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The Ergun equation, derived by the Turkish chemical engineer Sabri Ergun in 1952, expresses the friction factor in a packed column as a function of the Reynolds number:

 f_p = \frac {150}{Re_p} + 1.75

where fp and Rep are defined as

f_p = \frac{\Delta p}{L} \frac{D_p}{\rho V_s^2} (\frac{\epsilon^3}{1-\epsilon}) and Re_p = \frac{D_p V_s \rho}{(1-\epsilon)\mu}

where: Δp is the pressure drop across the bed,
L is the length of the bed (not the column),
Dp is the equivalent spherical diameter of the packing,
ρ is the density of fluid,
μ is the dynamic viscosity of the fluid,
Vs is the superficial velocity (i.e. the velocity that the fluid would have through the empty tube at the same volumetric flow rate), and
ε is the void fraction of the bed(Bed porosity at any time).

References

Flow through packed beds


Sabri Ergun (1 March 1918 in Turkey - 18 February 2006) was a chemical engineer.

He is widely recognized for his enthusiasm and many contributions to the fields of chemical engineering and solid state physics.

Ergun Equation

The Ergun Equation is a correlation derived by Ergun in 1952 for the friction factor in a packed column as a function of the Reynolds number:

f_p = \frac {150}{Re_p} + 1.75

where f_p and Re_p are defined as

f_p = \frac{\Delta p}{L} \frac{D_p}{\rho V_s^2} (\frac{\epsilon^3}{1-\epsilon}) and Re_p = \frac{D_p V_s \rho}{(1-\epsilon)\mu}

where: \Delta p is the pressure drop across the bed,
L is the length of the bed (not the column),
D_p is the equivalent spherical diameter of the packing,
\rho is the density of fluid,
\mu is the dynamic viscosity of the fluid,
V_s is the superficial velocity (i.e. the velocity that the fluid would have through the empty tube at the same volumetric flow rate), and
\epsilon is the void fraction of the bed(Bed porosity at any time).

References

Flow through packed beds








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