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BAKER HUGHES - Drilling Fluids Reference Manual

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HYDRAULICS<br />

ρ = fluid density, lb m /gal<br />

If γ p > γ b , the slip velocity is determined by the equation below, slip velocity of a particle in<br />

turbulent flow.<br />

Turbulent Flow Condition<br />

Find the particle shear stress:<br />

where:<br />

τp<br />

= 7.9 T( 20.8 – ρ)<br />

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

2<br />

T = particle thickness, in.<br />

ρ = fluid density, lb m /gal.<br />

Slip velocity of a particle in turbulent flow is:<br />

where:<br />

V s<br />

16.62τp<br />

= ------------------<br />

ρ<br />

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

τ f /100 ft 2<br />

p = particle shear stress, lb<br />

ρ = fluid density, lb m /gal<br />

Cuttings Transport<br />

The cuttings transport for each different hole geometry is obtained by subtracting the slip velocity<br />

of the cuttings from the annular velocity in that particular section of the hole by:<br />

where:<br />

Vt<br />

= V a − V s<br />

V t = cuttings transport, ft/ min<br />

V a = annular velocity × 60, ft/min<br />

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

Transport Efficiency<br />

Perhaps more important than an actual cuttings transport value is the cuttings transport<br />

efficiency, which is simply the ratio of cuttings transport to annular velocity, defined by:<br />

E t<br />

V t<br />

----- × 100 1 V s<br />

= = ⎛ – ----- ⎞ × 100<br />

⎝ ⎠<br />

V a<br />

V a<br />

where,<br />

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

REFERENCE MANUAL<br />

REVISION 2006 9-26

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