Heated air required for a food-drying process is generated by passing ambient air at 2 0 ° C through long, circular tubes ( D = 50 m m , L = 5 m ) housed in a steam condenser. Saturated steam at atmospheric pressure condenses on the outer surface of the tubes, maintaining a uniform surface temperature of 1 00 ° C . (a) 1f an airflow rate of 0.01 k g / s is maintained in each tube, determine the air outlet temperature T m , o , and the total heat rate q for the tube. (b) The air outlet temperature may be controlled by adjusting the tube mass flow rate. Compute and plot T m , o , as a function of m ˙ for 0.005 ≤ m ˙ ≤ 0.050 k g / s . If a particular drying process requires approximately 1 k g of air at 75 ° C , what design and operating conditions should be prescribed for the air heater, subject to the constraint that the tube diameter and length be fixed at 5 0 mm and 5 m , respectively?
Heated air required for a food-drying process is generated by passing ambient air at 2 0 ° C through long, circular tubes ( D = 50 m m , L = 5 m ) housed in a steam condenser. Saturated steam at atmospheric pressure condenses on the outer surface of the tubes, maintaining a uniform surface temperature of 1 00 ° C . (a) 1f an airflow rate of 0.01 k g / s is maintained in each tube, determine the air outlet temperature T m , o , and the total heat rate q for the tube. (b) The air outlet temperature may be controlled by adjusting the tube mass flow rate. Compute and plot T m , o , as a function of m ˙ for 0.005 ≤ m ˙ ≤ 0.050 k g / s . If a particular drying process requires approximately 1 k g of air at 75 ° C , what design and operating conditions should be prescribed for the air heater, subject to the constraint that the tube diameter and length be fixed at 5 0 mm and 5 m , respectively?
Solution Summary: The author explains the outlet temperature, pressure and rate of heat transfer. The Reynolds number for the type of flow is calculated as follows:
Heated air required for a food-drying process is generated by passing ambient air at
2
0
°
C
through long, circular tubes
(
D
=
50
m
m
,
L
=
5
m
)
housed in a steam condenser. Saturated steam at atmospheric pressure condenses on the outer surface of the tubes, maintaining a uniform surface temperature of
1
00
°
C
. (a) 1f an airflow rate of
0.01
k
g
/
s
is maintained in each tube, determine the air outlet temperature
T
m
,
o
, and the total heat rate q for the tube. (b) The air outlet temperature may be controlled by adjusting the tube mass flow rate. Compute and plot
T
m
,
o
, as a function of
m
˙
for
0.005
≤
m
˙
≤
0.050
k
g
/
s
. If a particular drying process requires approximately
1
k
g
of air at
75
°
C
, what design and operating conditions should be prescribed for the air heater, subject to the constraint that the tube diameter and length be fixed at
5
0
mm
and
5 m
, respectively?
A condenser consists of several tubes. The outer diameter of each tube is 2 cm,
and the thickness is 2 mm. It is designed to condense saturated steam that
enters the condenser at the mass flow rate of 100 kg/s. The steam pressure is
10 kPa. There is 10% moisture in saturated steam. The inlet temperature of
cooling water is 20°C, and the outlet temperature is 40°C. Water velocity 2
m/s. The overall heat transfer coefficient based on outer surface area is 3.5
3.
kW/m2.K. The heat capacity of water is 4.2 kJ/kg.K. Water density is 1000
kg/m'. Find the number of tubes and the length of each tube.
Q 2- The Nusselt number for flow in a tube is given by
Nu = C₁ Rea Prb
where the constants, C1, a, and b are 0.023, 0.8, and 0.3, respectively. Estimate a mass-transfer
coefficient for moist air flowing in a 30 cm tube with a diameter of 10 cm at the rate of 0.3 m3/s.
Assume standard air, Prandtl number is 0.7 and unity Lewis number.
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