Straight and Stepped Labyrinth Seal Leakage Calculator

Estimate steady ideal-gas leakage through straight-through or stepped labyrinth seals using pressure, gas properties, fin count and annular clearance.

Seal and gas inputs

kPa absolute

Optimol

kPa absolute; below p₀

K

Rtec

J/(kg·K); 287 for dry air

used for choking warning

Falex

integer count

mm², total flow area

Predicted gas leakage
—
kg/s
Mass flow— g/s
Pressure ratio, r—
Critical ratio—
Area used— m²
Mass-flow function—
Coefficient product—

Enter valid inputs and calculate.

How to use

  1. Select Straight — Martin for a straight-through labyrinth or Stepped — Zimmermann–Wolff for a stepped geometry.
  2. Enter upstream total and downstream static pressures as absolute kPa, with downstream pressure below upstream pressure.
  3. Enter upstream total temperature in kelvin, the gas-specific constant, heat-capacity ratio and integer fin count.
  4. Enter clearance area directly in mm², or select diameter plus radial clearance to calculate the exact annular area. In stepped mode, also enter independently validated Cd and ks.
  5. Select Calculate to update leakage and diagnostics. Reset restores the air example and recalculates.
  6. Read mass flow first. Review pressure ratio, critical ratio, area and warnings; correct any red message before using a value.
  7. Do not use the model when real-gas, transient, rotating-cavity, heat-transfer, rub, eccentricity or safety-critical effects require a validated seal analysis or test.

Equations used

Definitions: p₀ is absolute upstream total pressure (Pa); pₙ is absolute downstream static pressure (Pa); T₀ is upstream total temperature (K); R is the specific gas constant (J/(kg·K)); n is the dimensionless integer fin count; A is annular flow area (m²); m is predicted mass flow (kg/s); r is the downstream-to-upstream absolute-pressure ratio (dimensionless); Q is the normalized mass-flow function (√K·s/m); rcrit is the ideal-gas critical pressure ratio (dimensionless); γ is the heat-capacity ratio (dimensionless); kₛ is the stepped-geometry correction (dimensionless); C_d is the discharge coefficient (dimensionless); Ainput is directly entered flow area (mm²); D is seal diameter (m); and c is radial clearance (m).

r = pₙ / p₀
A = Ainput × 10⁻⁶
A = (π/4)[(D + 2c)² − D²]
m = A p₀ √{(1 − r²) / [R T₀ (n − ln(r))]}

For stepped mode, the coefficient-explicit equation is:

m = kₛ C_d A p₀ √{(1 − r²) / [R T₀ (n − ln(r))]}
m_g/s = 1000m
Q = m√T₀/(A p₀)  ;  rcrit = [2/(γ + 1)]γ/(γ − 1)

Entered pressures in kPa are multiplied by 1000 before substitution. Geometry inputs D and c are entered in mm and multiplied by 10⁻³ before the exact-annulus equation. Positive mass flow is defined from upstream to downstream. The model assumes steady one-dimensional ideal-gas flow, constant T₀ and equal throttling stages. A ratio at or below rcrit triggers a warning but does not alter the cited empirical equation.

The stepped coefficients must represent the applicable clearance-to-land ratio, step height, pitch and flow regime. Published broad discharge-coefficient ranges are not a substitute for design-specific validation. This screening model excludes rotation, swirl, Reynolds corrections, heat transfer, real-gas behavior, rubs, eccentricity and transients.

References