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 β fluid flow and recovery calculations
- Material balance β reserves estimation
- Well performance β inflow and outflow analysis
- Facilities design β separator and pipeline sizing
- Production forecasting β 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 | GlasΓΈ (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
βββββββββββββββββββββββββββββββββββββββ
β Reservoir Oil β
β (Gas in Solution + Liquid) β
βββββββββββββββββββββββββββββββββββββββ
β
βββββββββββββββββΌββββββββββββββββ
β β β
βΌ βΌ βΌ
βββββββββββββ βββββββββββββ βββββββββββββ
β Rs β β Bo β β ΞΌo β
β Solution β β Formation β β Viscosity β
β GOR β β Volume β β β
βββββββββββββ βββββββββββββ βββββββββββββ
β β β
βΌ βΌ βΌ
βββββββββββββ βββββββββββββ βββββββββββββ
β Pb β β Co β β Stage β
β Bubble β βCompress- β β Dead β β
β Point β β ibility β βSat β USat β
βββββββββββββ βββββββββββββ βββββββββββββ
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 | GlasΓΈ |
| North Sea | GlasΓΈ | 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 |
π Full Documentation: Bubble Point Correlations
Solution Gas-Oil Ratio ()
Same regional preferences as bubble point β the correlations are mathematically related (inverses of each other).
π Full Documentation: Solution GOR Correlations
Oil Formation Volume Factor ()
| Condition | Correlation | Notes |
|---|---|---|
| Saturated () | Match correlation | Use same author for consistency |
| Undersaturated () | From and |
π 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) |
π Full Documentation: Oil Viscosity Correlations
Oil Compressibility ()
| Condition | Correlation | Typical Values |
|---|---|---|
| Undersaturated () | Vasquez-Beggs (1980) | 10-30 Γ 10β»βΆ 1/psi |
| Saturated () | Villena-Lanzi (1985) | 50-200 Γ 10β»βΆ 1/psi |
π Full Documentation: Oil Compressibility Correlations
Calculation Workflow
Complete Oil PVT at Any Pressure
βββββββββββββββββββββββββββββββββββββββββββββββββββββββββββββββ
β INPUTS: P, T, Ξ³g, Ξ³API, (Rsob or lab Pb) β
βββββββββββββββββββββββββββββββββββββββββββββββββββββββββββββββ
β
βΌ
βββββββββββββββββββββββββββββββββββββββββββββββββββββββββββββββ
β Step 1: Calculate Bubble Point β
β Pb = f(Rsob, Ξ³g, Ξ³API, T) β
β OR use measured Pb β
βββββββββββββββββββββββββββββββββββββββββββββββββββββββββββββββ
β
βΌ
βββββββββββββββββββββββββββββββββββββββββββββββββββββββββββββββ
β Step 2: Determine Pressure Regime β
β P > Pb β Undersaturated β
β P β€ Pb β Saturated β
βββββββββββββββββββββββββββββββββββββββββββββββββββββββββββββββ
β β
Undersaturated Saturated
β β
βΌ βΌ
ββββββββββββββββββββββββββββ ββββββββββββββββββββββββββββ
β Step 3a: USat Properties β β Step 3b: Sat Properties β
β Rs = Rsob (constant) β β Rs = f(P, T, Ξ³g, Ξ³API) β
β Bo = BobΒ·exp[-co(P-Pb)] β β Bo = f(Rs, T, Ξ³g, Ξ³o) β
β ΞΌo = f(ΞΌob, P, Pb) β β ΞΌo = f(ΞΌod, Rs) β
β co = f(Rsob, Ξ³g, Ξ³API, β β co = f(P, Pb, T, Rsob, β
β T, P) β β Ξ³API) β
ββββββββββββββββββββββββββββ ββββββββββββββββββββββββββββ
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 β 0.55 | |
| 10 - 60 | Water = 10, very light > 40 | |
| 0 - 3000 scf/STB | Higher = more volatile | |
| 60 - 350 Β°F | Reservoir temperature | |
| 100 - 10000 psia | Must be < initial pressure |
Related Documentation
Oil Properties
- Bubble Point Correlations β 7 methods with regional guidance
- Solution GOR Correlations β Rs calculation methods
- Oil Formation Volume Factor β Bo saturated/undersaturated
- Oil Viscosity Correlations β Three-stage viscosity calculation
- Oil Compressibility Correlations β Co above and below Pb
Gas Properties
- Gas Properties β Z-factor, viscosity, density, pseudo-criticals
Water Properties
- Water Properties β Bw, Cw, ΞΌw, Rsw correlations
Other Properties
- Interfacial Tension β Gas-oil IFT for multiphase flow
Supporting Functions
- Unit Conversions β API/SG conversions
- Interpolation β 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 BrulΓ©, 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.