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STANDARD HANDBOOK OF PETROLEUM & NATURAL GAS ...

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714 Drilling and Well Completions<br />

Table 4-69<br />

Fluid Density Adjustment for Downhole Temperature Effect [26]<br />

Surfacemeasured density<br />

Loss in density per 100°F<br />

rise in average circulating<br />

temperature above surfacemeasured<br />

temperature<br />

Iblgal SP gr iblgai SP gr<br />

8.5 1.020 0.35 0.042<br />

9 1.080 0.29 0.035<br />

10 1.201 0.26 0.031<br />

11 1.321 0.23 0.028<br />

12 1.441 0.20 0.024<br />

13 1.561 0.16 0.019<br />

14 1.681 0.13 0.016<br />

15 1.801 0.12 0.014<br />

Courtesy Baroid Drilling Fluids, Inc.<br />

+60<br />

+40<br />

u"<br />

5 +20<br />

G<br />

CI:<br />

w<br />

a<br />

o<br />

2<br />

p -20<br />

-40<br />

-60<br />

8 9 10 11 12 13 14 l!<br />

DENSITY, ppg<br />

Figure 4-125. Crystallization temperature of various brines [37].<br />

Weight materials commonly used in completion fluids are given in Table 4-70.<br />

Although they add solid particles to the fluid, their use can be economical where<br />

densities exceed 11 .O lb/bbl.<br />

Oil-Base Systems. Oil-base completion and workover fluids contain oil as the<br />

continuous phase. Their application is limited by their density to formations with

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