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.

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

Time<br />

The calculation of filtrate loss at variable time intervals relative to known filtrate loss and time<br />

interval can be predicted by the following equation:<br />

where,<br />

f 1<br />

T 1<br />

= f × ---------<br />

T<br />

f = known filtrate at a time interval of T<br />

f l = unknown filtrate at a time interval of T 1<br />

For example, if fluid loss is 8.0 mL in 15 minutes, the predicted fluid loss in 30 minutes would be,<br />

f 1 = 8 ---------<br />

30<br />

8<br />

5.48<br />

× = × --------- = 11.3 m L<br />

15 3.87<br />

or if time is doubled, filtrate theoretically would be increased by 41%. It should be noted that the<br />

above equation would apply only under conditions where pressure, filtrate viscosity, and cake<br />

permeability remained constant and no changes in chemical contents occurred due to effect of<br />

temperature and/or flocculation.<br />

Summary<br />

Filtration rate is often the most important property of a drilling fluid, particularly when drilling<br />

permeable formations where the hydrostatic pressure exceeds the formation pressure. Proper control<br />

of filtration can prevent or minimize wall sticking and drag, and in some areas improve borehole<br />

stability. Filtration control poses a question that should be answered only after a thorough study is<br />

made based on past experience, predicted pressure differentials, lithology, formation protection<br />

requirements, and overall economics.<br />

Solids<br />

Quantity, type, and size of suspended solids in a drilling fluid is of primary concern in the control of<br />

rheological and filtration properties. Solids in a drilling fluid are comprised of varying quantities of<br />

weighting materials [MIL-BAR ® , DENSIMIX ® , and/or W.O. 30 (Calcium Carbonate)], commercial<br />

bentonite, drilled solids (sand and shale) and, in some cases, loss of circulation additives. Material<br />

balance equations help differentiate high-specific gravity solids from low-specific gravity solids when<br />

the total solids content is obtained from the retort. These materials balance equations are presented in<br />

Chapter 10, Mechanical Solids Control.<br />

Typically, the only high-specific gravity solid in a drilling fluid is the weight material, MIL-BAR ® ,<br />

ORIMATITA ® or DENSIMIX ®. However, low-specific gravity solids are defined as all other solids<br />

except weight material. Low-gravity solids are comprised primarily of MILGEL ® , drilled solids and,<br />

in some cases, treatment chemicals. In the analysis of low-gravity solids, it will be assumed that any<br />

contribution from treatment chemicals is negligible. Therefore, the analysis of low-gravity solids<br />

distinguishes between the quantity of commercial bentonite added to a drilling fluid and the quantity<br />

of drilled solids incorporated into a drilling fluid.<br />

ADVANTAGE performs solids analysis based on the retort and titration results. If barite is not being<br />

used then the default value for the weight material should be changed to the appropriate density.<br />

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

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

Revised 2006 1-25

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

Saved successfully!

Ooh no, something went wrong!