Common Results | |||||
| Pressure Drop | Pressure Drop Ratio (DP/P1) | N/A | |||
| Pressure Ratio (P2/P1) | N/A | Critical Pressure Ratio | N/A | ||
| Reynolds (ReD) | N/A | Reynolds Flow Regime | N/A | ||
| Contraction coefficient | N/A | Expansibility Factor | N/A | ||
| Beta Ratio | N/A | Velocity in Pipe | |||
Specific Results | |||||
| Mass Flow | Mass Flow | ||||
| Volumetric Flow | |||||
Limits of Use | |||||
| Choked Flow - The result has not yet been evaluated. | |||||
| Velocity in Pipe - The result has not yet been evaluated. | |||||
This tutorial walks through two complete calculations using the Restriction Orifice — Find Flow Rate calculator. You will calculate the flow through an existing restriction orifice — once for a liquid (water) and once for a compressible gas (air), including a choked flow condition.
The calculator solves the inverse sizing problem: the orifice geometry is fixed and the upstream/downstream pressures are known; the output is flow rate. The governing equation for the base case is:
q = Cd × A × sqrt(2 × ΔP / ρ)
For compressible flow, the expansibility factor ε is applied:
q = Cd × ε × A × sqrt(2 × ΔP / ρ₁)
where ρ₁ is the upstream density and ε ≤ 1 corrects for gas expansion across the orifice.
Scope: This tutorial covers the Find Flow calculator only. If you need to size an orifice for a target flow, use the Restriction Orifice — Find Orifice Size calculator instead.
The page is organised into three sections — Identification Data, Fluid Data, and Pipe Data — followed by a Results panel.
These fields populate the downloadable ISA S20 report header. None affect the numerical result.
| Field | Purpose |
|---|---|
| Tagname | Instrument or RO tag |
| Plant | Plant or unit name |
| Area | Area or loop identifier |
| Notes | Free-text; appears in the report |
| Field | Liquid mode | Gas mode |
|---|---|---|
| Fluid Name | Free text | Free text |
| State of Matter | Liquid | Gas |
| Density (ρ) | Enter directly | Computed — field disabled |
| Molecular Weight | Disabled | Enter (g/mol) |
| Temperature | Disabled | Enter (°C) |
| Pressure Upstream (P1) | Enter | Enter |
| Pressure Downstream (P2) | Enter | Enter |
| Dynamic Viscosity | Enter (cP or Pa·s) | Enter (cP or Pa·s) |
State switching: When you select Gas, the Density field disables and Molecular Weight + Temperature enable. The calculator derives gas density via the ideal gas law:
ρ = P × M / (R × T). Switching back to Liquid restores the Density field.
| Field | Description |
|---|---|
| Pipe Diameter D | Internal pipe diameter (mm or in) |
| Orifice Diameter d | Orifice bore diameter (mm or in) |
The beta ratio β = d / D is computed internally and displayed in gas results.
A 4-inch line has a restriction orifice with a 10.943 mm bore. Upstream pressure is 14 bar(a), downstream 12 bar(a). Confirm the flow rate at these conditions.
Set State of Matter to Liquid first.
| Field | Value | Unit |
|---|---|---|
| Fluid Name | Water | — |
| State of Matter | Liquid | — |
| Density | 998 | kg/m³ |
| Pressure Upstream (P1) | 14 | bar |
| Pressure Downstream (P2) | 12 | bar |
| Dynamic Viscosity | 1 | cP |
Use consistent pressure references for P1 and P2 — the calculator uses
ΔP = P1 − P2, so the absolute/gauge offset cancels as long as both share the same reference.
| Field | Value | Unit |
|---|---|---|
| Pipe Diameter D | 101.6 | mm |
| Orifice Diameter d | 10.943 | mm |
This gives β = 10.943 / 101.6 ≈ 0.1077.
