DIERS Omega Two-Phase Relief — Engineering Fundamentals

Why single-phase sizing fails for flashing relief, Leung's Omega closed-form, choked vs subcritical regime.

1. When two-phase matters

API 520 single-phase sizing assumes either pure gas (compressible critical flow) or pure liquid (Bernoulli). Relief from a saturated liquid system flashes inside the valve nozzle — the working fluid is two-phase by the time it reaches the throat. Single-phase gas sizing under-predicts the required area (treats it as gas-only); single-phase liquid over-predicts because it ignores the vapor expansion.

DIERS (Design Institute for Emergency Relief Systems, AIChE 1976–1995) developed the rigorous two-phase model. Leung (1986) gave the closed-form Omega simplification that turns the iterative DIERS solution into a single equation.

2. The Omega parameter

For a saturated-liquid inlet:

ω = cp · To · Po · ((vg − vl) / hfg

ω captures the compressibility of the two-phase mixture during expansion through the nozzle:

  • ω < 0.1 — essentially incompressible (liquid-dominated). Use API 520 liquid sizing.
  • 0.1 ≤ ω ≤ 100 — DIERS Omega applies; use this calc.
  • ω > 100 — essentially gas-only. Use API 520 gas sizing.

3. Choked / subcritical

The critical pressure ratio ηc from Leung's fit:

ηc ≈ 0.55 + 0.217·ln(ω) − 0.046·(ln ω)² + 0.004·(ln ω)³

If backpressure P_b/P_o ≤ η_c → choked flow (mass flux = G_crit). Otherwise non-choked; G is reduced via a square-root subcritical correction.

Mass flux G then drives area via A = W/(3600·G·K_d), with K_d = 0.65 standard DIERS convention.

4. Common scenarios

ScenarioSystemω range
Runaway exotherm (BPC reactor)Liquid + light vapor1 – 10
Fire on liquid-full vesselSat. hydrocarbon0.5 – 5
Loss of cooling on refrigerated drumSat. propane / butane1 – 20
Power failure on cryogenic NGLNGL, low T5 – 50

5. References

  • DIERS Project Manual (CCPS / AIChE 1995). Two-Phase Relief and Vent Systems.
  • Leung, J.C. (1986). "A generalized correlation for one-component homogeneous equilibrium flashing choked flow." AIChE J. 32(10), 1743–1746.
  • API Std 520 Part I §A.3 — Two-phase sizing guidance.
  • Fauske, H.K. (1985). "Flashing flows or: some practical guidelines for emergency relief vent design." Plant Oper. Prog. 4(3), 132–134.

Size your PSV

→ Open Calculator