
ISO 5167 vs. AGA Report No. 3
An interactive guide to the world's leading standards for differential pressure flow measurement.
The Philosophical Divide
The core differences between ISO 5167 and AGA 3 stem from their origins. One was designed for universal engineering versatility, the other for specialized fiscal accuracy in a single industry.
ISO 5167: The Universal Framework
Developed by a cross-industrial, international body, ISO 5167 provides a scientifically robust and versatile framework for a vast range of fluids and devices. Its goal is consistent and reliable measurement for broad engineering applications like process control, efficiency monitoring, and energy allocation.
Fluids: Any single-phase Newtonian fluid (liquids, gases, steam).
Devices: Orifice Plates, Nozzles, Venturi Tubes, Cone & Wedge Meters.
AGA Report No. 3: The Fiscal Specialist
Born from the high-stakes commercial needs of the U.S. natural gas industry, AGA 3 is a highly prescriptive and detailed standard. Its primary driver is absolute accuracy and contractual defensibility for the custody transfer of a high-value commodity.
Fluids: Primarily natural gas and related hydrocarbon fluids.
Devices: Almost exclusively the concentric, flange-tapped orifice meter.
Technical Deep Dive
Orifice Plate Specifications
Both standards demand precision, but AGA 3's focus on fiscal metering leads to significantly tighter tolerances in key areas. This chart compares relative stringency (higher score = tighter tolerance). For a detailed breakdown, view the specification table.
Parameter | ISO 5167-2 Specification | AGA 3 Part 2 Specification |
---|---|---|
Edge Sharpness | Edge radius r < 0.0004d | Square and sharp; free from defects visible to the naked eye |
Plate Flatness | Deviation < 1% of dam height | Deviation < 0.010 in/in of dam height |
Eccentricity | Must be concentric | Extremely tight tolerances (e.g., 0.006" for 2" pipe) |
Beta Ratio (β) | 0.10 to 0.75 | 0.10 to 0.75 (recommends 0.2 to 0.6 for min. uncertainty) |
Reynolds No. (ReD) | ≥ 5000 | ≥ 4000 |
Installation: The Cost of Compliance
AGA 3 generally mandates longer upstream straight pipe lengths, directly impacting capital costs. Use the dropdown to see how Beta Ratio (β) affects requirements for various fittings. In practice, flow conditioners are often used to drastically reduce these lengths.
The Physics of Flow Calculation
While the standards have converged on the core Reader-Harris/Gallagher (RHG) equation for the discharge coefficient (Cd), differences remain in other areas. Explore the key components of the flow calculation below.
Both standards derive their calculations from Bernoulli's principle. The resulting equation for mass flow rate (qm) transforms the measured differential pressure (Δp) into a flow rate using several empirical correction factors.
This is the most critical factor. Historically, ISO used the Stolz equation and AGA used the Buckingham equation, causing discrepancies. A major international research effort led to the development of the more accurate **Reader-Harris/Gallagher (RHG) Equation**, which has now been adopted by both standards, marking a significant harmonization.
The calculation is not a single step. The discharge coefficient (Cd) depends on the Reynolds number (ReD), but the Reynolds number depends on the flow rate (qm)—the very thing you are trying to calculate. Modern flow computers solve this circular dependency by starting with an assumed flow rate and iterating the calculation until the values converge to a stable solution.
Quantifying Doubt: Uncertainty Methodologies
A measured value is incomplete without a statement of its uncertainty. While both standards aim for a 95% confidence interval, their approaches reflect different philosophies.
ISO 5167: The GUM Framework
Adheres to the global ISO/IEC *Guide to the Expression of Uncertainty in Measurement* (GUM). It involves identifying all uncertainty sources, quantifying them as standard uncertainties (Type A or B), and combining them using the root-sum-of-squares (RSS) method to find the total uncertainty.
AGA 3: Systematic & Random Errors
Categorizes errors into two types: **Systematic (bias)** errors that are consistently directional, and **Random** errors that have an equal chance of being positive or negative. This approach is often preferred for field diagnostics in the gas industry.
Primary Uncertainty Contributors
For a well-maintained meter, the inherent uncertainty of the discharge coefficient equation itself is often the largest single contributor to the total measurement uncertainty.
Practical Application
The choice is not about which standard is "better," but which is correct for the specific application, fluid, location, and, most importantly, the commercial contract.
Decision Flowchart
(North America)
(International / Contract Dependent)