The fire tube of a hot water heater consists of a long circular duct of diameter D = 0.07 m and temperature T s = 385 K , through which combustion gases flow at a temperature of T m , g = 900 K . To enhance heat transfer from the gas to the tube, a thin partition is inserted along the midplane of the tube. The gases may be assumed to have the thermophysical properties of air and to be radiatively nonparticipating. (a) With no partition and a gas flow rate of m ˙ g =0 .50 kg/s , what is the rate of heat transfer per unit length, q’ , to the tube? (b) For a gas flow rate of m ˙ g =0 .05 kg/s and emissivities of ε s = ε p = 0.5 , determine the partition temperature T p and the total rate of heat transfer q’ to the tube. (c) For m ˙ g =0 .02, 0 .05 , and 0 .08 kg/s and equivalent emissivities ε p = ε s ≡ ε compute and plot T p and q’ as a function of ε for 0.1 ≤ ε ≤ 1.0 . For m ˙ g =0 .05 kg/s and equivalent emissivities, plot the convective and radiative contributions to q’ as a function of ε .
The fire tube of a hot water heater consists of a long circular duct of diameter D = 0.07 m and temperature T s = 385 K , through which combustion gases flow at a temperature of T m , g = 900 K . To enhance heat transfer from the gas to the tube, a thin partition is inserted along the midplane of the tube. The gases may be assumed to have the thermophysical properties of air and to be radiatively nonparticipating. (a) With no partition and a gas flow rate of m ˙ g =0 .50 kg/s , what is the rate of heat transfer per unit length, q’ , to the tube? (b) For a gas flow rate of m ˙ g =0 .05 kg/s and emissivities of ε s = ε p = 0.5 , determine the partition temperature T p and the total rate of heat transfer q’ to the tube. (c) For m ˙ g =0 .02, 0 .05 , and 0 .08 kg/s and equivalent emissivities ε p = ε s ≡ ε compute and plot T p and q’ as a function of ε for 0.1 ≤ ε ≤ 1.0 . For m ˙ g =0 .05 kg/s and equivalent emissivities, plot the convective and radiative contributions to q’ as a function of ε .
Solution Summary: The author explains that heat transfer to the tube wall occurs only by convection when there is no partition.
The fire tube of a hot water heater consists of a long circular duct of diameter
D
=
0.07
m
and temperature
T
s
=
385
K
, through which combustion gases flow at a temperature of
T
m
,
g
=
900
K
. To enhance heat transfer from the gas to the tube, a thin partition is inserted along the midplane of the tube. The gases may be assumed to have the thermophysical properties of air and to be radiatively nonparticipating.
(a) With no partition and a gas flow rate of
m
˙
g
=0
.50
kg/s
, what is the rate of heat transfer per unit length, q’, to the tube? (b) For a gas flow rate of
m
˙
g
=0
.05
kg/s
and emissivities of
ε
s
=
ε
p
=
0.5
, determine the partition temperature Tpand the total rate of heat transfer q’ to the tube. (c) For
m
˙
g
=0
.02, 0
.05
, and
0
.08
kg/s
and equivalent emissivities
ε
p
=
ε
s
≡
ε
compute and plot Tpand q’ as a function of
ε
for
0.1
≤
ε
≤
1.0
. For
m
˙
g
=0
.05
kg/s
and equivalent emissivities, plot the convective and radiative contributions to q’ as a function of
ε
.
The extremely high temperatures needed to trigger nuclear fusion are proposed to be generated by laser irradiating a spherical pellet
of deuterium and tritium fuel of diameter Dp = 1.8 mm.
(a) Determine the maximum fuel temperature that can be achieved by irradiating the pellet with 200 lasers, each producing a power of
P = 500 W. The pellet has an absorptivity a = 0.3 and emissivity & = 0.8.
(b) The pellet is placed inside a cylindrical enclosure. Two laser entrance holes are located at either end of the enclosure and have a
diameter of DLEH = 2.0 mm. Determine the maximum temperature that can be generated within the enclosure.
N
(a)
K
Dp
Determine the maximum fuel temperature that can be achieved in part (a), in K.
Tmax = i
K
DLEH
N
#K
Determine the maximum fuel temperature that can be achieved in part (b), in K.
Tmax
i
Physical Properties Mathematical Functions
(b)
Need correctly, I am posting this question again.
Keep in mind that both the bottom and top surfaces of the workpiece are exposed to radiation and convection. The workpiece is suspended in air in the furnace.
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