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BAKER HUGHES - Drilling Fluids Reference Manual

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HYDRAULICS<br />

Laminar Flow Condition<br />

Find the boundary shear rate,<br />

186<br />

γ b = --------------<br />

D c ρ<br />

where,<br />

γ b = boundary shear rate, sec -1<br />

D c = particle diameter, in.<br />

ρ = fluids density, lb m /gal<br />

Find the shear stress developed by the particle:<br />

τ = 7.9 T 20.8 –<br />

p ( ρ)<br />

where,<br />

τ p = particle shear stress, lb f /100 ft 2<br />

T = particle thickness, in.<br />

ρ = fluid density, lb m /gal<br />

Find the shear rate developed by the particle using the annular power law constants for the fluid:<br />

1<br />

⎛<br />

γ p<br />

= ------<br />

τ p⎞ n ----<br />

a<br />

⎜ ⎟<br />

⎝K a ⎠<br />

where,<br />

γ p = particle shear rate, sec -1<br />

τ p = particle shear stress, lb f /100ft 2<br />

n a = annular flow behavior index<br />

K a = annular consistency factor, poise<br />

If γ p < γ b<br />

, the slip velocity is determined by:<br />

(<br />

V s = 1.22τ p ----------------------<br />

γp) ( D c )<br />

ρ<br />

1/2<br />

where,<br />

V s = slip velocity, ft/min<br />

τ p = particle shear stress, lb f /100 ft 2<br />

γ<br />

-1<br />

p = particle shear rate, sec<br />

D c = particle diameter, in.<br />

<strong>BAKER</strong> <strong>HUGHES</strong> DRILLING FLUIDS<br />

REFERENCE MANUAL<br />

REVISION 2006 9-25

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