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The Inflow Performance Relationship (IPR) defines the mathematical link between flowing bottomhole pressure ($p_{wf}$) and the volumetric production rate ($Q$) delivered from the porous rock reservoir into the wellbore. Accurately modeling this relationship is fundamental to production engineering: it dictates artificial lift design, tubing size selection, surface compression schedules, and field life forecasting.
In natural gas reservoirs, high fluid velocities near the wellbore cause inertial pressure losses (the Forchheimer effect or non-Darcy turbulence). The classic standard for capturing this non-linear behavior is the Rawlins and Schellhardt Backpressure Equation (US Bureau of Mines Monograph 7).
1. Wellhead & Reservoir Test Data
A production well drilled into a deep sandstone gas reservoir underwent a 4-point modified isochronal backpressure test: * Average Static Reservoir Pressure ($\bar{p}_R$): $280.0\text{ barg}$ ($281.01\text{ bar(a)} = 4,075.8\text{ psia}$) * Stabilized Test Flow Rate ($Q_{test}$): $250,000\text{ Sm}^3/\text{day}$ ($8.829\text{ MMSCFD}$) * Flowing Bottomhole Pressure ($p_{wf}$): $240.0\text{ barg}$ ($241.01\text{ bar(a)} = 3,495.3\text{ psia}$) * Deliverability Exponent ($n$): $0.82$ (fitted from multi-rate flow periods) * Gas Specific Gravity ($G$): $0.65$ * Reservoir Temperature: $95.0^\circ\text{C}$ ($203.0^\circ\text{F}$)
2. Mathematical Foundation: Rawlins-Schellhardt Formulation
The empirical backpressure equation states:
Where: * $Q$ is gas flow rate (in $\text{MMSCFD}$ or $\text{Sm}^3/\text{day}$) * $\bar{p}R$ is static average reservoir pressure ($\text{psia}$ or $\text{bar}$) * $p$) * $C$ is the stabilized deliverability performance coefficient * $n$ is the backpressure turbulence exponent ($0.5 \le n \le 1.0$) * $n = 1.0$: Completely laminar Darcy flow * $n = 0.5$: Completely turbulent (non-Darcy) flow dominated by inertial resistance}$ is flowing bottomhole pressure ($\text{psia}$ or $\text{bar
3. Step 1: Calculate Pressure-Squared Drawdown ($\Delta p^2$)
Convert pressures to field units ($\text{psia}$):
The drawdown pressure-squared driving force is:
4. Step 2: Solve for Performance Coefficient ($C$)
Rearranging the backpressure formula:
Substitute the test rate ($Q_{test} = 8.829\text{ MMSCFD}$) and $n = 0.82$:
In metric units (using $\text{bar}$ and $\text{Sm}^3/\text{day}$):
5. Step 3: Determine Absolute Open Flow Potential (AOFP)
The Absolute Open Flow Potential (AOFP) is the theoretical maximum rate the reservoir could deliver if the flowing bottomhole pressure were reduced to absolute atmospheric pressure ($p_{wf} = 0\text{ psia}$):
In standard metric units:
6. Step 4: Construct Full Inflow Performance Curve
Using our fitted parameters ($C = 0.031541, n = 0.82$), we calculate flow rates across bottomhole operating pressures:
| Drawdown % | Flowing $p_{wf}$ (barg) | Flowing $p_{wf}$ (psia) | $\bar{p}R^2 - p^2$)}^2$ ($\text{psia | Flow Rate $Q$ (MMSCFD) | Flow Rate $Q$ ($\text{Sm}^3/\text{day}$) |
|---|---|---|---|---|---|
| 0% (Shut-in) | $280.0$ | $4075.8$ | $0.00$ | $0.00$ | $0$ |
| 10% | $252.0$ | $3669.7$ | $3.14 \times 10^6$ | $6.69$ | $189,400$ |
| 20% | $224.0$ | $3263.6$ | $5.96 \times 10^6$ | $11.33$ | $320,800$ |
| 30% | $196.0$ | $2857.5$ | $8.45 \times 10^6$ | $15.02$ | $425,300$ |
| 40% | $168.0$ | $2451.4$ | $1.06 \times 10^7$ | $18.11$ | $512,800$ |
| 50% | $140.0$ | $2045.3$ | $1.24 \times 10^7$ | $20.76$ | $587,800$ |
| 60% | $112.0$ | $1639.2$ | $1.39 \times 10^7$ | $22.75$ | $644,200$ |
| 70% | $84.0$ | $1233.1$ | $1.51 \times 10^7$ | $24.28$ | $687,500$ |
| 80% | $56.0$ | $827.0$ | $1.59 \times 10^7$ | $25.32$ | $717,000$ |
| 90% | $28.0$ | $420.9$ | $1.64 \times 10^7$ | $25.96$ | $735,100$ |
| 100% (AOFP) | $0.0$ | $14.7$ | $1.66 \times 10^7$ | $26.28$ | $744,132$ |
7. Engineering Discussion: Deliverability Diagnostics
graph TD
A[AOFP = 26.28 MMSCFD] --> B[Typical Operating Window: 40% - 65% of AOFP]
B --> C[Recommended Production Rate: 10.5 - 17.0 MMSCFD]
C --> D[Pwf = 180 to 230 barg]
D --> E[Prevents Sand Production & Water Coning]
- Operating Range vs AOFP:
- Wells are rarely operated at $>70\%$ of AOFP. Operating at extreme drawdowns triggers wellbore shear failure, sand mobilization, premature water coning, and severe near-wellbore skin damage.
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For this well, a sustainable production target is $10.5$ to $17.0\text{ MMSCFD}$ ($p_{wf} \approx 180 - 230\text{ barg}$).
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Significance of $n = 0.82$:
- An exponent of $0.82$ indicates moderate turbulence in the completion gravel pack or perforation tunnels. If stimulation (hydraulic fracturing or acidizing) is performed, non-Darcy pressure loss is minimized, shifting $n \to 0.95$ and significantly expanding deliverability.
Gas Well Deliverability & IPR Curve
Apply this methodology directly in the ChemProCal calculator.
Open Calculator →References
- Rawlins, E.L. and Schellhardt, M.A. - Back-Pressure Data on Natural Gas Wells and Their Application to Production Practices (US Bureau of Mines Monograph 7, 1935) - Book
- Lee, J. and Wattenbarger, R.A. - Gas Reservoir Engineering (SPE Textbook Series Vol. 5, 1996) - Book
- API RP 14B - Design, Installation, Operation, Test, and Redress of Subsurface Safety Valve Systems (6th Edition, 2015) - Standard [Link ↗]
Apply Methodology in Gas Well Deliverability & IPR Curve
Execute complete engineering simulations using the governing mathematical equations from this guide:
Apply the exact mathematical principles from this fundamental directly inside the official Gas Well Deliverability & IPR Curve engine.