have serious effects on food quality and safety.…”
Section: Introductionmentioning
confidence: 99%
“…Until now, engineers have used practical know-how and rules of thumb in chiller design and operation, with all the inherent risks of making mistakes (Mirade & Picgirard, 2006). Non uniform air distribution in blast refrigeration systems is one of the major factors that result in significant spatial temperature variability (Becker & Fricke, 2004;Dincer, 1994;Kondjoyan et al, 2006;Wooton, 1986). Lack of accounting for these variations may have serious effects on food quality and safety.…”
Section: Introductionmentioning
confidence: 99%
“…A number of efforts have been made to describe the physical parameters and to model the processes, both for dry air (Kondjoyan, Mccann et al 2006a;Kondjoyan, Rouaud et al 2006b;Kondjoyan and Havet 2003;Valdramidis et al 2005) and steam (Kondjoyan and Portanguen 2008;Valdramidis et al 2008). The experimental data typically shows variations way beyond what can be explained by model parameters, thus indicating that the models may be incomplete with respect to parameters.…”
Section: Surface Pasteurisationmentioning
confidence: 99%
“…Thermal properties of the Teflon sample used during experiments were accurately known from a previous study: its thermal conductivity k=0.23 Wm −1 K −1 , a ¼ 1:23 Â 10 À7 m 2 :s À1 (Kondjoyan et al 2006). During the first period of treatment and during sample cooling, the upper boundary condition was determined by Neumann's condition and using Newton's law.…”
Section: Microbial Strain Preparationmentioning
confidence: 99%
“…On the upper surface of the sample h, the heat transfer coefficient, was equal to 760 Wm −2 K −1 (value for the mixed steam/air jet; Techasena and Flick 1995) and to 150 Wm −2 K −1 (Kondjoyan et al 2006) during the first steam condensation stage and the last cooling stage, respectively. The lower surface of the sample was stuck to the support.…”
Section: Microbial Strain Preparationmentioning
confidence: 99%