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The mean heat exchange coefficient between heating cell and evaporating film was around 1100 W.m−2.K−1.
The aim of this study was to develop a mathematical model of a solid food material undergoing heating in a cylindrical batch ohmic heating cell.
The heating cell has a single communication orifice; Equation 27 could be written in the following form: δ Q c + δ W c + C p T rc d m c = C v ⋅ d mT c. (31).
As for the heating cell, we obtain also d m f = V f T f dp r + P T f d V f r = 1 r T f V f dp + Pd V f. (38).
A strategy has been proposed and evaluated recently towards this purpose in which a heating cell with accurate temperature control is synchronized with the split Hopkinson pressure bar (SHPB) system.
While in most systems without the heating cell being synchronized with the SHPB system, the typical CCT is about 500 ms, and therefore the experimental data cannot be taken as representing the material behavior.
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Hyperthermia, heating cells to higher than normal temperature, has been used in a limited way for many years.
It induces a thermal destruction of tissues by heating cells to >60°C obtaining a non-reversible cellular modification, called "coagulative necrosis" [12].
During a crankshaft rotation, the heat exchanged in the cooling and heating cells are Q c = ∮ δQ c and Q f = ∮ δQ f obtained by integration of Equations 36 and 39.
They apply the heat as close to the brood as possible: workers heating cells from within have a higher probability of endothermy than those on the comb surface.
Necrotic cells (NC) were prepared by heating cells for 20 minutes to 65°C.
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