Section 2: Boundary Layer and Turbulence

MODULE 2

Section 1:   

Boundary Layer and Turbulence

Section 2:
Pressure Drop and Friction Factor

Section 3:   

Heat Transfer Coefficient

Section 4:   

Convection With Change of Phase

 

 

Pressure Drop and Friction Factor

 

Several formulations are available to estimate the friction factor for turbulent flows. Correlations that reasonably approximate the smooth surface condition are: 

f = 0.316Red-0.25      Red < 2x104               (3.14)

f = 0.184Red-0.2        Red < 2x104               (3.15)

 

Another option to estimate the friction factor is to use the Moody diagram, figure 6. This graphical approach is a compilation of several empiric formulations.

In addition to depending on the Reynolds number the friction factor is a function of the tube surface condition. It is a minimum for smooth surfaces and increases with increasing surface roughness.

Fig. 6. Moody Diagram

The friction factor is also temperature dependent and Seider and Tate suggest the correction:

 

(3-16)


where

fiso is the friction factor for the isothermal case, mw the fluid viscosity close to the wall and mf the average fluid viscosity.

The power required to overcome the pressure drop is estimated by:

 

(3.17)

In a circuit the total pressure drop is estimated by the algebraic sum of the distributed losses along the tubes (estimated by 3.12) and the frictional losses (due to singularities such as expansions, contractions, valves, bands, etc.).

 

 

 Previous page

 Back to the Menu

Next Section

2/2

 
  Tutorials   NUSAFE