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Many modeling challenges are excluded from this paper: Fluid-Structure Interactions (FSI) for the running paper web, coating of the paper web, the rheology of fluids and solids, heat transfer during the drying process, to mention a few.
Similar relationships are seen in the gas mass fraction n0 and solids heat capacity C s inputs.
Here, we find that the solids heat capacity C s, wind entrainment coefficient k w, heat capacity of dry air C a and no-wind entrainment coefficient k s (in descending order) have largest effect on the variation in model outputs.
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Due to contacting the hot air with the entrained particles, its temperature is dampened while the bed solids heat-up.
It also highlights that hot solids, heated to their maximum temperature, move into a coaxial inner cylinder and are transferred toward its outlet.
This large temperature peak is due to the occurrence of the exothermic reaction of SO2 with CuO in combination with efficient counter-current gas-solids heat exchange.
Solid heat capacity (kJ/kg K).
Solid heat capacity (j/mol k).
Within a solid, heat can be thought of as tiny quantum mechanical vibrations of atoms and molecules, known as "phonons".
The bed material is non-calcined olivine which acts as the solid heat carrier.
The SN2/HTS system design includes a second solid heat capacitor that cools a radiation shield.
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