SC DrillTechSC DrillTechSOLIDS CONTROL · DWM← Main site
Calculators
Live field tools

Solids-control & drilling-fluid calculators

Six calculators a field engineer actually reaches for — running live in your browser, free, no sign-up. Each one shows the formula and the standard behind it, so you can see exactly where the number comes from. Measured, not guessed.

Shaker · API RP 13C

Shale shaker G-force calculator

Enter the basket stroke and speed to get the G-force the deck is actually developing. Most decks target 4–8 G; below that, conveyance and screen life suffer.
in
rpm
0 G
G-force developed at the basket
Formula & reference
G = RPM² × stroke(in) ÷ 70,400 (stroke = total throw; mm ÷ 25.4 → in)
Standard vibratory-screen relation; target 4–8 G typical for linear-motion shakers per OEM/API RP 13C practice. Confirm the OEM rating for your specific deck.
Mud system · Cost control

Dilution to control low-gravity solids

How many barrels of clean fluid you'd need to bring the low-gravity-solids (LGS) fraction down — when the solids-control equipment isn't doing it.
bbl
% vol
% vol
0 bbl
clean fluid (dilution) to reach target LGS
Formula & reference
V_dilution = V_system × (LGS_current − LGS_target) ÷ LGS_target (assumes dilution fluid carries ~0% solids)
Mass-balance dilution relation (API RP 13C / SPE solids-control practice). Whole-mud dilution then needs weight-up — see the barite calculator. Equipment removal is always cheaper than dilution.
Mud weight · API 13B

Barite to increase mud weight

Pounds and sacks of barite per barrel to raise mud density, plus the volume increase it creates. Barite SG 4.2 (35.0 ppg).
ppg
ppg
bbl
0 sacks
barite (100-lb sacks) for the whole system
Formula & reference
lb/bbl = 1470 × (W₂ − W₁) ÷ (35.0 − W₂) Volume gain (bbl/bbl) = (W₂ − W₁) ÷ (35.0 − W₂) Sacks = total lb ÷ 100
API 13B weight-up relation, barite SG 4.2 → 35.0 ppg. W in ppg. Volume gain dilutes other properties — re-check rheology and chemistry after weight-up.
Hydrocyclones · Performance

Hydrocyclone feed head

Desanders and desilters are designed around a feed head — not just a pressure. Enter manifold pressure and mud weight to see the head you're actually feeding. Target ≈ 75 ft.
psi
ppg
0 ft
feed head delivered to the cones
Formula & reference
Head(ft) = P(psi) ÷ (0.052 × MW(ppg)) Target operating head ≈ 75 ft (desander & desilter)
Hydrocyclones are head-driven devices; OEMs specify ~75 ft of feed head for correct cut. Too low → poor separation; too high → premature cone wear. Verify against your cone OEM curve.
Hydraulics · Transport

Line & annular velocity

Fluid velocity in a transfer line or in the annulus. Annular velocity must beat cuttings slip velocity to lift solids; transfer lines have their own erosion/settling windows.
gpm
in
0 ft/min
line velocity
Formula & reference
Line: v(ft/min) = 24.51 × Q(gpm) ÷ ID²(in) Annulus: v(ft/min) = 24.51 × Q(gpm) ÷ (D_hole² − D_pipe²) ft/s = ft/min ÷ 60
Standard field hydraulics relations. Annular velocity must exceed cuttings slip velocity (commonly ~100–120 ft/min minimum) for effective hole cleaning; slip velocity itself depends on rheology and cutting size.
Shaker screens · API RP 13C

Shaker screen cut-point

Pick an API screen designation to see its separation cut-point and what it removes — and where you start losing barite. Finer than ~API 200 begins taking weighting material out.
75 µm
approximate D100 separation cut-point
API No.Cut-pointRemoves
API 40420 µmCoarse — gravel/large cuttings
API 60250 µmCoarse sand
API 80180 µmMedium sand
API 100150 µmMedium sand
API 120125 µmFine sand
API 140106 µmFine sand
API 17090 µmVery fine sand
API 20075 µmCoarse silt / barite-friendly
API 23063 µmSilt
API 27053 µmFine silt
API 32545 µmFine silt — barite recovery limit
Formula & reference
API RP 13C screen designation ↔ d100 separation potential (microns). Barite median ≈ 10–75 µm → screens finer than ~API 200 start removing barite.
API RP 13C (ISO 13501) screen labelling. Cut-points are nominal separation potentials; actual performance depends on G-force, conveyance, mud rheology and screen condition.

These calculators are field aids for quick checks and decisions, not a substitute for a full engineering review. Results depend on the inputs you give and on assumptions noted under each tool. For anything load-bearing — a weight-up programme, a dilution plan, a hydrocyclone or shaker set-up on a live well — have it validated against your actual fluid, equipment and well conditions.

Numbers point one way — your rig may be another

These tools tell you what the formulas say. A field evaluation tells you what your shakers, hydrocyclones, centrifuge and mud system are actually doing — and what to change. That's the engineering.

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