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:
- Tune correlations to match measured points
- Validate consistency across related properties
- Use measured values at calibration points, correlations elsewhere
PVT Property Relationships
The Black Oil Model
Property Interdependencies
| Property | Depends On | Used By |
|---|---|---|
| (Bubble Point) | , , , | , , at |
| (Solution GOR) | , , , | , |
| (Formation Volume) | , , , | Material balance, flow calculations |
| (Viscosity) | Stage: | Flow calculations, mobility |
| (Compressibility) | relative to | Material balance, PTA |
Correlation Selection Guide
By Property
Bubble Point Pressure ()
| 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 ()
Same regional preferences as bubble point — the correlations are mathematically related (inverses of each other).
📖 Full Documentation: Solution GOR Correlations
Oil Formation Volume Factor ()
| Condition | Correlation | Notes |
|---|---|---|
| Saturated () | Match correlation | Use same author for consistency |
| Undersaturated () | From and |
📖 Full Documentation: Oil Formation Volume Factor
Oil Viscosity ()
Three-stage calculation:
| Stage | Function | Correlation |
|---|---|---|
| 1. Dead oil () | Egbogah (1983) | |
| 2. Saturated (, ) | Beggs-Robinson (1975) | |
| 3. Undersaturated (, ) | Vasquez-Beggs (1980) |
📖 Full Documentation: Oil Viscosity Correlations
Oil Compressibility ()
| Condition | Correlation | Typical Values |
|---|---|---|
| Undersaturated () | Vasquez-Beggs (1980) | 10-30 × 10⁻⁶ 1/psi |
| Saturated () | Villena-Lanzi (1985) | 50-200 × 10⁻⁶ 1/psi |
📖 Full Documentation: Oil Compressibility Correlations
Calculation Workflow
Complete Oil PVT at Any Pressure
Statistical Performance Guidelines
Expected Accuracy
| Property | AARE Range | Best Achievable |
|---|---|---|
| 5-15% | < 5% with tuning | |
| 5-12% | < 5% with tuning | |
| 1-5% | < 2% with tuning | |
| 10-25% | 5-10% with tuning | |
| 15-30% | 10-15% with tuning |
When Correlations Fail
| Symptom | Likely Cause | Solution |
|---|---|---|
| off by > 20% | Wrong correlation for oil type | Try regional correlation |
| too high/low | Inconsistent and | Use matched pair |
| 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
- at should be maximum value
- at should be minimum value
- for all
- decreases for (undersaturated)
- decreases for (saturated, as gas evolves)
Input Validation
| Parameter | Typical Range | Check |
|---|---|---|
| 0.55 - 1.5 | Air = 1.0, methane ≈ 0.55 | |
| 10 - 60 | Water = 10, very light > 40 | |
| 0 - 3000 scf/STB | Higher = more volatile | |
| 60 - 350 °F | Reservoir temperature | |
| 100 - 10000 psia | Must be < initial pressure |
Related Documentation
Oil Properties
- Bubble Point Correlations — 7 methods with regional guidance
- Solution GOR Correlations — Rs calculation methods
- Oil Formation Volume Factor — Bo saturated/undersaturated
- Oil Viscosity Correlations — Three-stage viscosity calculation
- Oil Compressibility Correlations — Co above and below Pb
Gas Properties
- Gas Properties — Z-factor, viscosity, density, pseudo-criticals
Water Properties
- Water Properties — Bw, Cw, μw, Rsw correlations
Other Properties
- Interfacial Tension — Gas-oil IFT for multiphase flow
Supporting Functions
- Unit Conversions — API/SG conversions
- Interpolation — For PVT table lookup
References
McCain, W.D. Jr. (1990). The Properties of Petroleum Fluids, 2nd Edition. PennWell Books.
Ahmed, T. (2019). Reservoir Engineering Handbook, 5th Edition. Gulf Professional Publishing.
Whitson, C.H. and Brulé, M.R. (2000). Phase Behavior. SPE Monograph Vol. 20.
Standing, M.B. (1981). Volumetric and Phase Behavior of Oil Field Hydrocarbon Systems, 9th Edition. Society of Petroleum Engineers.
Danesh, A. (1998). PVT and Phase Behaviour of Petroleum Reservoir Fluids. Elsevier.