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Kozeny–Carman equation

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Relation used in the field of fluid dynamics

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) and Carman (1937, 1956) 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.

Equation

The equation is given as:

Δ P L = 150 μ Φ s 2 d p 2 ( 1 − ε ) 2 ε 3 V 0 {\displaystyle {\frac {\Delta P}{L}}={\frac {150\mu }{{\mathit {\Phi }}_{\mathrm {s} }^{2}d_{\mathrm {p} }^{2}}}{\frac {(1-\varepsilon )^{2}}{\varepsilon ^{3}}}V_{\mathrm {0} }}

where:

  • Δ P {\displaystyle \Delta P} is the pressure drop;
  • L {\displaystyle L} is the total height of the bed;
  • μ {\displaystyle \mu } is the viscosity of the fluid;
  • ε {\displaystyle \varepsilon } is the porosity of the bed ( ≃ 0.37 {\displaystyle \simeq 0.37} for randomly packed spheres);
  • Φ s {\displaystyle {\mathit {\Phi }}_{\mathrm {s} }} is the sphericity of the particles in the packed bed ( Φ s {\displaystyle {\mathit {\Phi }}_{\mathrm {s} }} = 1.0 for spherical particles);
  • d p {\displaystyle d_{\mathrm {p} }} is the diameter of the volume equivalent spherical particle;
  • V 0 {\displaystyle V_{\mathrm {0} }} is the superficial or "empty-tower" velocity which is directly proportional to the average volumetric fluid flux in the channels (q), and porosity ( ε {\displaystyle \mathbf {\varepsilon } } ).

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 = κ μ Δ P L {\displaystyle ={\frac {\kappa }{\mu }}{\frac {\Delta P}{L}}}

Combining these equations gives the final Kozeny equation for absolute (single phase) permeability:

κ = Φ s 2 ε 3 d p 2 180 ( 1 − ε ) 2 {\displaystyle \kappa ={\mathit {\Phi }}_{\mathrm {s} }^{2}{\frac {\varepsilon ^{3}d_{\mathrm {p} }^{2}}{180(1-\varepsilon )^{2}}}}

where:

  • κ {\displaystyle \kappa } is the absolute (i.e., single phase) permeability.

History

The equation was first proposed by Kozeny (1927) and later modified by Carman (1937, 1956). A similar equation was derived independently by Fair and Hatch in 1933. A comprehensive review of other equations has been published.

See also

References

  1. ^ J. Kozeny, "Ueber kapillare Leitung des Wassers im Boden." Sitzungsber Akad. Wiss., Wien, 136(2a): 271-306, 1927.
  2. ^ P.C. Carman, "Fluid flow through granular beds." Transactions, Institution of Chemical Engineers, London, 15: 150-166, 1937.
  3. ^ P.C. Carman, "Flow of gases through porous media." Butterworths, London, 1956.
  4. ^ Fluid Mechanics, Tutorial No. 4: Flow through porous passages (PDF)
  5. McCabe, Warren L.; Smith, Julian C.; Harriot, Peter (2005), Unit Operations of Chemical Engineering (seventh ed.), New York: McGraw-Hill, pp. 152–153, ISBN 0-07-284823-5
  6. Wu, Yugong; Fan, Zhigang; Lu, Yuzhu (2003-05-01). "Bulk and interior packing densities of random close packing of hard spheres". Journal of Materials Science. 38 (9): 2019–2025. doi:10.1023/A:1023597707363. ISSN 1573-4803. S2CID 137583828.
  7. McCabe, Warren L.; Smith, Julian C.; Harriot, Peter (2005), Unit Operations of Chemical Engineering (seventh ed.), New York: McGraw-Hill, pp. 188–189, ISBN 0-07-284823-5
  8. 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)
  9. G.M. Fair, L.P. Hatch, Fundamental factors governing the streamline flow of water through sand, J. AWWA 25 (1933) 1551–1565.
  10. 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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