Common Results
| Result | Value |
|---|---|
| Pressure Drop | 2.00 bar |
| Reynolds Number (ReD) | Turbulent range |
| Reynolds Flow Regime | Turbulent |
| Velocity in Pipe | Low (< 1 m/s) |
Specific Results
| Result | Approximate Value |
|---|---|
| Mass Flow | ~0.1 kg/s |
| Mass Flow | ~360 kg/h |
| Volumetric Flow | ~0.36 m³/h |
Choked flow for liquids: No choked flow check is applied. Liquid choking (cavitation onset) is a separate phenomenon. If cavitation is a concern, verify that P2 is well above the fluid vapour pressure at operating temperature.
Unit switching: After the calculation runs you can change the result unit selector (e.g. bar → psi, kg/s → lb/h) without re-running — the calculator applies a client-side conversion from the stored base value.
Same orifice and pipe geometry, now carrying air. Upstream 14 bar(a), downstream 7 bar(a). The pressure ratio P2/P1 = 0.500 is below the critical pressure ratio for air (~0.528), so choked flow is expected.
Set State of Matter to Gas.
| Field | Value | Unit |
|---|---|---|
| Fluid Name | Air | — |
| State of Matter | Gas | — |
| Molecular Weight | 28.97 | g/mol |
| Temperature | 25 | °C |
| Pressure Upstream (P1) | 14 | bar |
| Pressure Downstream (P2) | 7 | bar |
| Dynamic Viscosity | 0.018 | cP |
The calculator derives upstream density:
ρ = 1,400,000 × 0.02897 / (8.314 × 298.15) ≈ 16.37 kg/m³
Same as Example 1: D = 101.6 mm, d = 10.943 mm.
Specific Results — Gas
| Result | Value | Notes |
|---|---|---|
| Beta Ratio (β) | 0.1077 | d / D |
| Contraction Coefficient | < 1 | Vena contracta area ratio |
| Expansibility Factor (ε) | < 1 | Compressibility correction |
| Critical Pressure Ratio | ~0.528 | For air, γ = 1.4 |
| Pressure Drop Ratio (x) | 0.50 | ΔP / P1 = 7 / 14 |
| Choked Flow | Yes | P2/P1 < r_c |
| Mass Flow | (choke-limited) | Capped at sonic condition |
| Volumetric Flow | (at P1, T) | Based on upstream density |
The critical pressure ratio for an ideal gas:
r_c = (2 / (γ + 1))^(γ / (γ − 1))
For air (γ = 1.4):
r_c = (2 / 2.4)^(1.4 / 0.4) = (0.8333)^3.5 ≈ 0.528
P2 / P1 ≥ r_c → Not choked. Flow proportional to sqrt(ΔP).P2 / P1 < r_c → Choked. Velocity at the vena contracta is sonic. Further reduction of P2 does not increase mass flow.Practical consequence: If the calculator returns Choked Flow = Yes, the displayed mass flow is the maximum achievable at those upstream conditions. To increase throughput you must raise P1 or enlarge the orifice bore.
γ dependency: The critical pressure ratio depends on γ = Cp/Cv. The calculator uses γ ≈ 1.4 (diatomic gases). For other gases, verify against the Heat Capacity Ratio of Common Fluids table.
The expansibility factor ε corrects for the reduction in gas density as it accelerates and expands from P1 to P2. A common approximation for sharp-edged orifices:
ε = 1 − (0.41 + 0.35 × β⁴) × x / γ
where x = ΔP / P1.
ε = 1 for incompressible fluids (liquids).ε < 1 for gases; decreases as x increases.ε is not extrapolated beyond its valid range.For small pressure drops (x < 0.1) the correction is minor. At x = 0.5 as in Example 2, ignoring ε would significantly overestimate the flow. The calculator applies it automatically.
| Aspect | Liquid | Gas |
|---|---|---|
| Density input | Direct entry | Computed via ideal gas law |
| Expansibility factor | 1.0 (not displayed) | Computed and displayed |
| Choked flow check | Not applicable | Evaluated against r_c automatically |
| Beta ratio displayed | No | Yes |
| Compressibility (Z) | Not accounted for | Ideal gas (Z = 1) |
| Volumetric flow basis | Process conditions | Upstream conditions (P1, T) |
High-pressure gases: The ideal gas law (Z = 1) is adequate for moderate pressures. For gases with significant non-ideal behaviour at high pressure, obtain the actual density from a real-gas equation of state and enter it manually by switching to Liquid mode.
