A fluid is flowing through a circulat tube at 0.4 kg/s. Tube inner surface is smooth with a diameter 0.014 m. Fluid density is 990 kg/m^3, specific heat is 3,845 J/(kg-K), viscosity is 0.00079 Ns/m^2, thermal conductivity is 0.74, and Prandtl number is 8.6. A uniform heat flux of 71,297 W/m^2 is supplied to the flow from the surface. If the flow is fully developed, what is the convection coefficient in W/(m^2-K)

Respuesta :

Answer:

The convection coefficient is [tex]15456.48\ W/m^{2}K[/tex]

Solution:

Mass flow rate, [tex]\dot{m} = 0.4\ kg[/tex]

Inner diameter of the tube, d = 0.014 m

Fluid density, [tex]\rho_{f} = 990\ kg/m^{3}[/tex]

Specific Heat, C = 3845 J/K

Thermal Conductivity, K = 0.74

Prandtl Number, [tex]P_{r} = 8.6[/tex]

Heat flux, [tex]\dot{q} = 71,297\ W/m^{2}[/tex]

Viscosity, [tex]\mu = 0.00079\ Ns/m^{2}[/tex]

Now,

To calculate the convection heat coefficient, h:

Determine the cross sectional area of the circular tube:

[tex]A_{c} = \frac{\pi}{4}d^{2} = \frac{\pi}{4}\times (0.014)^{2} = 1.54\time 10^{- 4}\ m^{2}[/tex]

Determine the velocity of the fluid inside the tube by mass flow rate:

[tex]\dot{m} = \rho_{f}A_{c}v[/tex]

[tex]0.4 = 990\times 1.54\time 10^{- 4}v[/tex]

v = 2.624 m/s

Determine the Reynold's Number, [tex]R_{e}[/tex]:

[tex]R_{e} = \frac{\rho_{f}dv}{\mu}[/tex]

[tex]R_{e} = \frac{990\times 0.014\times 2.624}{0.00079} = 46036.253[/tex]

Thus it is clear that [tex]R_{e}[/tex] > 10,000 hence flow is turbulent.

Now,

Determine the Nusselt Number:

[tex]N_{u} = 0.023R_{e}^{0.8}P_{r}^{0.4}[/tex]

[tex]N_{u} = 0.023\times 46036.253^{0.8}\times 8.6^{0.4} = 292.42[/tex]

Also,

[tex]N_{u} = \frac{dh}{K}[/tex]

where

h = convection coefficient

Now,

[tex]292.42 = \frac{0.014\times h}{0.74}[/tex]

[tex]h = 15456.48\ W/m^{2}K[/tex]