An air heater for an industrial application consists of an insulated, concentric tube annulus, for which air flows through a thin-walled inner tube. Saturated steam flows through the outer annulus, and condensation of the steam maintains a uniform temperature T s on the tube surface. Consider conditions for which air enters a 50-mm-diameter tube at a pressure of 5 atm, a temperature of T m , i = 17 ° C , and a flow rate of m ˙ = 0.03 kg/s , while saturated steam at 2.455 bars condenses on the outersurface of the tube. If the length of the annulus is L = 5 m , what are the outlet temperature T m , o , and pressure p o of the air? What is the mass rate at which condensate leaves the annulus?
An air heater for an industrial application consists of an insulated, concentric tube annulus, for which air flows through a thin-walled inner tube. Saturated steam flows through the outer annulus, and condensation of the steam maintains a uniform temperature T s on the tube surface. Consider conditions for which air enters a 50-mm-diameter tube at a pressure of 5 atm, a temperature of T m , i = 17 ° C , and a flow rate of m ˙ = 0.03 kg/s , while saturated steam at 2.455 bars condenses on the outersurface of the tube. If the length of the annulus is L = 5 m , what are the outlet temperature T m , o , and pressure p o of the air? What is the mass rate at which condensate leaves the annulus?
Solution Summary: The author explains the outlet temperature and pressure drop of the air and mass rate at which the condensate leaves the annulus.
An air heater for an industrial application consists of an insulated, concentric tube annulus, for which air flows through a thin-walled inner tube. Saturated steam flows through the outer annulus, and condensation of the steam maintains a uniform temperature
T
s
on the tube surface.
Consider conditions for which air enters a 50-mm-diameter tube at a pressure of 5 atm, a temperature of
T
m
,
i
=
17
°
C
, and a flow rate of
m
˙
=
0.03
kg/s
, while saturated steam at 2.455 bars condenses on the outersurface of the tube. If the length of the annulus is
L
=
5
m
, what are the outlet temperature
T
m
,
o
, and pressure
p
o
of the air? What is the mass rate at which condensate leaves the annulus?
A two effect system of evaporators with parallel forward feed flow of liquid and vapor is to be designed to concentrate
continuously 10,000 Ib/h of a 10% by weight solution to 40%, the feed being at 150 °F. It is planned to use saturated steam
condensing at 220 °F. Specific Heat of feed liquor is 0.9, while that leaving the first effect is equal to the average specific
heat of feed and product. The overall heat transfer coefficients are 300 and 400 BTU/(f2-hr-°F) for the first and second
effects respectively. The latent heat of vaporization for the vapor leaving the first effect is 1002.3 BTU/lb and 1020 BTU/lb for
the second. Calculate for the steam economy and the heat transfer area in each effect.
Given:
(1)
Required:
and
Please help. I am not sure how to approach this problem. This problem involves heat transfer and internal flow within a pipe. Thank you.
Not Ai generated answers, I need to understand please show all steps.
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