The Kozeny–Carman equation (or Carman–Kozeny equation or Kozeny equation) is a relation used in the field of fluid dynamics to calculate the pressure drop of a fluid flowing through a packed bed of solids. It is named after Josef Kozeny and Philip C. Carman. The equation is only valid for creeping flow, i.e. in the slowest limit of laminar flow. The equation was derived by Kozeny (1927)[1] and Carman (1937, 1956)[2][3][4] from a starting point of (a) modelling fluid flow in a packed bed as laminar fluid flow in a collection of curving passages/tubes crossing the packed bed and (b) Poiseuille's law describing laminar fluid flow in straight, circular section pipes.
This equation holds for flow through packed beds with particle Reynolds numbers up to approximately 1.0, after which point frequent shifting of flow channels in the bed causes considerable kinetic energy losses.
This equation is a particular case of Darcy's law, with a very specific permeability. Darcy's law states that "flow is proportional to the pressure gradient and inversely proportional to the fluid viscosity" and is given as:
q
Combining these equations gives the final Kozeny equation for absolute (single phase) permeability:
where:
is the absolute (i.e., single phase) permeability.
History
The equation was first[8] proposed by Kozeny (1927)[1] and later modified by Carman (1937, 1956).[2][3] A similar equation was derived independently by Fair and Hatch in 1933.[9] A comprehensive review of other equations has been published.[10]
^Robert P. Chapuis and Michel Aubertin, "PREDICTING THE COEFFICIENT OF PERMEABILITY OF SOILS USING THE KOZENY-CARMAN EQUATION", Report EPM–RT–2003-03, Département des génies civil, géologique et des mines; École Polytechnique de Montréal, January 2003 https://publications.polymtl.ca/2605/1/EPM-RT-2003-03_Chapuis.pdf (accessed 2011-02-05)
^ G.M. Fair, L.P. Hatch, Fundamental factors governing the streamline flow of water through sand, J. AWWA 25 (1933) 1551–1565.
^ E. Erdim, Ö. Akgiray and İ. Demir, A revisit of pressure drop-flow rate correlations for packed beds of spheres, Powder Technology Volume 283, October 2015, Pages 488-504
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