Used Equation
Dimensional Analysis
Beta Ratio The ratio of the orifice diameter to the pipe diameter, affecting flow restriction and pressure drop. It is essential in flow measurement, with specific ratios optimizing accuracy for different flow ranges.
Choked Flow Choked flow occurs when a gas flow reaches maximum velocity due to critical pressure conditions, limiting further flow increase. It is vital in gas transport systems to avoid system inefficiencies and ensure safe operation.
Common Results Refers to standard calculations and outputs in fluid mechanics, such as flow rate, pressure drop, and velocity, essential for analyzing system performance and determining if the design meets operational requirements.
Contraction Coefficient A factor representing the reduction in cross-sectional area in a flow contraction, influencing flow speed and pressure. It is used in flow calculations involving orifices and sudden changes in pipe diameter.
Critical Pressure Ratio The critical pressure ratio is the ratio of downstream to upstream pressure at which gas flow becomes choked, meaning maximum flow rate is reached. It is essential in designing nozzles and controlling flow in compressible fluid systems.
Density Density is the mass per unit volume of a fluid, typically measured in kg/m3. It impacts fluid behavior, such as buoyancy and pressure. High-density fluids exert greater pressure in systems, influencing design parameters in piping and fluid transport applications.
Dynamic Viscosity Dynamic viscosity is a measure of a fluid's resistance to shear or flow, measured in Pascal-seconds (Pa·s) or centipoise (cP). It affects how easily a fluid flows through pipes and around objects, influencing energy requirements in pumping systems.
Expansibility Factor A correction factor for compressible fluids, accounting for gas expansion in flow through orifices or nozzles. It affects accurate flow measurements and is particularly important in high-pressure gas systems.
Fluid Data Refers to essential information about a fluid, including properties like density, viscosity, and specific heat. This data is crucial for calculating flow rates, pressure drops, and heat transfer in systems.
Limits of Use Defines the operational boundaries, like maximum pressure or temperature, for a system. Staying within these limits ensures safe, efficient operation and protects equipment from damage or failure.
Mass Flow (kg/h) The amount of fluid mass passing through a point per hour. It is critical for measuring fluid transport, affecting system sizing, energy requirements, and overall efficiency in industrial processes.
Mass Flow (kg/s) Mass flow in kg/s indicates fluid mass per second, important for real-time flow control and energy calculations in fast-moving fluid systems, especially in high-demand applications like power generation.
Molecular Weight Molecular weight is the mass of a molecule of a substance, measured in atomic mass units (amu). In fluid mechanics, it helps calculate the density of gases and affects the fluid's compressibility and flow characteristics.
Operating Pressure The pressure at which a system operates, influencing fluid density and flow rate. Higher pressures increase fluid density in gases, affecting flow calculations and system integrity. Operating pressure is crucial for safety, efficiency, and equipment durability in fluid systems.
Operating Temperature The temperature at which a fluid operates within a system, influencing its viscosity, density, and flow behavior. Higher temperatures generally decrease fluid viscosity, affecting the resistance to flow.
Orifice Diameter The diameter of an orifice or opening in a pipe, often used for flow restriction or measurement. It restricts flow, creating a pressure difference used to calculate flow rate, with smaller diameters increasing pressure drop and reducing flow.
Pipe Data Refers to the dimensions, materials, and specifications of piping systems, affecting fluid dynamics, resistance, and capacity. Pipe data is essential for designing efficient fluid transport systems and calculating parameters like flow rate and pressure drop.
Pipe Diameter Inside diameter of the pipe. All process calculations are based on the volume of the pipe which is a function of its internal diameter. Larger diameters reduce friction and resistance, improving flow efficiency.
