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Live calculators · API RP 13C

The numbers that
decide the well.

The same relationships built into our tool kits and remote evaluations — run them live, get the band you're in, and know what to do next. Works on the rig, online or off.

Removal efficiency η Cyclone head Centrifuge G Dilution cost Screen selection
01 · EFFICIENCY

Drilled-solids removal efficiency (η)

Current API RP 13C SRE compares drilled-solids volume removed with excavated hole volume over the same interval. Use a consistent volume basis and assess mud-to-cuttings ratio (MCR) alongside SRE; wet discard volume is not drilled-solids volume.

Inputs

bbl
bbl
SRE (%) = 100 × Vremoved / Vhole
Vhole is excavated hole volume. Measure Vremoved separately from retained liquid and weighting material. Vremoved exceeding hole volume requires a balance review; the coloured bands are illustrative, not API acceptance limits.

Removal efficiency

0
% η
—
050 · reference70 · reference100
Knowing η is step one. The SC DrillTech Doctor toolkit shows you why it's dropping — and runs the what-if before you ever touch the rig.
02 · HYDROCYCLONES

Hydrocyclone feed head

Cone separation depends on geometry, feed pressure/head, flow and fluid properties. Calculate head from pressure and density, then compare the measured duty with the OEM operating range; head alone does not establish cut size or separation efficiency.

Inputs

psi
ppg
h = 19.2 × p ÷ ρ
Some OEM cones are rated at 75 ft head; use the specified design range for the actual cone. Verify pressure, density, flow, piping and wear before assigning a fault.

Feed head

0
ft of head
—
06075 · reference120 ft
One bank, many machines. The RIG-EVAL forms walk every unit on the train — shakers, desander, desilter, centrifuge — tour by tour.
03 · CENTRIFUGE

Decanter bowl G-force

Bowl acceleration is one operating variable. Barite recovery, fines separation and dewatering depend on fluid properties, feed rate, pond depth, differential speed and actual discharge routing; speed alone cannot define the duty.

Inputs

rpm
in
G = N² × s ÷ 70,414
Decide the duty first, then set the machine. Feed rate and pond depth also move the cut point — bowl speed is the headline lever, not the only one.

Relative G-force

0
× g
—
01500 · reference30004500 g
Set every machine to its duty across the whole train. The Doctor toolkit links centrifuge, cyclones and shakers into one connected picture.
04 · ECONOMICS

Dilution cost saver

Solids-control losses are invisible because the system never stops running — the dilution rate just sits quietly higher than it should. Put a number on what restoring efficiency is worth over a section.

Inputs

bbl/d
bbl/d
days
$/bbl
saved = (now − target) × days × $/bbl

Modelled over the section

$0
illustrative gross fluid-cost difference
Current 0 bbl/d
Target 0 bbl/d
This is an illustrative cost model. A scoped evaluation can assess your baseline, practical options and intervention costs; the $48k example is not a documented field saving.
05 · METHOD

Shaker screen selector

Pick a screen by mesh alone and you're guessing. API RP 13C labels a screen through a defined screen-cloth test and conductance, not through field PSD alone. Tell us the section and fluid; get the cut-point priority, the trade-off to watch, and what to read on the deck.

Inputs

Use API screen designation and conductance with OEM guidance, measured flow and fluid properties. Deck appearance alone does not verify separation.

Recommendation

Watch on the deck
    This is the quick read. The RIG-EVAL shaker form records it tour-by-tour — screens, beach, conductance — your daily companion on the deck.
    Take it to the rig

    One number is the symptom. The system is the fix.

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