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BAKER HUGHES - Drilling Fluids Reference Manual

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Water Based <strong>Drilling</strong> <strong>Fluids</strong><br />

bacteria will attack the starch and fermentation will proceed at a rapid rate. This will be observed<br />

by a rapid loss of fluid loss control.<br />

Prehydrated MILGEL and Salt <strong>Fluids</strong><br />

Pre-hydrated MILGEL salt fluids are used in top hole drilling for hole cleaning and suspension.<br />

The pre-hydrated MILGEL slurry increases the yield point and gel strengths due to flocculation<br />

of the bentonite with salt compounds. These properties give the fluid excellent carrying capacity.<br />

Colloidal Protected MILGEL may be pre-hydrated as follows.<br />

• 1.0 bbl Drill Water<br />

• Soda Ash (as needed)<br />

• 0.5 lbm/bbl Caustic Soda<br />

• 20 to 25 lbm/bbl MILGEL<br />

• 0.50 to 2.0 lbm/bbl UNI-CAL<br />

• 15 to 20 lbm/bbl additional MILGEL<br />

This slurry should be mixed thoroughly before it is added to the salty drilling fluid.<br />

Since pre-hydrated bentonite contributes very little to fluid loss control, normal salt water fluid<br />

loss control materials such as MILSTARCH should be used as required.<br />

The high gel strengths of these fluids contribute to the retention of air or gas. Adding small<br />

quantities of MIL-PAC and UNI-CAL will aid in controlling gel strengths and allow gases to<br />

break out of the fluid. LD-8 or the alcohol-base defoamers may also be required to control gas or<br />

air entrainment and foaming.<br />

Avoid using surface guns for fluid agitation because they tend to inject air into the system,<br />

foaming problems are inherent to saturated salt systems.<br />

High-Salt or Salt-Saturated Polymer <strong>Fluids</strong><br />

High-molecular-weight polysaccharides and XAN-PLEX ® (xanthan gum) are unique because<br />

they perform in saturated salt water as well as freshwater. XAN-PLEX has shear thinning<br />

characteristics which result in very low bit viscosities with good annular viscosity recovery as<br />

shear rate decreases. This characteristic contributes to increased penetration rates and good hole<br />

cleaning.<br />

Under laboratory conditions these polymers start to degrade at temperatures above 250°F.<br />

However, this does not prevent their practical use at temperatures greater than this range.<br />

Polymers tend to exhibit lower viscosities as temperature increases. Viscosity may decrease to<br />

one-half or less when temperature is increased from 125°F to 250°F. For this reason,<br />

supplementing the material with small quantities of pre-hydrated MILGEL (5 to 10 lbm/bbl)<br />

would be advantageous. Bentonite tends to flocculate at elevated temperatures, which helps<br />

counteract the temperature thinning action on the polymers.<br />

If an API filtrate below 20 to 25 cc/30 min is desired, it is necessary to add a supplementary<br />

filtration control material such as BIO-LOSE ® or MIL-PAC. Small additions of MIL-PAC (0.1<br />

to 0.25 lbm/bbl) may have a thinning effect on these fluids if they contain flocculated drill solids.<br />

Although deflocculants are not normally added to this system, pre-solubilized UNI-CAL can be<br />

added. The pH of these fluids is usually maintained on the basic side (10.0) to minimize<br />

hardness. Caustic Soda is used, but should be added slowly to prevent momentary pH humps<br />

<strong>Reference</strong> <strong>Manual</strong><br />

Baker Hughes <strong>Drilling</strong> <strong>Fluids</strong><br />

3-36 Revised 2006

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