Simple Engineering Calculators

Screw Compressor — Natural Gas Throughput

Positive-displacement screw-compressor performance estimator for the Frick TDS line and the Kobelco KS gas screws. Gas density via the Sutton + Dranchuk-Abou-Kassem real-gas method. Everything updates live as you change inputs.

Throughput

Standard flow
9.12MMSCFD

Referenced to 14.696 psia, 60 °F (the engine's standard state)

Mass flow
18,903lb/hr
Actual inlet flow
1,455ACFM

Real gas volume drawn in at suction

Pressure ratio
3.32: 1

Power & discharge

Estimated brake power
603BHP
Adiabatic gas power
561HP

Thermodynamic minimum at perfect Vᵢ match

HP per MMSCFD
66.1
Dry discharge temp
224°F

Dry adiabatic reference — oil flooding keeps the real discharge 170–185 °F

Operating limits — TDSH 233XL
LimitValueBasis
Max dry discharge temp230 °Ftypical practice
Max pressure ratio7 : 1typical practice
Min differential (ΔP)30 psigtypical practice
Compressor casing rating400 psigcasing rating

Generic oil-flooded screw limits are rules of thumb; casing, MAWP and package figures come from the sources shown under the model picker.

Capacity curve

Standard flow (MMSCFD)

0.03.26.39.5136001,5752,5503,5254,500Drive speed (RPM)MMSCFD

Estimated brake power (BHP)

0.02094186278366001,5752,5503,5254,500Drive speed (RPM)Brake BHP
Show the full calculation & assumptions

Machine — TDSH 233XL, swept volume 0.45580 ft³/rev

  • Displacement = swept × RPM × load = 0.45580 × 3550 × 100% = 1,618 ACFM (theoretical)
  • × volumetric efficiency 0.899 = 1,455 ACFM actually drawn in

Gas at suction (64.7 psia, 70 °F)

  • Specific gravity 0.65 → molar mass 18.83 lb/lbmol, k = 1.270
  • Compressibility Z = 0.9894 → density 0.2166 lb/ft³

Throughput

  • Mass flow = 1,455 ACFM × 0.2166 lb/ft³ × 60 min/hr = 18,903 lb/hr
  • ÷ standard density 0.04974 lb/ft³ = 6,334 SCFM = 9.12 MMSCFD

Power (built-in Vᵢ = 2.57, mech. eff 0.93)

  • Adiabatic (min) 561 HP · indicated 561 HP · brake 603 HP

Rough estimate. Volumetric efficiency is the dominant uncertainty (±5% → ±5% on flow). For a guaranteed selection, confirm against Frick CoolWare.

Read before you rely on these numbers

  • This is a rough estimate, not a guaranteed compressor selection.
  • Volumetric efficiency is the dominant assumption (±5% → ±5% on flow). Override it with a manufacturer value when you have one.
  • The discharge temperature shown is the dry adiabatic reference; oil flooding keeps the real gas discharge much lower (~170–185 °F target).
  • Geometry source per machine is shown under the model picker (Frick: service manual 070.250-IOM1 Table 2; Kobelco: see the provenance note for how the figure was derived).