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BAKER HUGHES - Drilling Fluids Reference Manual

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PRESSURE PREDICTION AND CONTROL<br />

gradients are low, it may be necessary to take special precautions to avoid breaking down a<br />

formation.<br />

Riser Collapse / Displacement / Trapped Gas<br />

After formation gas has been circulated from the wellbore through the choke lines and the well<br />

is dead, a small volume of gas can be trapped in the sub-sea BOP between the choke line and<br />

uppermost closed BOP. If this trapped gas is not removed before opening the stack, its<br />

expansion can deplete the riser of fluid and cause another kick, collapse of the riser, or both. It<br />

is critical that before the BOPs are opened, (1) the riser has been displaced with kill fluid and<br />

(2) trapped gas has been removed from the BOP stack. A technique that has been proven<br />

successful is discussed by Shaunessy, et al.<br />

Gas Hydrates<br />

Gas hydrates are an ice-like mixture of natural gas and water. Their formation is a function of<br />

pressure and temperature. At low temperatures (30°F to 40°F), hydrate formation can occur at<br />

low pressures (40 to 400 psi). In the deepwater depths being drilled in the Gulf Coast,<br />

temperatures at the sea floor can be as low as 40°F. There have been several instances while<br />

killing kicks where the formation of gas hydrates has plugged choke lines and BOP stacks,<br />

making well control difficult or impossible.<br />

The suppression of hydrate formation can be accomplished by increasing the chloride<br />

concentration of the drilling fluid. Fluid systems with chlorides in the 150,000 mg/L (≈ 21% by<br />

wt.) range will suppress hydrate formation by 26°F. These fluid systems have been used to<br />

prevent the formation of gas hydrates. A discussion of the components of these systems can be<br />

found in Chapter 1, Fundamentals of <strong>Drilling</strong> <strong>Fluids</strong>.<br />

Other potential hydrate suppressors are methanol, glycol, and oil. Problems with the use of<br />

these additives relate to their toxicity levels and their use may be prohibitive because of<br />

handling and disposal requirements. Another option is to insulate and heat the subsea well<br />

control equipment but, at present, the technology to do this has not been developed.<br />

Commonly Used Equations in Pressure Control<br />

Hydrostatic Pressure (psi)<br />

Pressure Gradient (psi/ft)<br />

Hydrostatic Pressure = 0.052 x MW 1 x TVD<br />

Pressure Gradient = MW 1 x 0.052<br />

Pressure Expressed as Equivalent Fluid (Mud) Weight (EMW)<br />

EMW =<br />

0.052P s<br />

× TVD<br />

+ MW 1<br />

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

REFERENCE MANUAL<br />

REVISION 2006 12-40

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