ABSTRACT
Thermal characteristics of water in a ground U-tube with twisted tape inserts were addressed. At inlet temperatures of 60°C to 75°C, and Reynolds numbers of 3000 to 9000, the surface heat transfer coefficients for water with twisted tapes ranged from 442 to 897 W m−2 K−1, which were higher than that in smooth tube, 384–810 W m−2 K−1. Average convective heat transfer coefficient for the smooth tube in sand/graphite blend ameliorated by 36% compared to that in sand. Average apparent thermal diffusivities of sand/graphite at hot end temperature of 70°C rose by about 17% compared to sand.
Nomenclature
A | = | heat transfer surface area (m2) |
c | = | specific heat capacity (J kg−1 K−1) |
d | = | diameter (m) |
f | = | friction factor |
h | = | heat transfer coefficient (W m−2 K−1) |
l | = | length (m) |
Nu | = | Nusselt number |
Pr | = | Prandtl number |
p | = | pressure drop (Pa) |
qv | = | volumetric flow rate (m3 s−1) |
Q | = | heat flow rate (W) |
Re | = | Reynolds number |
t | = | time (s) |
T | = | temperature (°C) |
Greek letters
U | = | flow velocity (m s−1) |
λ | = | thermal conductivity (W m−1 K−1) |
ν | = | kinematic viscosity (m2 s−1) |
ρ | = | density (kg m−3) |
ω | = | water content |
Subscripts and Superscripts
h | = | hot end |
i | = | inner/initial |
in | = | inlet |
l | = | liquid |
o | = | outer |
out | = | outlet |
w | = | wall |
Supplementary material
Supplemental data for this article can be accessed publisher’s website.