Multiphase Correlation Comparison
Spreadsheet
55 rows x 3 columns
| A | B | C | |
|---|---|---|---|
| 1 | Multiphase Flow Correlation Comparison | ||
| 2 | Well & Fluid Properties | ||
| 3 | Liquid Rate | 1500 | bbl/d |
| 4 | Liquid Density | 52 | lb/ft3 |
| 5 | Liquid Viscosity | 1.5 | cP |
| 6 | Gas Rate | 2 | mmscf/d |
| 7 | Gas Specific Gravity | 0.7 | (air=1) |
| 8 | Gas Density | 3 | lb/ft3 |
| 9 | Gas Viscosity | 0.012 | cP |
| 10 | Interfacial Tension | 25 | dynes/cm |
| 11 | Liquid FVF (Bl) | 1.15 | bbl/STB |
| 12 | Gas FVF (Bg) | 0.006 | rcf/scf |
| 13 | Solution GOR (Rs) | 350 | scf/STB |
| 14 | |||
| 15 | Pipe Properties | ||
| 16 | Tubing ID | 2.992 | in |
| 17 | Pipe Length | 7500 | ft |
| 18 | Pipe Roughness | 0.0006 | - |
| 19 | Pipe Angle | 90 | degrees |
| 20 | Temperature | 175 | degF |
| 21 | Wellhead Pressure | 200 | psia |
| 22 | |||
| 23 | Bottomhole Pressure Comparison | ||
| 24 | Correlation | BHP (psia) | Difference from B&B |
| 25 | Beggs & Brill | 1190.747578 | - |
| 26 | Gray | 907.836087 | -282.9114907 |
| 27 | Hagedorn & Brown | 1116.928959 | -73.81861869 |
| 28 | Ansari (Mechanistic) | 1108.865095 | -81.88248264 |
| 29 | Hasan-Kabir | 899.6309867 | -291.116591 |
| 30 | Mukherjee-Brill | 1296.968294 | 106.2207164 |
| 31 | Orkiszewski | 947.9161498 | -242.8314279 |
| 32 | Duns & Ros | 1128.362389 | -62.38518841 |
| 33 | Aziz | 762.5826439 | -428.1649338 |
| 34 | Poettmann-Carpenter | 691.8865161 | -498.8610616 |
| 35 | |||
| 36 | Pressure Gradient Comparison (at 1000 psi) | ||
| 37 | Correlation | dP/dL (psi/ft) | Relative % |
| 38 | Beggs & Brill | 0.2194305283 | 100 |
| 39 | Gray | 0.218146079 | 99.41464424 |
| 40 | Hagedorn & Brown | 0.2039705991 | 92.95452219 |
| 41 | Ansari (Mechanistic) | 0.2039705991 | 92.95452219 |
| 42 | Hasan-Kabir | 0.2530955091 | 115.3419768 |
| 43 | Mukherjee-Brill | 0.2357231555 | 107.4249592 |
| 44 | Orkiszewski | 0.2141559834 | 97.59625751 |
| 45 | Duns & Ros | 0.2233078682 | 101.7670011 |
| 46 | Aziz | 0.2517333456 | 114.7212047 |
| 47 | Poettmann-Carpenter | 0.2039705991 | 92.95452219 |
| 48 | |||
| 49 | BHP vs Rate - Key Correlations | ||
| 50 | Rate (bbl/d) | B&B BHP | Gray BHP |
| 51 | 500 | 1092.155946 | 640.193133 |
| 52 | 1000 | 1105.224901 | 761.5381642 |
| 53 | 1500 | 1190.747578 | 907.836087 |
| 54 | 2000 | 1312.477189 | 1059.746117 |
| 55 | 2500 | 1454.632767 | 1213.011793 |
Description
Compare pressure drop predictions from all ten industry-standard multiphase flow correlations. Understanding correlation differences helps engineers select the most appropriate method for specific well conditions.
Correlations:
- Beggs & Brill (1973): General-purpose, any inclination, most widely used
- Gray (1974): Best for gas wells with liquid loading
- Hagedorn & Brown (1965): Near-vertical oil wells, industry standard
- Ansari (1994): Mechanistic TUFFP model, vertical wells
- Hasan-Kabir (1988): Mechanistic, deviated wells and annular geometry
- Mukherjee-Brill (1985): Improvement over Beggs-Brill for inclined wells
- Orkiszewski (1967): Composite vertical well correlation
- Duns & Ros (1963): High GOR gas wells
- Aziz (1972): Drift-flux model for vertical wells
- Poettmann-Carpenter (1952): Historical no-slip method, high-rate dispersed flow
How to use this blueprint
- In Excel, go to the Petroleum Office ribbon tab and click Blueprint Manager
- Search for Multiphase Correlation Comparison
- Click on the blueprint to preview the spreadsheet template
- Click Insert to place it into your worksheet. Modify the input values to match your data.