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BAKER HUGHES - Drilling Fluids Reference Manual

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MECHANICAL SOLIDS CONTROL<br />

Desilters are hydroclones which are normally 4 in. in diameter and will process 50 to 80 gal of<br />

fluid per minute per cone depending on manufacturer. Feed head requirements range from 75 to 96<br />

ft with the most common requirement being 75 ft. Desilters with a spray discharge will make a 16-<br />

to 18-micron median cut on low-gravity solids. A sufficient number of cones should be provided to<br />

process 1.25 to 1.5 times the circulating rate for maximum efficiency.<br />

It is most important that desilters be employed at the start of an operation and run almost<br />

continuously until a weighted drilling fluid is required. If desilting is delayed or utilized only parttime,<br />

the recycled drilled solids will rapidly degrade into particle sizes too small to be removed by<br />

the desilter.<br />

The general operating parameters for hydrocyclones is presented in Table 10 – 4 as follows:<br />

Press<br />

(psi)<br />

2" 4" 6" 12"<br />

Head Vol Press Head Vol Press Head Vol Press Head<br />

(ft) (gpm) (psi) (ft) (gpm) (psi) (ft) (gpm) (psi) (ft)<br />

Vol<br />

(gpm)<br />

35 75 20 35 75 60 35 75 100 35 75 500<br />

Table 10 - 4 Recommended Hydrocyclone Feed Head Requirements (Pressures based<br />

on 9 lbm/gal fluid)<br />

The quantity of solids removed from an unweighted system by a hydrocyclone can be calculated as<br />

follows.<br />

W S = 97(D μ – 8.33)(Q µ )<br />

where,<br />

Ws = lb solids removed per hour per cone<br />

Dµ= density of underflow, lb m /gal<br />

Qµ = underflow rate, gal/min.<br />

Smaller diameter hydrocyclones (usually 2 inches in diameter) have been used for barite salvage.<br />

Under ideal conditions, these cones will make a D-50 cut on barite in the 4- to 6-micron range and<br />

a 7- to 10-micron out on low-gravity solids. Barite recovery efficiency is less than that obtained<br />

with a centrifuge which should give D-95 cut in the 4- to 6-micro range.<br />

Figure 10-4 illustrates approximate performance curves for various diameter hydrocyclones. These<br />

curves are for low-gravity solids in unweighted drilling fluids.<br />

<strong>BAKER</strong> <strong>HUGHES</strong> DRILLING FLUIDS<br />

REVISION 2006 10-13<br />

REFERENCE MANUAL

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