“…For the geometry given in Table 1, natural convection is not present. As noted in the introduction, previous work has been used to derive U [24,25]. The more elegant of these results will be used, namely that the overall heat transfer coefficient, U, can be found from the device geometry (A t , A w , h s ), thermophysical properties (k s ), convective coefficient, h, and the melt fraction, x e , which is a function of position in the device as well as time:…”