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A feedback method was utilized to generate a time-dependent heat flux by controlling the output power of radiative heater.
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The objective is to determine the powers and locations of the heaters to attain prescribed uniform temperature and radiative heat flux on the design surface.
A conveyorised drying system having three chambers was fitted with mid-infrared (MIR) heaters for radiative heating.
Model results indicated that heaters alter radiative, turbulent and mass fluxes by amounts comparable to the differences between CO and NM fluxes.
An inverse analysis is employed to control the time rate of heaters in a 2-D smelting furnace to provide the specified radiative heat flux across the design surface to establish a desired melting rate.
The temperature of the Ge lens is monitored via telemetry and kept thermally stable by a heater to prevent radiative coupling.
As a result, radiative heat transport is less effective.
The combustion is trigged by a 3 kW electric heater as an external thermal radiative source, and then the surface temperature, combustion behavior, heat release rate, flame temperature and mass loss rate are obtained.
In this study, uniform temperature and heat flux are prescribed in one of the surfaces of a radiative system, while the shape and position of filament heaters are left to be found.
The operation at liquid helium temperature reduces non-equivalence errors between electrical and radiative heating by increasing the receiver's thermal conductivity and eliminating heater lead losses through the use of a superconducting wire [2, 3].
The solution contains three sub-models: (i) regularized inversion of the cause effect matrix with the target cabin air temperatures as the known input, which solves the convective heat rates of the underfloor heaters and the air-supply temperature, (ii) solution of underfloor heater's surface temperatures based on Newton's law of cooling, and (iii) computation of the radiative heat rates.
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CEO of Professional Science Editing for Scientists @ prosciediting.com