15.03.2018 Views

BAKER HUGHES - Drilling Fluids Reference Manual

Create successful ePaper yourself

Turn your PDF publications into a flip-book with our unique Google optimized e-Paper software.

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

Figure 3-21<br />

Relative Inhibition of Tertiary Clay in KCl Solutions<br />

MIL-PAC LV – Low viscosity polyanionic cellulose will provide a degree of polymer<br />

encapsulation, but its principle function is in the control of the API filtrate. MIL-PAC LV as a<br />

filtration control agent will impart minimal viscosity to the system. Concentrations will vary with<br />

filtration rate desired and overall salinity of the fluid. Normally, a treatment level of 1.43 to 5.7<br />

kg/m 3 (0.5 to 2.0 lbm/bbl) will provide the desired results.<br />

MIL-PAC R – The regular grade polyanionic cellulose functions in a similar way to the low<br />

viscosity version but will also impart viscosity. The ratio of MIL-PAC R to MIL-PAC LV will<br />

control the degree of viscosity-to-filtrate control required. MIL-PAC R will impart a significant<br />

level of high shear viscosity, but minimal gel strength.<br />

Traditionally, the gel strengths in the system were provided in part by formation clays in a<br />

conventional polymer system while drilling in a reactive area. However, the high level of<br />

inhibition provided by AQUA-COL has led to minimal increase in gel strengths. On recent wells,<br />

the concentration of MIL-PAC R has been decreased in favor of XAN-PLEX D polymer.<br />

Improved hole cleaning is a direct result of this change. To reduce fluid loss or increase viscosity,<br />

1.43 to 5.7 kg/m 3 (0.5 to 2.0 lbm/bbl) is normally required.<br />

XAN-PLEX D– Xanthan gum used to increase viscosity and gel strengths, as well as to aid in<br />

suspending weight materials and cuttings. Normal treatment is 2.85 kg/m 3 (1.0 lbm/bbl) to<br />

achieve a funnel viscosity of 35 to 38 sec/qt.<br />

NEW-DRILL – This is a PHPA polymer supplied in fine powder form. The high molecular<br />

weight of this anionic polymer is designed to encapsulate and reduce drill cutting dispersal and<br />

swelling. Addition of a PHPA polymer is a preventative measure and not a cure for high solids<br />

induced mud rheological properties. If PHPA polymer is added to a system that is solids laden,<br />

this will result in excessive viscosities. NEW-DRILL additions to new polymer fluid will result in<br />

a viscosity hump, therefore, allow a minimum of four (preferably eight) hours mixing time. If the<br />

drill-out formation is a clay, then it is recommended that a minimum of half the NEW-DRILL<br />

concentration be added prior to displacement. The level of NEW-DRILL in the system can be<br />

monitored using the Clapper Gas Train test. While this provides only approximate values, it will<br />

clearly indicate an excess of the polymer in the system. A minimum excess of 1.0 lbm/bbl is<br />

recommended.<br />

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

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

3-84 Revised 2006

Hooray! Your file is uploaded and ready to be published.

Saved successfully!

Ooh no, something went wrong!