Pressure Downstream Fluid pressure after passing through the restriction orifice. It impacts flow rate and is essential for calculating pressure drops, energy losses, and flow efficiency within the piping system.
Pressure Drop Pressure drop is the reduction in fluid pressure as it flows through a system, caused by friction, restrictions, or changes in elevation. Across a restriction orifice it is the driving force for the flow and is determined by the difference between upstream and downstream pressures.
Pressure Drop Ratio The ratio of pressure drop across an element to the inlet pressure. It helps assess energy losses and efficiency in a system, with high ratios indicating significant pressure loss and potential flow restrictions.
Pressure Ratio The ratio of outlet pressure to inlet pressure, used to describe pressure changes across systems. It is crucial in analyzing compressible flows, particularly in gas systems, to determine flow characteristics and efficiency. For gases, it determines whether flow is choked.
Ratio of Specific Heats The ratio of specific heats (γ or kappa) is the ratio of a fluid's specific heat at constant pressure to its specific heat at constant volume. It affects compressible flow and is critical in calculations involving gases and thermodynamics.
Reynolds Flow Regime The classification of flow as laminar, transitional, or turbulent based on the Reynolds number. It affects flow behavior, pressure drop, and efficiency, guiding the design and operation of fluid systems.
Reynolds Number A dimensionless number indicating whether a fluid flow is laminar or turbulent, calculated from fluid velocity, density, viscosity, and characteristic length. It helps predict flow patterns and friction losses in pipes and channels.
Specific Results Refers to calculated values unique to a system's conditions, such as specific flow rates or pressure conditions, essential for verifying that the system operates within desired parameters for performance and safety.
State of Matter Defines the physical state of a substance: solid, liquid, or gas, determined by temperature and pressure. In fluid mechanics, the state of matter affects fluid flow, density, and viscosity. Gases are compressible; liquids are nearly incompressible.
Velocity in Pipe The speed of fluid movement through the pipe, influenced by pipe diameter and flow rate. It affects pressure drop, energy losses, and is crucial for sizing pipes to avoid excessive turbulence or friction.
Volumetric Flow The volume of fluid passing through a point per unit time, often in m3/h. It is used in pump sizing, system efficiency calculations, and to ensure fluid supply meets demand in various processes.
1 International Organization of Standards (ISO 5167-1). 2003. Measurement of fluid flow by means of pressure differential devices inserted in circular cross-section conduits running full - Part 1: General principles and requirements.
2 International Organization of Standards (ISO 5167-2). 2003. Measurement of fluid flow by means of pressure differential devices inserted in circular cross-section conduits running full -- Part 2: Orifice plates.
3 American Society of Mechanical Engineers (ASME). 2001. Measurement of fluid flow using small bore precision orifice meters. ASME MFC-14M-2001.
4 U.S. Dept. of the Interior, Bureau of Reclamation, 2001 revised, 1997 third edition, Water Measurement Manual.
5 Michael Reader-Harris (2015) Orifice Plates and Venturi Tubes.
6 Miller, R. W., Flow Measurement Handbook, 3rd ed., McGraw-Hill, New York, 1996.
7 American Gas Association, AGA Gas Measurement Manual, American Gas Association, New York.
8 Wikipedia
9 Corrosionpedia
10 Orifice Plates and Venturi Tubes (2015) - Michael Reader-Harris
11 EMERSON Fundamentals of Orifice Meter Measurement
12 Search Data Center
Flow Rate Calculator — calculate the volumetric flow rate of any liquid or gas through a specific pipe diameter and download results.
Pressure Measurement — learn about pressure measurement principles, units, and instrumentation.
Orifice Plate Calculator — Find Orifice Size — a useful tool to calculate the size of an orifice plate for flow measurement.
Density of Common Liquids — a useful table that represents the density of some common liquids and their temperature.
Absolute Viscosity of Common Gases — reference table for dynamic viscosity values needed as calculator input for gas flows.
Heat Capacity Ratio of Common Fluids — reference table for the ratio of specific heats (γ) required for gas restriction orifice calculations.
Molecular Weight of Common Fluids — reference table for molecular weight values to use as input when calculating gas density.
