A bayonet cooler is used to reduce the temperature of a pharmaceutical fluid. The pharmaceutical fluid flows through the cooler, which is fabricated of l 0 − mm diameter, thin—walled tubing with two 25 0 − mm —long straight sections and a coil with six and a half turns and a coil diameter of 75 mm . A coolant flows outside the cooler, with a convection coefficient at the outside surface of h = 5 00 W / m 2 K and a coolant temperature of 2 0 ° C . Consider the situation where the pharmaceutical fluid enters at 9 0 ° C with a mass flow rate of 0.00 5 kg / s . The pharmaceutical has the following properties: ρ = 1200 Kg / m 3 , μ = 4 × 10 − 3 N ⋅ s/m 2 , c p = 2000 J/Kg ⋅ K , k = 0.5 W/m ⋅ K , and k = 0.5 W/m ⋅ K . (a) Determine the outlet temperature of the pharmaceutical fluid. (b) It is desired to further reduce the outlet temperature of the pharmaceutical. However, because the cooling process is just one pan of an intricate processing operation, flow rates cannot be changed. A young engineer suggests that the outlet temperature might be reduced by inserting stainless steel coiled springs into the straight sections of the cooler with the notion that the springs will disturb the how adjacent to the inner tube wall and, in turn, increase the heat transfer coefficient at the inner tube wall. A senior engineer asserts that insertion of the springs should double the heat transfer coefficient at the straight inner tube walls. Determine the outlet temperature of the pharmaceutical fluid with the springs inserted into the tubes, assuming the senior engineer is correct in his assertion. (c) Would you expect the outlet temperature of the pharmaceutical to depend on whether the springs have a left-hand or right-hand spiral? Why?
A bayonet cooler is used to reduce the temperature of a pharmaceutical fluid. The pharmaceutical fluid flows through the cooler, which is fabricated of l 0 − mm diameter, thin—walled tubing with two 25 0 − mm —long straight sections and a coil with six and a half turns and a coil diameter of 75 mm . A coolant flows outside the cooler, with a convection coefficient at the outside surface of h = 5 00 W / m 2 K and a coolant temperature of 2 0 ° C . Consider the situation where the pharmaceutical fluid enters at 9 0 ° C with a mass flow rate of 0.00 5 kg / s . The pharmaceutical has the following properties: ρ = 1200 Kg / m 3 , μ = 4 × 10 − 3 N ⋅ s/m 2 , c p = 2000 J/Kg ⋅ K , k = 0.5 W/m ⋅ K , and k = 0.5 W/m ⋅ K . (a) Determine the outlet temperature of the pharmaceutical fluid. (b) It is desired to further reduce the outlet temperature of the pharmaceutical. However, because the cooling process is just one pan of an intricate processing operation, flow rates cannot be changed. A young engineer suggests that the outlet temperature might be reduced by inserting stainless steel coiled springs into the straight sections of the cooler with the notion that the springs will disturb the how adjacent to the inner tube wall and, in turn, increase the heat transfer coefficient at the inner tube wall. A senior engineer asserts that insertion of the springs should double the heat transfer coefficient at the straight inner tube walls. Determine the outlet temperature of the pharmaceutical fluid with the springs inserted into the tubes, assuming the senior engineer is correct in his assertion. (c) Would you expect the outlet temperature of the pharmaceutical to depend on whether the springs have a left-hand or right-hand spiral? Why?
Solution Summary: The author explains the outlet temperature of pharmaceutical fluid, the convection heat coefficient, density, viscosity, and thermal conductivity of the fluid.
A bayonet cooler is used to reduce the temperature of a pharmaceutical fluid. The pharmaceutical fluid flows through the cooler, which is fabricated of
l
0
−
mm
diameter, thin—walled tubing with two
25
0
−
mm
—long straight sections and a coil with six and a half turns and a coil diameter of
75 mm
. A coolant flows outside the cooler, with a convection coefficient at the outside surface of
h
=
5
00
W
/
m
2
K
and a coolant temperature of
2
0
°
C
. Consider the situation where the pharmaceutical fluid enters at
9
0
°
C
with a mass flow rate of
0.00
5 kg
/
s
. The pharmaceutical has the following properties:
ρ
=
1200
Kg
/
m
3
,
μ
=
4
×
10
−
3
N
⋅
s/m
2
,
c
p
=
2000
J/Kg
⋅
K
,
k
=
0.5
W/m
⋅
K
, and
k
=
0.5
W/m
⋅
K
.
(a) Determine the outlet temperature of the pharmaceutical fluid.
(b) It is desired to further reduce the outlet temperature of the pharmaceutical. However, because the cooling process is just one pan of an intricate processing operation, flow rates cannot be changed. A young engineer suggests that the outlet temperature might be reduced by inserting stainless steel coiled springs into the straight sections of the cooler with the notion that the springs will disturb the how adjacent to the inner tube wall and, in turn, increase the heat transfer coefficient at the inner tube wall. A senior engineer asserts that insertion of the springs should double the heat transfer coefficient at the straight inner tube walls. Determine the outlet temperature of the pharmaceutical fluid with the springs inserted into the tubes, assuming the senior engineer is correct in his assertion.
(c) Would you expect the outlet temperature of the pharmaceutical to depend on whether the springs have a left-hand or right-hand spiral? Why?
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.
Water at a flow rate of 0.215 kg/s is cooled from 70°C to 30°C by passing it through a thin-walled tube of diameter of 50 mm and maintaining a coolant at 15°C in cross flow over the tube. What is the required tube length if the coolant is air and its velocity is V = 20 m/s?Water : cp = 4181 J/kg⋅K, μ = 548 × 10-6 N⋅s/m2, k = 0.643 W/m⋅K, Pr = 3.56.Air : ν = 15.89 × 10-6 m2/s, k = 0.0263 W/m⋅K, Pr = 0.707.(Hint: For external flow use Churchill/Bernstein correlation.)
Need a deep-dive on the concept behind this application? Look no further. Learn more about this topic, mechanical-engineering and related others by exploring similar questions and additional content below.