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This paper presents ice slurry melting experiments with a tube-in-tube heat transfer coil.
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Relative location, and therefore the coupling coefficient M, of the two power transfer coils (external and implanted) is defined by horizontal (d x ), vertical (d y ), and angular misalignments.
This experimental data provides a basis for designing a larger-scale sparging hydrolysis reactor for the calcium bromide thermochemical cycle where the endothermic heat of reaction can be effectively supplied by heat transfer coils embedded in the melt.
Through numerical computation, a coupling temperature distribution in the adsorbent and the heat-transfer coil is obtained.
Based on discretized energy control equations of the fluid in the heat-transfer coil and transient heat conduction equations of the adsorbent in the bed with unsteady boundary conditions, a numerical analysis is made.
The secondary objective is to compare the efficiency of heat transfer in spiral coils to vertical tube baffles.
In addition, for better mixing and heat transfer, electromagnetic coils or permeable refractory blocks for gas stirring are often installed in furnace bottoms.
Inductive-coupling-based power transfer requires two coils (primary and secondary coils), and the efficiency of power transfer between the coils is a strong function of the coil dimensions and distance between them.
A physical empirical model is designed to describe heat transfer of helical coil in oil and glycerol/water solution.
Implanted, a coil transfers power across the skin and recharges the device from the outside.
When it is implanted, a coil transfers power across the skin and recharges the device from the outside.
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