Introduction & Context

A steam-jet ejector is a static device that uses high-pressure motive steam to create a low-pressure region (vacuum) and simultaneously compress the evacuated gas to a higher, still-sub-atmospheric pressure. The calculation below sizes the ejector by predicting the mass of motive steam required to entrain and compress a given suction load. It is a rapid screening tool for:

  • vacuum distillation, crystallisation and drying columns;
  • flash-cooling or solvent recovery systems;
  • barometric condensers and turbine condenser air-removal sections.

The result flags whether a single-stage ejector is thermodynamically feasible or whether a multi-stage (or booster) arrangement is required.

Methodology & Formulas

  1. Unit consistency
    Suction pressure is converted from mbar to bar to match the other pressures: \[ P_{\text{s}} = \frac{P_{\text{s,mbar}}}{1000} \]
  2. Compression ratio
    The ratio of discharge to suction absolute pressures defines the duty: \[ \text{CR} = \frac{P_{\text{d}}}{P_{\text{s}}} \]
  3. Entrainment ratio
    An empirical correlation (valid for 1.2 ≤ CR ≤ 12) gives the mass of gas entrained per mass of motive steam: \[ \text{ER} = 0.75 - 0.25 \ln(\text{CR}) \] The required motive steam flow is then: \[ \dot{m}_{\text{m}} = \frac{\dot{m}_{\text{s}}}{\text{ER}} \]
  4. Stage limit
    The highest suction pressure at which a single-stage ejector can operate against the specified discharge pressure is estimated from: \[ P_{\text{s}}^{*} = 0.18 \; P_{\text{m}}^{0.95} \] If the actual suction pressure \( P_{\text{s}} \) is below this critical value, a single-stage device is adequate; otherwise a booster or multi-stage system is required.
Correlation limits
Parameter Lower bound Upper bound
Compression ratio CR 1.2 12
Motive steam pressure \( P_{\text{m}} \) 3 bar a 15 bar a