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?
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Two large tanks, each holding 100 L of liquid, are interconnected by pipes, with the liquid flowing from tank
A into tank B at a rate of 3 L/min and from B into A at a rate of 1 L/min (see Figure Q1). The liquid inside each
tank is kept well stirred. A brine solution with a concentration of 0.2 kg/L of salt flows into tank A at a rate of
6 L/min. The diluted solution flows out of the system from tank A at 4 L/min and from tank B at 2 L/min. If,
initially, tank A contains pure water and tank B contains 20 kg of salt.
A
6 L/min
0.2 kg/L
x(t)
100 L
4 L/min
x(0) = 0 kg
3 L/min
B
y(t)
100 L
y(0) = 20 kg
2 L/min
1 L/min
Figure Q1 - Mixing problem for interconnected tanks
Determine the mass of salt in each tank at time t > 0:
Analytically (hand calculations)
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