PVT Properties Overview

Introduction

PVT (Pressure-Volume-Temperature) properties describe how reservoir fluids behave under changing conditions. Accurate PVT data is essential for:

  • Reservoir simulation — fluid flow and recovery calculations
  • Material balance — reserves estimation
  • Well performance — inflow and outflow analysis
  • Facilities design — separator and pipeline sizing
  • Production forecasting — rate predictions

When laboratory PVT measurements are unavailable, engineers rely on empirical correlations developed from measured datasets.

Correlation Philosophy

Regional Basis

Most PVT correlations were developed from specific geographic datasets:

Region Typical Crude Type Representative Correlations
California Light, low-sulfur Standing (1947)
North Sea Light to medium, waxy Glasø (1980)
Middle East Medium, sulfur Al-Marhoun (1988)
Gulf of Mexico Variable Vasquez-Beggs (1980), Petrosky-Farshad (1993)
Deepwater GOM Light, high GOR Dindoruk-Christman (2004)
UAE Medium Dokla-Osman (1992)

Best Practice: Use correlations developed from oils similar to your reservoir.

Calibration Strategy

When some laboratory data is available:

  1. Tune correlations to match measured points
  2. Validate consistency across related properties
  3. Use measured values at calibration points, correlations elsewhere

PVT Property Relationships

The Black Oil Model

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Property Interdependencies

Property Depends On Used By
PbP_b (Bubble Point) RsR_s, γg\gamma_g, γAPI\gamma_{API}, TT BoB_o, μo\mu_o, coc_o at PbP_b
RsR_s (Solution GOR) PP, TT, γg\gamma_g, γAPI\gamma_{API} BoB_o, μo\mu_o
BoB_o (Formation Volume) RsR_s, TT, γg\gamma_g, γo\gamma_o Material balance, flow calculations
μo\mu_o (Viscosity) Stage: μodμobμo\mu_{od} \to \mu_{ob} \to \mu_o Flow calculations, mobility
coc_o (Compressibility) PP relative to PbP_b Material balance, PTA

Correlation Selection Guide

By Property

Bubble Point Pressure (PbP_b)

Oil Type First Choice Alternative
Light California Standing Glasø
North Sea Glasø Standing
Middle East Al-Marhoun Vasquez-Beggs
Gulf of Mexico Petrosky-Farshad Vasquez-Beggs
Deepwater/High GOR Dindoruk-Christman -
UAE Dokla-Osman Al-Marhoun
General purpose Vasquez-Beggs Standing

📖 Full Documentation: Bubble Point Correlations


Solution Gas-Oil Ratio (RsR_s)

Same regional preferences as bubble point — the correlations are mathematically related (inverses of each other).

📖 Full Documentation: Solution GOR Correlations


Oil Formation Volume Factor (BoB_o)

Condition Correlation Notes
Saturated (PPbP \le P_b) Match RsR_s correlation Use same author for consistency
Undersaturated (P>PbP > P_b) From BobB_{ob} and coc_o Bo=Bobexp[co(PPb)]B_o = B_{ob} \exp[-c_o(P - P_b)]

📖 Full Documentation: Oil Formation Volume Factor


Oil Viscosity (μo\mu_o)

Three-stage calculation:

Stage Function Correlation
1. Dead oil (μod\mu_{od}) f(γAPI,T)f(\gamma_{API}, T) Egbogah (1983)
2. Saturated (μo\mu_o, PPbP \le P_b) f(μod,Rs)f(\mu_{od}, R_s) Beggs-Robinson (1975)
3. Undersaturated (μo\mu_o, P>PbP > P_b) f(μob,P,Pb)f(\mu_{ob}, P, P_b) Vasquez-Beggs (1980)

📖 Full Documentation: Oil Viscosity Correlations


Oil Compressibility (coc_o)

Condition Correlation Typical Values
Undersaturated (P>PbP > P_b) Vasquez-Beggs (1980) 10-30 × 10⁻⁶ 1/psi
Saturated (PPbP \le P_b) Villena-Lanzi (1985) 50-200 × 10⁻⁶ 1/psi

📖 Full Documentation: Oil Compressibility Correlations


Calculation Workflow

Complete Oil PVT at Any Pressure

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Statistical Performance Guidelines

Expected Accuracy

Property AARE Range Best Achievable
PbP_b 5-15% < 5% with tuning
RsR_s 5-12% < 5% with tuning
BoB_o 1-5% < 2% with tuning
μo\mu_o 10-25% 5-10% with tuning
coc_o 15-30% 10-15% with tuning

When Correlations Fail

Symptom Likely Cause Solution
PbP_b off by > 20% Wrong correlation for oil type Try regional correlation
BoB_o too high/low Inconsistent RsR_s and BoB_o Use matched pair
μo\mu_o unrealistic Dead oil viscosity wrong Check API gravity input
Non-physical values Outside correlation range Check input ranges

Available Property Documentation

Oil Properties

Property Functions Documentation
Bubble Point 7 correlations Bubble Point
Solution GOR 6 correlations Solution GOR
Formation Volume Factor 7+ correlations Formation Volume Factor
Viscosity 3-stage Oil Viscosity
Compressibility 2 correlations Oil Compressibility

Gas Properties (Reference materials needed)

  • Z-factor correlations
  • Gas viscosity
  • Gas density

Water Properties (Reference materials needed)

  • Water formation volume factor
  • Water compressibility
  • Water viscosity

Best Practices

Consistency Checks

  1. BoB_o at PbP_b should be maximum value
  2. μo\mu_o at PbP_b should be minimum value
  3. Rs=RsbR_s = R_{sb} for all PPbP \ge P_b
  4. BoB_o decreases for P>PbP > P_b (undersaturated)
  5. BoB_o decreases for P<PbP < P_b (saturated, as gas evolves)

Input Validation

Parameter Typical Range Check
γg\gamma_g 0.55 - 1.5 Air = 1.0, methane ≈ 0.55
γAPI\gamma_{API} 10 - 60 Water = 10, very light > 40
RsR_s 0 - 3000 scf/STB Higher = more volatile
TT 60 - 350 °F Reservoir temperature
PbP_b 100 - 10000 psia Must be < initial pressure

Oil Properties

Gas Properties

Water Properties

Other Properties

Supporting Functions


References

  1. McCain, W.D. Jr. (1990). The Properties of Petroleum Fluids, 2nd Edition. PennWell Books.

  2. Ahmed, T. (2019). Reservoir Engineering Handbook, 5th Edition. Gulf Professional Publishing.

  3. Whitson, C.H. and Brulé, M.R. (2000). Phase Behavior. SPE Monograph Vol. 20.

  4. Standing, M.B. (1981). Volumetric and Phase Behavior of Oil Field Hydrocarbon Systems, 9th Edition. Society of Petroleum Engineers.

  5. Danesh, A. (1998). PVT and Phase Behaviour of Petroleum Reservoir Fluids. Elsevier.

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