Tools

Practical calculators and utilities for engineering teams

25 tools found

Separator Preliminary Sizing

Process Engineering · Oil & Gas

Screening calculation for preliminary vessel dimensions and operating checks.

Preliminary engineering only
Unsaved session

Project information

Load example:

Service

Operating conditions

Gas flow and properties

Density priority: manual ρ wins; else ρ from P/T/Z/MW. >3% mismatch warns.

If both standard flow and actual flow are entered, they are cross-checked (>5% warns).

Suggested K: 0.32 ft/s
Recommended droplet: 150 µm — Bulk gas–liquid separation with inlet device + mist extractor; ~150 µm typical.

Standards reference (API 12J / GPSA Section 7 — Separation Equipment): conventional separator with mist extractor ≈ 150 µm; bulk knock-out (KOD) without fine mist removal ≈ 250–500 µm; scrubber upstream of rotating equipment ≤ 100 µm. Mist extractor removes droplets down to ~10 µm. Verify against project criteria / vendor.

Informational only — does not change the calculation (edit K directly).

Liquid data

Design constraints

Informational only — does not change the calculation (edit K directly).

Typical K screening defaults (not project criteria)

horizontalno mist0.2 ft/s0.15–0.25
horizontalmist0.32 ft/s0.25–0.40
verticalno mist0.15 ft/s0.10–0.20
verticalmist0.27 ft/s0.20–0.35

Recommended preliminary separator

Internal diameter (in)

54.0

Tangent-to-tangent length (ft)

19.0

L/D

4.22

Gross vessel volume (ft³)

302.2

Gas disengagement area (ft²)

7.95

Gas velocity (ft/s)

1.706

% of allowable: 82.6%

Allowable gas velocity (ft/s)

2.066

Required liquid volume (ft³)

139.0

Available liquid volume: 151.1 ft³

Calculated retention time (min)

7.75

InletGas outWater outCondensate outD = 54.0 inL_tt = 19.0 ft
GasCondensateWater

3D preview

Parametric preview from sizing results — not a fabrication model.

Checks

Gas capacityPass
Gas velocity vs allowablePass
Liquid retentionPass
L/D ratioPass
Max lengthPass
Three-phase L-L settlingNot calculated

Warnings

  • L-L settling: Not calculated — verify Stokes/project criteria / vendor.
  • This tool does not size inlet devices, mist extractors, level controls, relief devices, nozzles, internals, wall thickness, supports, or ASME mechanical design.

Preliminary screening tool only. Results must be verified against the applicable project design basis, fluid characterization, process simulation, applicable codes and standards, and vendor/manufacturer requirements. This tool is not suitable for final mechanical, safety, relief, internals, nozzle, control valve, or guaranteed separation design.

Souders–Brown screening consistent with common oil & gas practice; not a certified API 12J / GPSA compliance calculator.

Calculation details

Method: Souders–Brown gas-capacity screening + liquid retention holdup. Preliminary, deterministic. US Customary units (engine works in canonical SI).

V_max = K · √((ρL − ρg)/ρg) = 0.6298 m/s (ρL=768.886 kg/m³, ρg=18.0076 kg/m³)

ρg source: calc from P/T/Z/MW (calc=18.0076 kg/m³)

Method (horizontal): vapor area A_vap = A_total − A_liquid_segment (fill=50% of D); gas capacity = A_vap · V_max

Horizontal gas capacity uses vapor cross-section only (length-independent); length is set by liquid holdup.

Liquid holdup V_req = Q_liq · t_ret · surge = 3.936 m³; L_tt = V_req / A_liquid_segment

Three-phase holdups: V_cond = 1.905 m³, V_water = 2.032 m³ (separate)

Rounded: D = 1.372 m, L_tt = 5.791 m (margin 5% applied to holdup length)

Final: A_diseng = 0.7388 m², V_gas = 0.5199 m/s = 82.6% of allowable

Liquid retention: required 3.936 m³ vs available 4.278 m³ → 7.75 min

Candidate scan (first 5): D=0.61m, D=0.76m, D=0.91m, D=1.07m, D=1.22m

Horizontal and vertical use distinct area/volume equations (vapor segment vs full cross-section). Three-phase holdups are computed separately; liquid–liquid settling is not resolved here.

Illustrative only — verify against project criteria.

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