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Phase Envelope Calculator

Wilson K-values ยท SBV Mixing ยท GPSA 14th Ed

Phase Envelope Estimation Tool
Calculates phase envelope boundaries using Wilson K-value correlations and Stewart-Burkhardt-Voo (SBV) mixing rules. Estimates cricondenbar, cricondentherm, and dew/bubble points for pipeline and process design per Industry methodology.

Light Components (mol%)

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Heavy Components (mol%)

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Total: 100.0%

Operating Conditions

psig
ยฐF
Phase Envelope Basics:
โ€ข Cricondenbar: Maximum P for two-phase
โ€ข Cricondentherm: Maximum T for two-phase
โ€ข Dew Point: First liquid forms from gas
โ€ข Bubble Point: First gas forms from liquid

About This Calculator

Estimates phase envelope boundaries using Wilson K-value correlations with Stewart-Burkhardt-Voo (SBV) pseudo-critical mixing rules per Industry methodology.

Calculation Method:

  • K-values: Wilson correlation (1968)
  • Mixing: Kay's + SBV corrections
  • Properties: GPSA/GPA 2145 data

Key Applications:

  • Pipeline operating point verification
  • Separator inlet phase determination
  • Retrograde condensation assessment
  • Dense phase transport feasibility

Accuracy Note:

ยฑ5-10% for typical natural gas. Use process simulator (HYSYS, ProMax) with tuned EOS for detailed design.

Frequently Asked Questions

What is a phase envelope for natural gas?

A phase envelope is a pressure-temperature diagram showing the boundary between single-phase and two-phase regions for a gas mixture. It defines the dew point curve (first liquid forms), bubble point curve (first vapor forms), cricondenbar (maximum two-phase pressure), and cricondentherm (maximum two-phase temperature).

What is retrograde condensation in natural gas pipelines?

Retrograde condensation occurs when a gas mixture forms liquid as pressure decreases, which is opposite to normal behavior. This happens between the cricondentherm and the critical point on the phase envelope, and is a key concern for pipeline operations and separator design.

What are Wilson K-values used for in phase envelope calculations?

Wilson K-values are equilibrium ratios that estimate vapor-liquid distribution of each component based on its critical properties and acentric factor. They provide a rapid approximation of dew and bubble points without requiring a full equation of state calculation.

How accurate is the Wilson K-value phase envelope estimation?

Wilson K-value correlations with SBV mixing rules provide ยฑ5-10% accuracy for typical natural gas compositions. For detailed design, a process simulator with a tuned equation of state such as Peng-Robinson or SRK should be used.