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BAKER HUGHES - Drilling Fluids Reference Manual

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

above 11.0, which can be detrimental to the polymer. In most drilling situations (high salinity<br />

and pH), these polymers will not usually biodegrade. If, however, a polymer system is to be<br />

stored or bacterial degradation is a possibility, a preservative should be added (0.25 to 0.5<br />

lbm/bbl).<br />

Note:<br />

Once fermentation starts, it is too late to treat with a preservative.<br />

Although this system has mostly been associated with low-solids applications, it can be weighted<br />

if higher densities are necessary. The performance of a weighted system can be improved with a<br />

centrifuge and fine screens on the shakers to minimize the incorporation of drilled solids.<br />

Phosphate-Treated <strong>Fluids</strong><br />

Phosphates are used for deflocculating drilling fluids. The ones most commonly used are sodium<br />

tetraphosphate (OILFOS ® ) which has a pH near 7.0 and sodium acid pyrophosphate (SAPP)<br />

which has a pH near 4.0.<br />

Sodium tetraphosphate and SAPP are most commonly used to control rheological properties in<br />

freshwater, low-solids systems. Treatments of 0.1 to 0.2 lbm/bbl are normally sufficient when the<br />

system is maintained in the 8.0 to 9.0 pH range. Care should be taken to avoid overtreatments<br />

which results in excessive viscosity.<br />

Since SAPP sequesters calcium and reduces pH, it is often used to combat cement contamination.<br />

The amount required depends upon the severity of the contamination. However, as a general<br />

guide, 0.2 lbm/bbl of SAPP will treat out approximately 200 mg/l of calcium ion. Monitor the<br />

chemical properties of the fluid (P m , pH, P f , Ca ++ ) carefully. When the P m to P f ratio approaches<br />

3:1, discontinue use of SAPP to avoid over treatment.<br />

Phosphates revert to orthophosphates at temperatures above 175°F. Orthophosphates will not<br />

thin above this temperature, but still function as a sequestering agent. Therefore, this material is<br />

rarely used at deeper depths, because of the temperatures normally encountered. Phosphates are<br />

also ineffective as dispersants in the presence of severe calcium and salt contamination.<br />

Under proper conditions phosphate fluids offer good rheological properties at a minimum cost.<br />

Caustic Soda is normally added for pH maintenance. Small quantities of tannin-type dispersants<br />

may further enhance deflocculation of the system. MILGEL ® is added periodically to improve<br />

filter cake and to reduce filtrate.<br />

Tannin and Lignin <strong>Fluids</strong><br />

Additives rich in tannin, namely quebracho, were commonly employed as thinners prior to the<br />

advent of lignosulfonate. The material is derived from the quebracho tree and normally has a pH<br />

of 3.8.<br />

Most quebracho products are a quebracho extract blend. These are used primarily as a thinner in<br />

freshwater drilling fluids for moderate depth wells. The product is unstable at temperatures<br />

above 240°F. It also loses its effectiveness in environments containing excess salt (6000 to 7000<br />

mg/L) or calcium ion (240 mg/L). The system can be maintained at a pH as low as 9.0, but it will<br />

tolerate more salt and calcium contamination at pH ranges of 10.5 to 11.5. When used as a thinner<br />

for freshwater fluids, 1 to 2 lbm/bbl of the material is normally required. When used with lime<br />

fluids, 2 to 4 lbm/bbl will be needed for initial conversion. For treatment of cement<br />

contamination in freshwater fluids, concentrations of 1 to 2 lbm/bbl are usually sufficient.<br />

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

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

Revised 2006 3-37

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