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BAKER HUGHES - Drilling Fluids Reference Manual

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HYDRAULICS<br />

where:<br />

V p<br />

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

90L s<br />

t<br />

L s = stand length, ft<br />

t = time from slips to slips, sec<br />

2. Measurement of the time required for the middle joint of a three-joint stand to pass through the<br />

rotary table divided into the joint length.<br />

where:<br />

V p<br />

=<br />

Flow Regime<br />

60L<br />

---------- j<br />

t<br />

L j = joint length, ft<br />

t = time through rotary table, sec<br />

The possibility of turbulent flow in the annulus must be considered in surge and swab calculations.<br />

The equivalent fluid velocity may be compared to the critical flow rate for the annular section of<br />

interest previously calculated if the fluid properties or pipe diameters have not changed. If changes<br />

have occurred, calculate a new critical flow rate by following the steps outlined earlier.<br />

Surge or Swab Pressure<br />

The appropriate Fanning Friction Factor for annular flow and Friction-Loss Pressure Gradient are<br />

used to obtain the surge or swab pressure loss in each interval.<br />

Equivalent Fluid Weight<br />

In order to be meaningful, the surge or swab pressure and resulting equivalent fluid weight must be<br />

compared to some fracture gradient or pore pressure. The pressure drops in each annular interval<br />

are summed together, very similar to the steps used to obtain the Equivalent Circulating Density.<br />

When running pipe in the hole, the equivalent fluid weight due to the surge pressure is:<br />

EMW =ρ +<br />

∑ P<br />

( 0.052)( TVD)<br />

a<br />

When pulling pipe out of the hole, the equivalent fluid weight due to the swab pressure is,<br />

EMW =ρ −<br />

∑ P<br />

( 0.052)( TVD)<br />

a<br />

where:<br />

EMW = equivalent fluid weight, lb m /gal<br />

ρ = fluid density, lb m /gal<br />

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

REFERENCE MANUAL<br />

REVISION 2006 9-22

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