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 />

of addition of deflocculant and caustic soda should be increased along with an increase in<br />

water dilution.<br />

5. The API Filtrate is normally controlled with starch and/or CMC. Periodic additions of<br />

MILGEL ® normally should be accompanied by treatments with a deflocculant.<br />

6. After all chemicals have been added to the fluid system, a check should be made of fluid<br />

properties. Minor adjustments can then be made on subsequent circulations with<br />

additional lime, UNI-CAL ® , caustic, and a fluid loss control agent such as MIL-PAC ® .<br />

7. The addition of lime and MILSTARCH ® , BIO-LOSE ® , BIO-PAQ ® or CMC<br />

simultaneously through the hopper should be avoided because of drastic viscosity<br />

increases.<br />

8. Typical fluid properties after conversion and before weight-up are as follows.<br />

Table 3-12<br />

Typical Fluid Properties after Conversion and Before Weight-up<br />

Fluid Weight<br />

10.0 lbm/gal<br />

Funnel Viscosity<br />

40 to 44 sec/qt<br />

Plastic Viscosity<br />

18 cP<br />

Yield Point 6 lb f /100 ft 2<br />

Gels 0/0 lb f /100 ft 2<br />

API Filtrate<br />

6 to 12 cc/30 min<br />

Calcium<br />

75 to 200 mg/L<br />

pH 11.5 to 12.0<br />

Pf<br />

1.0 to 2.0 ml<br />

Pm<br />

5.0 to 10.0 ml<br />

Excess Lime<br />

1.0 to 2.0 lbm/bbl (low<br />

lime)<br />

9. Occasionally, it is necessary to convert weighted fluids when dilution is not practical. In<br />

this case, the fluid can be converted in the surface pits and displaced down the hole in<br />

stages.<br />

Maintenance of Lime <strong>Fluids</strong><br />

1. Lime fluid properties to be maintained should be determined and recorded; i.e., low-lime,<br />

moderate-lime, or high-lime properties.<br />

2. The P f and excess lime should be adjusted and maintained at near equal values. Low<br />

excess lime with high P f or high excess lime with low P f tends to cause rheological<br />

difficulties, i.e. the concentration of soluble calcium from lime is a function of pH, the<br />

higher the pH the less soluble.<br />

3. Caustic soda should be added to adjust the P f . The alkalinity of the filtrate affects the<br />

solubility of added lime. As the filtrate alkalinity approaches 1.0 ml, the solubility of lime<br />

decreases rapidly. After the 1.0 ml level is reached, solubility is only slightly affected.<br />

Normal additions of lime to the fluid will maintain the alkalinity of the fluid and the<br />

filtrate so that only small portions of caustic soda are required to maintain the desired<br />

alkalinity level in the filtrate.<br />

4. Lime is added to maintain the desired P m which controls the amount of excess lime.<br />

Excess lime can be calculated by the formula.<br />

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

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

Revised 2006 3-41

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

Saved successfully!

Ooh no, something went wrong!