Consider the ground source heat pump of Problem 5.100 under winter conditions for which the liquid isdischarged from the heat pump into high-density polyethylene (using of thickness t = 8 mm and thermal conductivity k = 0.47 W/m ⋅ K . The tubing is muted through soil that maintains a uniform temperature of approximately 10°C at the tube outer surface. The properties of the fluid may be approximated as those of water. (a) For a tube inner diameter and flow rate of D i = 25 mm and m ˙ = 0.03 kg/s and a fluid inlet temperature of T m , i = 0 ° C , determine the tube outlet temperature (heat pump inlet temperature), T m , o , as a function of the tube length L for 10 ≤ L ≤ 50 m . (b) Recommend an appropriate length for the system. How would your recommendation be affected by variations in the liquid flow rate?
Consider the ground source heat pump of Problem 5.100 under winter conditions for which the liquid isdischarged from the heat pump into high-density polyethylene (using of thickness t = 8 mm and thermal conductivity k = 0.47 W/m ⋅ K . The tubing is muted through soil that maintains a uniform temperature of approximately 10°C at the tube outer surface. The properties of the fluid may be approximated as those of water. (a) For a tube inner diameter and flow rate of D i = 25 mm and m ˙ = 0.03 kg/s and a fluid inlet temperature of T m , i = 0 ° C , determine the tube outlet temperature (heat pump inlet temperature), T m , o , as a function of the tube length L for 10 ≤ L ≤ 50 m . (b) Recommend an appropriate length for the system. How would your recommendation be affected by variations in the liquid flow rate?
Solution Summary: The author explains the properties of fluid at temperature 277 K as a function of tube length.
Consider the ground source heat pump of Problem 5.100 under winter conditions for which the liquid isdischarged from the heat pump into high-density polyethylene (using of thickness
t
=
8
mm
and thermal conductivity
k
=
0.47
W/m
⋅
K
. The tubing is muted through soil that maintains a uniform temperature of approximately 10°C at the tube outer surface. The properties of the fluid may be approximated as those of water.
(a) For a tube inner diameter and flow rate of
D
i
=
25
mm
and
m
˙
=
0.03
kg/s
and a fluid inlet temperature of
T
m
,
i
=
0
°
C
, determine the tube outlet temperature (heat pump inlet temperature),
T
m
,
o
, as a function of the tube length L for
10
≤
L
≤
50
m
. (b) Recommend an appropriate length for the system. How would your recommendation be affected by variations in the liquid flow rate?
To cool the hot oil, an engineer has suggested that the oil be pumped through a pipe submerged in a nearby lake. The pipe (external diameter = 20 cm) will be placed in the horizontal direction. The temperature of the outer surface of the pipe averages 130 ° C. The surrounding water temperature is assumed to be constant at 10 ° C. Pipe length 100 m. If it is assumed that there is no water movement.
a. Determine the convective heat transfer coefficient of the outer pipe surface to the water. = Answer Watt / (m² ° C)
b. Determine the heat transfer rate from the pipe to the water. = Answer kW
To cool hot oil, an engineer has suggested that the oil be pumped through a pipe submerged in a nearby lake. The pipe (external diameter = 15 cm) will be placed in the horizontal direction. The temperature of the outer surface of the pipe averages 125 ° C. The surrounding water temperature is assumed to be constant at 15 ° C. Pipe length 100 m. If it is assumed that there is no water movement.
a. Determine the convective heat transfer coefficient of the outer pipe surface to the water. = ..... Watt / (m² ° C)
b. Determine the heat transfer rate from the pipe to the water. = ..... kW
Dry, compressed air at Tm,i
whose surface is at T; = 25°C. Determine the thermal entry length, in m, the mean temperature of the air at the tube outlet, in K, the
rate of heat transfer from the air to the tube wall, in W, and the power required to flow the air through the tube, in W. For these
conditions the fully developed heat transfer coefficient is h = 3.58 W/m2-K. Evaluate the properties of air at 320 K
75°C, p = 10 atm, with a mass flow rate of m = 0.003 kg/s, enters a 32-mm-diameter, 5-m-long tube
i
Tmo =
i
K
P =
i
q =
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