Griffith correlation

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Brief

The Griffith correlation [1] is an empirical correlation which defines:

  • The boundary between the bubble and slug flow[2]
  • The void fraction of gas in bubble flow - gas hold up Hg[2]

Math & Physics

The bubble flow exist when:

 \frac{q_g}{q_g + q_L} < L_B [2]
 L_B = 1.071 - 0.2218 \frac{(v_g+v_L)^2}{D}, with the limit  L_B \geqslant 0.13 [2]

The gas holdup:

 H_g = \frac{1}{2}\ \left ( 1 + \frac{v_g+v_L}{v_s} - \sqrt{ \left ( 1 + \frac{v_g+v_L}{v_s} \right )^2 - 4 \frac{v_g}{v_s}}   \right ) [2]

Discussion

Nomenclature

 H_g = gas holdup factor, dimensionless
 f = friction factor, dimensionless
 GLR = gas-liquid ratio, scf/bbl
 M = total mass of oil, water and gas associated with 1 bbl of liquid flowing into and out of the flow string, lbm/bbl
 N_D = pipe diameter number number, dimensionless
 N_GV = gas velocity number, dimensionless
 N_L = liquid viscosity number, dimensionless
 N_LV = liquid velocity number, dimensionless
 p = pressure, psia
 q_c = conversion constant equal to 32.174, lbmft / lbfsec2
 q_L = total liquid production rate, bbl/d
 Re = Reynolds number, dimensionless
 R_s = solution gas-oil ratio, scf/stb
 SG = specific gravity, dimensionless
 T = temperature, °R or °K, follow the subscript
 v = velocity, ft/sec
 WOR = water-oil ratio, bbl/bbl
 z = gas compressibility factor, dimensionless

References

  1. Griffith, P.; Wallis, G. B. (August 1961). "Two-Phase Slug Flow"Paid subscription required. Journal of Heat Transfer. ASME. 83: 307–320. 
  2. 2.0 2.1 2.2 2.3 2.4 Orkiszewski, J. (June 1967). "Predicting Two-Phase Pressure Drops in Vertical Pipe"Paid subscription required. Journal of Petroleum Technology. SPE. 19 (SPE-1546-PA).