Q1 What is orifice restriction?
A1 Orifice restriction refers to the use of an orifice plate or similar device within a piping system to regulate fluid flow. The orifice creates a constriction, resulting in a drop in pressure as the fluid passes through. This drop can be utilised to control flow rates, improve measurement accuracy, or facilitate mixing processes. The size and shape of the orifice directly influence the flow characteristics, making it a critical component in systems designed for precise fluid handling. These devices are widely used in various applications, including chemical processing, water treatment, and HVAC systems.
Q2 What is the difference between a restrictor and an orifice?
A2 The main difference between a restrictor and an orifice lies in their design and intended function. A restrictor is typically designed to limit the flow of fluid through a system and can be adjustable, providing a variable restriction based on system requirements. Conversely, an orifice is a fixed opening that creates a pressure drop to regulate flow, often used for measurement or control. While both devices can restrict flow, restrictors are more versatile and often used in applications requiring fine-tuning of flow rates, whereas orifices are used for more specific pressure and flow measurements in established systems.
Q3 What is RO in P&ID?
A3 In a Piping and Instrumentation Diagram (P&ID), RO stands for Restriction Orifice. It is represented as a specific symbol indicating where the flow is restricted within the piping system. The RO is crucial in controlling flow rates, providing pressure drops, and measuring fluid dynamics in various applications. Properly designed ROs contribute to system reliability by preventing excessive pressure build-up and ensuring optimal flow characteristics.
Q4 What is the purpose of the orifice?
A4 The primary purpose of an orifice is to control the flow of fluid within a system. By providing a defined opening, orifices can regulate the passage of liquids or gases, enabling precise flow control and measurement. This functionality is essential in various applications, including water treatment, HVAC systems, and industrial processes. Orifices help maintain desired pressure levels, optimise energy consumption, and improve system efficiency.
Q5 What is a throttling orifice?
A5 A throttling orifice is a specific type of orifice used to reduce fluid flow and pressure within a piping system. It creates a pressure drop across the orifice, which allows for controlled flow rates and maintains specific operating conditions. Throttling orifices are commonly employed in applications where precise flow control is necessary, such as in hydraulic systems, chemical processes, and air conditioning.
Q6 Does an orifice reduce flow?
A6 Yes, an orifice does reduce flow. When fluid passes through an orifice, it encounters a constriction that creates a pressure drop. This drop leads to a reduction in the flow rate as the fluid is forced through the smaller opening. The degree of flow reduction is influenced by the size of the orifice and the fluid's properties. While the flow is reduced, orifices also help ensure that the system operates within safe and efficient limits.
Q7 How can we calculate a restriction orifice?
A7 Calculating a restriction orifice typically involves determining its size based on the desired flow rate, fluid properties, and system conditions. Engineers use various empirical methods based on standards such as ISO 5167 to estimate the appropriate diameter for the orifice, taking into account factors such as fluid viscosity, density, and the pressure differential across the orifice. It is also essential to consider the intended application, as different processes may require specific flow characteristics.
Q8 Is there any consideration about restriction orifices and gas flows?
A8 Yes, when dealing with restriction orifices and gas flows, several considerations must be taken into account. Gases are compressible fluids, which means their density and viscosity can change significantly with pressure and temperature variations. This characteristic affects the flow rate through the orifice and requires careful calculations to ensure accurate flow measurements. Additionally, pressure drops across the orifice can lead to choked flow conditions, where the flow rate reaches a maximum limit and cannot increase further despite changes in upstream pressure.
Q9 Which are the differences between liquid and gas regarding restriction orifice calculations?
A9 The differences between liquid and gas restriction orifice calculations primarily stem from their physical properties. Liquids are generally incompressible, allowing for simpler calculations based on flow rates, pressure drops, and orifice size. In contrast, gases are compressible, requiring more complex calculations that consider variations in density and viscosity. Additionally, gas flow can become choked when the pressure ratio reaches a critical value, necessitating a different approach to orifice sizing and pressure drop calculations.