An experiment is designed to study microscale forced convection. Water at T m , i = 300 K is to be heated in a straight, circular glass tube with a 50 - μ m inner diameter and a wall thickness of 1 mm . Warm water at T ∞ = 350 K , V = 2 m / s is in cross flow over the exterior tube surface. The experiment is to be designed to cover the operating range 1 ≤ Re D ≤ 2000 , where Re D , is the Reynolds number associated with the internal flow. (a) Determine the tube length L that meets a design requirement that the tube be twice as long as the thermal entrance length associated with the highest Reynolds number of interest. Evaluate water properties at 3 0 5 K . (b) Determine the water outlet temperature T m , o , that is expected to be associated with Re D = 2000 . Evaluate the heating water (water in cross flow over the tube) properties at 33 0 K . (c) Calculate the pressure drop from the entrance to the exit of the tube for Re D = 2000 . (d) Based on the calculated flow rate and pressure drop in the tube, estimate the height of a column of water (at 3 00 K ) needed w supply the necessary pressure at the tube entrance and the time needed to collect 0.1 liter of water. Discuss how the outlet temperature of the water flowing from the tube, T m , o , might be measured.
An experiment is designed to study microscale forced convection. Water at T m , i = 300 K is to be heated in a straight, circular glass tube with a 50 - μ m inner diameter and a wall thickness of 1 mm . Warm water at T ∞ = 350 K , V = 2 m / s is in cross flow over the exterior tube surface. The experiment is to be designed to cover the operating range 1 ≤ Re D ≤ 2000 , where Re D , is the Reynolds number associated with the internal flow. (a) Determine the tube length L that meets a design requirement that the tube be twice as long as the thermal entrance length associated with the highest Reynolds number of interest. Evaluate water properties at 3 0 5 K . (b) Determine the water outlet temperature T m , o , that is expected to be associated with Re D = 2000 . Evaluate the heating water (water in cross flow over the tube) properties at 33 0 K . (c) Calculate the pressure drop from the entrance to the exit of the tube for Re D = 2000 . (d) Based on the calculated flow rate and pressure drop in the tube, estimate the height of a column of water (at 3 00 K ) needed w supply the necessary pressure at the tube entrance and the time needed to collect 0.1 liter of water. Discuss how the outlet temperature of the water flowing from the tube, T m , o , might be measured.
An experiment is designed to study microscale forced convection. Water at
T
m
,
i
=
300
K
is to be heated in a straight, circular glass tube with a
50
-
μ
m
inner diameter and a wall thickness of
1 mm
. Warm water at
T
∞
=
350
K
,
V
=
2
m
/
s
is in cross flow over the exterior tube surface. The experiment is to be designed to cover the operating range
1
≤
Re
D
≤
2000
, where
Re
D
, is the Reynolds number associated with the internal flow. (a) Determine the tube length L that meets a design requirement that the tube be twice as long as the thermal entrance length associated with the highest Reynolds number of interest. Evaluate water properties at
3
0
5 K
. (b) Determine the water outlet temperature
T
m
,
o
, that is expected to be associated with
Re
D
=
2000
. Evaluate the heating water (water in cross flow over the tube) properties at
33
0
K
. (c) Calculate the pressure drop from the entrance to the exit of the tube for
Re
D
=
2000
. (d) Based on the calculated flow rate and pressure drop in the tube, estimate the height of a column of water (at
3
00
K
) needed w supply the necessary pressure at the tube entrance and the time needed to collect 0.1 liter of water. Discuss how the outlet temperature of the water flowing from the tube,
T
m
,
o
, might be measured.
A liquid metal flows at a mass rate of 3 kg/s through a constant heat flux 5-cm-i.d tube in a nuclear reactor. The fluid at 473 K is to be heated with the tube wall 30 K above the fluid temperature. Determine the length of the tube required for a 1-K rise in bulk fluid temperature, using the following properties: p = 7.7 x 10^3 kg/m^3v = 8.0 x 10^-8 m^2/sCp = 130 J/(kg K)k = 12 W/mKPr = 0.011
Kaufman's correlation: Nu = 0,625.(Re.Pr)0,4
Glycerin passes through a pipe of 30 mm inside diameter at a mass flow rate of 700 kg / hr. The wall of the 2.5 m heating section of the pipe is kept constant at 115 ° C. The glycerin inlet temperature is given as 15C. What is the exit temperature of glycerin from the pipe?
A liquid metal flows at the rate of 4kg/s through a constant heat flux 6cm inner diameter tube in a nuclear reactor. The fluid at 200 oC is to be heated with the tube wall 40 oC above the fluid temperature. Determine the length of the tube required 25 oC rise in bulk fluid temperature. Using the following properties: ρ = 7700 kg/m3 , Y = 8*10-8 m2/s , Pr=0.011 , Cp= 130 J/kg.K , k=12W/mk.
please can you solve it with keyboard,take your time
heat transfer, J.P.Holman .
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