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BAKER HUGHES - Drilling Fluids Reference Manual

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

The degree of torque is usually strongly influenced by the size of the cuttings bed upon which the<br />

pipe string is rotating. Often, the more inclined the hole, generally the larger the cuttings bed.<br />

This is increased by the amount of wall instability experienced (hole closure).<br />

Effect on Differential Sticking<br />

Differential pressure sticking is a condition in which the drill pipe becomes stuck against the wall<br />

of the wellbore because it has become embedded in the filter cake. There must be a permeable<br />

formation present and a pressure differential across a nearly impermeable filter cake. The quality<br />

of the filter cake and the rate of filtrate produced by the drilling fluid in use affect the possibility<br />

of differential sticking.<br />

NEW-DRILL fluids exhibit a compressible filter cake which helps considerably in preventing<br />

differential sticking. The NEW-DRILL system has accomplished this without the traditional<br />

liberal use of commercial bentonite. Cases of differential sticking in the field while using a<br />

NEW-DRILL system have been rare. In fact, highly depleted zones have been drilled utilizing<br />

the NEW-DRILL system with no occurrence of differential sticking. This has helped reduce fluid<br />

cost and prevent one of the most costly delays in drilling - stuck pipe<br />

Effects on Weight-On-Bit (WOB)<br />

Due to the reduced coefficient of friction from the NEW-DRILL, more effective collar weight is<br />

transferred to the bit. Less collar-to-wellbore friction has multiple benefits including less drill<br />

string wear. Reductions in torque of as much as 50% have been observed in the field.<br />

NEW-DRILL Operational Procedures<br />

NEW-DRILL systems have been developed through experience in several geographic areas under<br />

various drilling conditions. Consequently, techniques have been developed to meet the needs of<br />

customers at various locations.<br />

Methylene Blue Test (MBT)<br />

The performance of the NEW-DRILL System is based on a low colloid philosophy. Utilize<br />

solids control equipment for controlling solids content and plastic viscosity. Daily solids analysis<br />

must be used to monitor the solids content. Low gravity solid content is the key to proper control<br />

of the system. Total low gravity solids should be held in the range of 3 to 5% by volume,<br />

inclusive of commercial clay. Inadequate solids control equipment will cause increases in solids<br />

content and result in high rheological values and/or the need for a strong deflocculant such as<br />

UNI-CAL (lignosulfonate).<br />

Gel Strengths<br />

Gel strength values as determined by a 6-speed viscometer are generally higher for a NEW-<br />

DRILL system than traditional UNI-CAL lignosulfonate fluids. This illustrates the difference<br />

between a semi-dispersed as compared to a dispersed mud system. Also, the aqueous phase<br />

viscosity of the lignosulfonate system is only slightly greater than water while the NEW-DRILL ®<br />

system’s water is significantly thicker. It is common for 10-minute gels to reach 35 lb f /100 ft 2 .<br />

<strong>Drilling</strong> conditions and economics should determine the need to reduce gel strengths. Report the<br />

initial, 10-minute and 30-minute gel strengths on all NEW-DRILL systems.<br />

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

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

3-60 Revised 2006

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