h = 11 W/m K (outside furnace) Consider steady-state heat conduction through a cylindrical wall The fluid on the.inside. Fat 590 K with a heat transfer coefficiect of 23 W/m K. The temperature on the outside surfacc of the wall is known and maintained at 420 K. The heat flow rate through the cylindrical wall is 200 W per 1 m length of the cylinder. If the wall has a thermal conductivity of 0.17 W/m K, what are the inside and outside radii of the cylindrical wall? The rátio of the outside radius to inside radius is 2.

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h = 11 W/m K (outside furnace)
Consider steady-state heat conduction through a cylindrical wall The fluid on the inside.
Fat 590 Kwith a heat transfer coefficiert of 23 W/m K. The temperature on the outside
surfacc of the wall is known and maintained at 420 K. The heat flow rate through the cylindrical
wall is 200 W per 1 m length of the cylinder. If the wall has a thermal conductivity of 0.17 W/m
K, what are the inside and outside radii of the cylindrical wall? The rátio of the outside radius to
inside radius is 2.
Calculate the net heat flow by radiation to the furmace all at 530 K from the fumace
(3)
floor at 810 K. Both surfaces can be considered to be black radiators.
::!...:
1 1..
3.7
Ta - 1
Transcribed Image Text:h = 11 W/m K (outside furnace) Consider steady-state heat conduction through a cylindrical wall The fluid on the inside. Fat 590 Kwith a heat transfer coefficiert of 23 W/m K. The temperature on the outside surfacc of the wall is known and maintained at 420 K. The heat flow rate through the cylindrical wall is 200 W per 1 m length of the cylinder. If the wall has a thermal conductivity of 0.17 W/m K, what are the inside and outside radii of the cylindrical wall? The rátio of the outside radius to inside radius is 2. Calculate the net heat flow by radiation to the furmace all at 530 K from the fumace (3) floor at 810 K. Both surfaces can be considered to be black radiators. ::!...: 1 1.. 3.7 Ta - 1
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