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The heating, holding and cooling section of the high temperature region (T>100°C) of coiled UHT-sterilisers were simulated three-dimensionally to assess the impact of centrifugal and buoyant forces on viscous power-law food products.
Moreover, since the strip temperature is measurable only at a few positions in water cooling section due to the difficult ambient conditions, an Extended Kalman Filter (EKF) is used to estimate the transient temperature of strip.
The NCL with a lower aspect ratio (ratio of vertical center distance between the heating and cooling section to the horizontal length of loop) is supposed to be more stable.
The hot aqueous stream coming out from the reactor was fast cooled to 40 °C in a tubular heat exchanger located soon after the reactor vessel (cooling section in Fig. 4).
Some extra water containers in the cooling section will also minimize the amount of inrushing warm air that has to be cooled when the door opens and shuts.
Check for the recommended temperatures, 37 to 40 degrees Fahrenheit in the cooling section and under 5 degrees Fahrenheit in the freezer compartment.
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This hybrid LD-HP system contained dehumidifying and cooling sections.
The reactor consisted of three tubular reactor sections with cooling sections in between.
For maximum carbon dioxide conversion, it is convenient to split the methanation into several stages adding cooling sections in between.
The lengths of heating, holding and cooling sections were found to be 2.28, 1.0 and 2.08 m, respectively.
The model takes into account the contribution from heating and cooling sections, the heat exchange with the ambient air and effective diffusion associated with non-ideal laminar flow.
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