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The heat transfer density was higher for more shear thinning fluids.
Compared to state-of-the-art dry cooling, nearly 27% improvement in gravimetric heat transfer density was noted at air-side coefficient of performance (COPair) of 172.
Compared to wavy fin and plain plate fin heat exchangers, up to 30% and 40% improvement, respectively, in gravimetric heat transfer density was recorded for the entire range of experimental data.
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This trend, and the method of optimizing flow architecture to achieve maximal heat transfer density, are essential in the continuing miniaturization of heat transfer devices.
The heat transfer density is further increased by progressively inserting another set of even shorter plates between the plates and then optimizing the whole structure.
The transfer current density is described by the Butler Volmer equation.
The dye-regeneration efficiency evaluated from a minimum electron density and a transferred counterpart ionic carrier density was approximately ranged between 1.5 and 3.0%.
Analogous approach was applied to MO distribution on Ph groups but, in addition, MO coefficients related with the phenyl ring (i.e. six carbon atoms, while no density was transferred to hydrogen in any case) were summed.
Larval density was controlled by transfer of approximately 75 eggs to each vial used to produce the next generation.
This paper shows that in a space filled with heat generating parallel plates and laminar forced convection, the heat transfer density can be increased beyond the level known for parallel plates with optimal spacing.
This paper shows that in a space filled with assemblies of cylinders cooled by natural convection the heat transfer density can be increased progressively by the use of cylinders of several sizes, and the optimal placement of each cylinder in the assembly.
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