Как выбрать гостиницу для кошек
14 декабря, 2021
DTf • T + T J. 1^*0 ) |
m |
dt |
2 |
(eq.13) |
The differential equation governing the heat transfer into the fluid during the discharging process is given by equation 13.
Time (s) Fig.6: Comparison between experience (interface absorber/polymer (o) and outlet (□) temperatures) and simulation (interface absorber/polymer (—) and outlet (—) temperatures) in discharging process |
This expression links the outlet temperature to the absorber temperature via a heat transfer coefficient hf-a calculated previously during preliminary absorber efficiency test (hf-a=70 W. m-2.K-1). Entering the experimental conditions (mass flow of 40L. h-1 and inlet temperature of 298 K) we obtain the profile temperatures plotted in figure 6.
G |
Solar global irradiation (W. m-2) |
h |
Heat transfer coefficient (W. m-2.K-1) |
m |
Mass flow (kg. s-1) |
m |
Mass (kg) |
T |
Temperature (K) |
||
Greek symbols |
|||
a |
Absorbance |
T |
Transmittance |
X |
Thermal conductivity (W. m-1.K-1) |
є |
Emissivity |
n |
Efficiency |
p |
Reflectivity |
Subscript |
|||
amb |
Ambiant |
c |
Composite |
e |
End |
f |
Fusion, Fluid |
i |
Inlet |
in |
Initial |
l |
Liquid |
o |
Outlet |
s |
Solid |
sky |
Sky |
Saunier Duval industry part of Vaillant Group and the French Government (trough the ANRT) are
acknowledged for financial support.
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