A cold air chamber is proposed for quenching steel ball bearings of diameter D = 0.2 m and initial temperature T i = 400 ° C . Air in the chamber is maintained at − 15 ° C by a refrigeration system, and the steel balls pass through the chamber on a conveyor belt. Optimum bearing production requires that 70 % of the initial thermal energy content of the ball above − 15 ° C be removed. Radiation effects may be neglected, and the convection heat transfer coefficient within the chamber is 1000 W/m 2 ⋅ K . Estimate the residence time of the balls within the chamber, and recommend a drive velocity of the conveyor. The following properties may be used for the steel: k = 50 W/m ⋅ K, α = 2 × 10 − 5 m 2 /s, and c = 450 J / k g ⋅ K .
A cold air chamber is proposed for quenching steel ball bearings of diameter D = 0.2 m and initial temperature T i = 400 ° C . Air in the chamber is maintained at − 15 ° C by a refrigeration system, and the steel balls pass through the chamber on a conveyor belt. Optimum bearing production requires that 70 % of the initial thermal energy content of the ball above − 15 ° C be removed. Radiation effects may be neglected, and the convection heat transfer coefficient within the chamber is 1000 W/m 2 ⋅ K . Estimate the residence time of the balls within the chamber, and recommend a drive velocity of the conveyor. The following properties may be used for the steel: k = 50 W/m ⋅ K, α = 2 × 10 − 5 m 2 /s, and c = 450 J / k g ⋅ K .
Solution Summary: The author describes the time required by the steel balls to stay in the chamber and recommend a drive velocity for the conveyer belt.
A cold air chamber is proposed for quenching steel ball bearings of diameter
D
=
0.2
m
and initial temperature
T
i
=
400
°
C
.
Air in the chamber is maintained at
−
15
°
C
by a refrigeration system, and the steel balls pass through the chamber on a conveyor belt. Optimum bearing production requires that
70
%
of the initial thermal energy content of the ball above
−
15
°
C
be removed. Radiation effects may be neglected, and the convection heat transfer coefficient within the chamber is
1000
W/m
2
⋅
K
.
Estimate the residence time of the balls within the chamber, and recommend a drive velocity of the conveyor. The following properties may be used for the steel:
k
=
50
W/m
⋅
K,
α
=
2
×
10
−
5
m
2
/s,
and
c
=
450
J
/
k
g
⋅
K
.
Please include free body diagram and please don't type
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Example 4.13. A thermocouple junction is in the form of 8 mm diameter sphere. Properties of
material are:
40 W/M2°C.
= 8000 kg/m³; k = 40 W/m°C and h
This junction is initially at 40°C and inserted in a stream of hot air at 300°C. Find:
%3D
420 J/kg°C; p
C =
(i) Time constant of the thermocouple;
(ii) The thermocouple is taken out from the hot air after 10 seconds and kept in still air at
30°C. Assuming the heat transfer coefficient in air 10 W/M²°C, find the temperature attained
by the junction 20 seconds after removing from hot air.
(P.U.)
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