A thin-walled tube with a diameter of 6 mm and length of 2 0 m is used to carry exhaust gas from a smoke stack to the laboratory in a nearby building for analysis. The gas enters the tube at 2 00 ° C and with a mass flow rate of 0.00 3 kg / s . Autumn winds at a temperature of 15 ° C blow directly across the tube at a velocity of 5 m / s . Assume the thermophysical properties of the exhaust gas are those of air. (a) Estimate the average heat transfer coefficient for the exhaust gas flowing inside the tube. (b) Estimate the heat transfer coefficient for the air flowing across the outside of the tube. (e) Estimate the overall heat transfer coefficient U and the temperature of the exhaust gas when it reaches the laboratory.
A thin-walled tube with a diameter of 6 mm and length of 2 0 m is used to carry exhaust gas from a smoke stack to the laboratory in a nearby building for analysis. The gas enters the tube at 2 00 ° C and with a mass flow rate of 0.00 3 kg / s . Autumn winds at a temperature of 15 ° C blow directly across the tube at a velocity of 5 m / s . Assume the thermophysical properties of the exhaust gas are those of air. (a) Estimate the average heat transfer coefficient for the exhaust gas flowing inside the tube. (b) Estimate the heat transfer coefficient for the air flowing across the outside of the tube. (e) Estimate the overall heat transfer coefficient U and the temperature of the exhaust gas when it reaches the laboratory.
Solution Summary: The author calculates the average heat transfer coefficient for exhaust gas flowing in the tube based on table A-4 "Thermo physical properties of air at atmospheric pressure".
A thin-walled tube with a diameter of 6 mm and length of
2
0
m
is used to carry exhaust gas from a smoke stack to the laboratory in a nearby building for analysis. The gas enters the tube at
2
00
°
C
and with a mass flow rate of
0.00
3 kg
/
s
. Autumn winds at a temperature of
15
°
C
blow directly across the tube at a velocity of
5 m
/
s
. Assume the thermophysical properties of the exhaust gas are those of air.
(a) Estimate the average heat transfer coefficient for the exhaust gas flowing inside the tube.
(b) Estimate the heat transfer coefficient for the air flowing across the outside of the tube.
(e) Estimate the overall heat transfer coefficient U and the temperature of the exhaust gas when it reaches the laboratory.
Liquid ammonia is transported from a production plant to a processing center via a 0.6-m diameter pipeline
at a mass flow rate of 0.15 kg/s. Surface temperature of the pipe is maintained 0°C by using a cooling jacket
with ice-cold water. Ammonia enters the pipeline at -17°C and exits at -3°C. Assume the flow is both
hydrodynamically and thermally fully developed in the pipe. What is the length of the pipe?
1857m
Air at a pressure of 1 atm. abs. and 50°C flows parallel to the top surface of a rectangular plate, 2
m x 9 m. Its temperature is maintained at 150°C. The air velocity is 8 m/s. If the critical Re no. is
106, determine the rate of heat transfer from the plate if the air flows parallel to
(i) the 2 m long side
(ii) the 9 m long side
Air at 0.8 atm enters at 18 C. Flows across bank of tubes 13 rows high and 7 rows deep at velocity of 9 m/s .The surfaces of tubes are maintained at 78 . The length of tubes is 1.2 m and the diameter of 1.5 cm .They are arranged in staggered manner so that the spacing in both the vertical and horizontal direction are 3cm and 2.25cm respectively. Calculate the total heat transfer and the exit air temperature.
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