A concentric lube arrangement, for which the inner and outer diameters are 8 0 mm and 100 mm . respectively, is used to remove heat from a biochemical reaction occurring in a 1 − m -long settling tank. Heat is generated uniformly within the tank at a rate of 10 5 W/m 3 , and water is supplied to the annular region at a rate of 0. 2 kg / s . (a) Determine the inlet temperature of the supply water that will maintain an average tank surface temperature of 37 ° C . Assume fully developed flow and thermal conditions. Is this assumption reasonable? (b) It is desired to have a slight, axial temperature gradient on the tank surface, since the rate of the biochemical reaction is highly temperature dependent. Sketch the axial variation of the water and surface temperatures along the flow direction for the following two cases: (i) the fully developed conditions of part (a), and (ii) conditions for which entrance effects are important. Comment on features of the temperature distributions. What change to the system or operating conditions would you make to reduce the surface temperature gradient?
A concentric lube arrangement, for which the inner and outer diameters are 8 0 mm and 100 mm . respectively, is used to remove heat from a biochemical reaction occurring in a 1 − m -long settling tank. Heat is generated uniformly within the tank at a rate of 10 5 W/m 3 , and water is supplied to the annular region at a rate of 0. 2 kg / s . (a) Determine the inlet temperature of the supply water that will maintain an average tank surface temperature of 37 ° C . Assume fully developed flow and thermal conditions. Is this assumption reasonable? (b) It is desired to have a slight, axial temperature gradient on the tank surface, since the rate of the biochemical reaction is highly temperature dependent. Sketch the axial variation of the water and surface temperatures along the flow direction for the following two cases: (i) the fully developed conditions of part (a), and (ii) conditions for which entrance effects are important. Comment on features of the temperature distributions. What change to the system or operating conditions would you make to reduce the surface temperature gradient?
Solution Summary: The author calculates the water properties at temperature 304 k and the convection rate equation applied to the inner surface.
A concentric lube arrangement, for which the inner and outer diameters are
8
0
mm
and
100
mm
. respectively, is used to remove heat from a biochemical reaction occurring in a
1
−
m
-long settling tank. Heat is generated uniformly within the tank at a rate of
10
5
W/m
3
, and water is supplied to the annular region at a rate of
0.
2 kg
/
s
.
(a) Determine the inlet temperature of the supply water that will maintain an average tank surface temperature of
37
°
C
. Assume fully developed flow and thermal conditions. Is this assumption reasonable?
(b) It is desired to have a slight, axial temperature gradient on the tank surface, since the rate of the biochemical reaction is highly temperature dependent. Sketch the axial variation of the water and surface temperatures along the flow direction for the following two cases: (i) the fully developed conditions of part (a), and (ii) conditions for which entrance effects are important. Comment on features of the temperature distributions. What change to the system or operating conditions would you make to reduce the surface temperature gradient?
An electric heater heats the inner tube walls of a concentric tube annulus at a rate of 2000 W/m. The inner and outer tube diameters are 25 and 50 mm respectively. Water enters the annular region at 25 ⁰C and leaves at 85 ⁰C. The flow rate of water is 0.04 kg/s and the outer tube wall is insulated. Assuming that fully developed conditions exist at the outlet, the inner tube surface temperature at the outlet will be ?
I need the answer as soon as possible
A 10-mm-inner-diameter pipe made of commercial steel is used to heat a liquid in an industrial process. The liquid enters the pipe with Ti=25°C, V=0.8 m/s. A uniform heat flux is maintained by an electric resistance heater wrapped arounf the outer surface of the pipe, so that the fluid exits at 75°C. Assuming fully developed flow and taking the average fluid properties to be ρ=1000 kg/m3, cp=4000 J/kg·K, µ=2x10-3 kg/m·s, k=0.48 W/m·K, and Pr=10, determine:
The required surface heat flux , produced by the heater
The surface temperature at the exit, Ts
The pressure loss through the piper and the minimum power required to overcome the resistance to flow.
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