Abstract
The author proposes a method of comparing the heat transfer coefficients in two channels in which
(1) the cross-sectional shape is different;
(2) there are different proportions of rough and smooth surfaces;
(3) there are different proportions of heated and unheated surfaces.
In particular the method applies to experimental results for the system in which a roughened, heated cylinder is placed centrally in a smooth unheated pipe. The effective diameter concept is used to allow for changes in shape, and the heat-transfer boundary conditions are modified to make them similar to the fluid-flow boundary conditions before the comparison is made.
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