Exhaust gases from a wire processing oven are discharged into a tall stack, and the gas and stack surface temperatures at the outlet of the stack must be estimated. Knowledge of the outlet gas temperature T m , o is useful for predicting the dispersion of effluents in the thermal plume, while knowledge of the outlet stack surface temperature T, indicates whether condensation of the gasproducts will occur. The thin-walled, cylindrical stack is0.5 in in diameter and 6.0 in high. The exhaust gas flowrate is 0.5 kg/s. and (he inlet temperature is 600°C. (a) Consider conditions for which the ambient air temperature and wind velocity are 4°C and 5 m/s.respectively. Approximating the thermophysicalproperties of the gas as those of atmospheric air,estimate the outlet gas and stack surface temperatures for the given conditions. (b) The gas outlet temperature is sensitive to variationsin the ambient air temperature and wind velocity.For T ∞ = − 25 °C. 5°C, and 35°C, compute and plotthe gas outlet temperature as a function of windvelocity for 2 ≤ V ≤ 10 m/s.
Exhaust gases from a wire processing oven are discharged into a tall stack, and the gas and stack surface temperatures at the outlet of the stack must be estimated. Knowledge of the outlet gas temperature T m , o is useful for predicting the dispersion of effluents in the thermal plume, while knowledge of the outlet stack surface temperature T, indicates whether condensation of the gasproducts will occur. The thin-walled, cylindrical stack is0.5 in in diameter and 6.0 in high. The exhaust gas flowrate is 0.5 kg/s. and (he inlet temperature is 600°C. (a) Consider conditions for which the ambient air temperature and wind velocity are 4°C and 5 m/s.respectively. Approximating the thermophysicalproperties of the gas as those of atmospheric air,estimate the outlet gas and stack surface temperatures for the given conditions. (b) The gas outlet temperature is sensitive to variationsin the ambient air temperature and wind velocity.For T ∞ = − 25 °C. 5°C, and 35°C, compute and plotthe gas outlet temperature as a function of windvelocity for 2 ≤ V ≤ 10 m/s.
Solution Summary: The author explains the outlet gas temperature and stack temperature. The mass flow rate is stackreldotm=0.5kg/s.
Exhaust gases from a wire processing oven are discharged into a tall stack, and the gas and stack surface temperatures at the outlet of the stack must be estimated. Knowledge of the outlet gas temperature
T
m
,
o
is useful for predicting the dispersion of effluents in the thermal plume, while knowledge of the outlet stack surface temperature T, indicates whether condensation of the gasproducts will occur. The thin-walled, cylindrical stack is0.5 in in diameter and 6.0 in high. The exhaust gas flowrate is 0.5 kg/s. and (he inlet temperature is 600°C.
(a) Consider conditions for which the ambient air temperature and wind velocity are 4°C and 5 m/s.respectively. Approximating the thermophysicalproperties of the gas as those of atmospheric air,estimate the outlet gas and stack surface temperatures for the given conditions. (b) The gas outlet temperature is sensitive to variationsin the ambient air temperature and wind velocity.For
T
∞
=
−
25
°C. 5°C, and 35°C, compute and plotthe gas outlet temperature as a function of windvelocity for
2
≤
V
≤
10
m/s.
.All properties should be evaluated at the temperature of the steam.Saturated, pure steam at 65 ºC condenses on the surface of a vertical tube with outersurface diameter 2 cm which is maintained at a uniform temperature of 35 ºC. Determinethe tube length for a condensate flow rate of 5 x 10-3 kg/s.
Saturated, pure steam at a temperature of 170 oC condenses on the outer surface of a vertical tube of outer diameter 2 cm and length 1.5 m. The tube surface is maintained at a uniform temperature of 150 oC.
Calculate:
the local film condensation heat-transfer coefficient at the bottom of the tube.
the average condensation heat-transfer coefficient over the entire length of the tube.
the total condensation rate at the tube surface.
It takes 0.035 W to diffuse water through a
temperature 290 K. The tube is 10 m in length and has a 1.5 cm ID. Assume that the total pressure is 0.1
MPa and all condensate remains inside the pipe. Neglect the effects of conduction and radiation. Calculate
the rate of evaporation.
m/s flowing dry air at 300 K along a cylindrical tube of
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