If you need any help, please feel free to contact us
A process engineer checks a differential pressure transmitter on a steam line, reads the pressure drop across an orifice plate, and converts that value into a mass flow figure for boiler efficiency reporting. That routine scene explains why differential pressure (DP) flow meters remain one of the most widely used and trusted methods of industrial flow measurement. The technology is simple in concept, robust in construction, and backed by decades of standards and field data.
A differential pressure flow meter measures the flow rate of a liquid, gas, or steam by sensing the pressure drop created when the fluid passes through a deliberate restriction in the pipe. The restriction is called the primary element. The pressure-sensing device that measures the difference between upstream and downstream pressure is called the secondary element, normally a differential pressure transmitter.
This approach works with virtually any fluid that can flow through a pipe, as long as the wetted materials handle the temperature, pressure, and chemical compatibility requirements. That broad applicability is the main reason DP flow measurement appears in nearly every industrial sector, from power generation and chemical processing to water treatment and HVAC systems.
The operating principle comes from Bernoulli's equation. For a steady flow, the sum of static pressure, velocity pressure, and elevation head remains constant along a streamline. When fluid enters a narrowed section of pipe, its velocity increases and its static pressure decreases. The pressure difference between the full-bore section and the restriction is proportional to the square of the flow velocity.
In practical terms, the volumetric flow rate equals a discharge coefficient multiplied by the square root of the differential pressure. That square root relationship has a direct consequence for instrument selection: at low flow, a small change in flow produces an even smaller change in differential pressure, which limits the usable turndown of the measurement.
A typical orifice plate installation offers a usable turndown of about 3:1 to 5:1. If a line is designed for a maximum flow of 100 m3/h, the measurement remains reasonably accurate down to roughly 20 to 33 m3/h, depending on the transmitter's performance at low differential pressures. Below that point, the square root curve becomes so flat that a tiny pressure error translates into a large flow error. Modern digital transmitters with high accuracy at low range improve the situation by a small margin, but the fundamental limitation stays.
The primary element determines the pressure drop, the permanent energy loss, and the overall accuracy of the system. Four designs cover the great majority of industrial applications.
| Primary element | Permanent pressure loss | Typical accuracy | Best-suited services |
| Orifice plate | High (about 40-70% of measured dP) | 1-2% of full scale | Clean liquids, gases, and steam; general industrial duty |
| Venturi tube | Low (about 10-15% of measured dP) | 0.5-1% of full scale | Large pipe sizes, permanent installations where pumping energy cost matters |
| Flow nozzle | Medium (about 30-50% of measured dP) | 1-1.5% of full scale | High-velocity flows and steam service |
| Pitot tube | Very low | 1-2% of reading, profile dependent | Large ducts and stacks, air and gas flow, minimal pressure loss required |
Orifice plates dominate because they are inexpensive, available in many materials, and governed by published standards such as ISO 5167. Venturi tubes are favored where pumping costs matter over the long term, because their low permanent pressure loss saves energy. Pitot tubes and averaging pitot arrays are common in large ductwork, where a full-bore restriction would be impractical.
The advantages explain the enduring popularity of the technique:
The limitations matter just as much:
As a rule, choose DP flow measurement when the fluid is steam, a clean liquid, or a gas at high temperature or high pressure, and when the expected flow range fits within a practical turndown. For steam mass flow, the orifice plate with a DP transmitter is still the default in power plants, refineries, and chemical facilities, because the same transmitter can also serve for static pressure and temperature compensation.
DP flow is a practical choice for large pipelines where a full-bore meter would be expensive to install, and for retrofits in older plants where existing flanges and straight pipe sections can accept an orifice plate. If the plant already stocks DP transmitters for other duties, the same spare instruments can support flow loops, simplifying spare parts management.
Look at other technologies when the fluid is viscous, dirty, or prone to clogging, because impulse lines and small bore openings will eventually block. Very low flow rates generate tiny differential pressures that are difficult to measure reliably. If the process regularly operates at widely different flow rates, the limited turndown of a DP system becomes a practical problem. And where the accuracy requirement must hold across a wide range, a Coriolis or ultrasonic meter is often a better fit.
The transmitter defines the quality of the final measurement. It must convert the differential pressure from the primary element into a stable, repeatable output signal and survive the process environment for years.
Start by calculating the maximum differential pressure the primary element will produce at the maximum expected flow, then choose a transmitter whose calibrated span covers that value with a safety margin. For general-purpose liquid, gas, and steam flow loops, a differential pressure transmitter like the PN55 provides a compact, well-proven solution with a 4-20 mA output and a rugged industrial housing.https://www.pakusensors.comShanghai Kayuan Electronic Technology Co., LtdView Product →
When the primary element generates only a small pressure drop, the transmitter needs a low span to make the reading usable. A pitot tube in a large duct or a low-flow liquid line can produce a full-scale differential pressure of only a few hundred pascals. In that situation, a micro differential pressure transmitter with a low-range sensing cell offers the resolution and stability that a standard-range unit cannot provide.https://www.pakusensors.comShanghai Kayuan Electronic Technology Co., LtdView Product →
In classified areas where flammable vapors may be present, the transmitter itself must carry an appropriate approval. Selecting an explosion-proof differential pressure sensor up front avoids the added cost of purged enclosures and simplifies the loop certification documentation.https://www.pakusensors.comShanghai Kayuan Electronic Technology Co., LtdView Product →

Regardless of the transmitter class, verify the wetted materials, the maximum static pressure rating, the ambient temperature effect on accuracy, and the availability of a local display for commissioning and diagnostics.
Even the best transmitter cannot compensate for a badly installed primary element. The meter run needs straight pipe upstream and downstream of the restriction, typically 10 to 20 pipe diameters upstream and 5 diameters downstream for an orifice plate, depending on the type and position of upstream fittings. When the straight run is insufficient, the flow profile is distorted and the discharge coefficient no longer matches the calibration data.
Impulse lines, which carry the upstream and downstream pressure to the transmitter, must slope upward for liquid services so trapped gas can escape, and downward for gas services so condensed liquid can drain. A three-valve or five-valve manifold lets the operator isolate the transmitter, equalize the pressures, and perform a zero check without shutting down the process. Regular zero verification and occasional inspection of the orifice plate for edge erosion, scaling, or damage keep the loop accurate over its service life.
For engineers new to the technique, it helps to review a guide to pressure sensors and their selection before finalizing a transmitter choice, and to browse the flow series product range to see how complete flow measurement loops are assembled in practice.
Differential pressure flow measurement does not offer the glamour of newer technologies, but it earns its place through predictability, standardization, and economy. The key to success is not sophisticated electronics. It is understanding the primary element, choosing a transmitter matched to the real differential pressure range, and following basic installation rules. When those three conditions are met, a DP flow loop often stays in service for decades with routine zero checks and occasional maintenance. For steam lines, large water pipes, and high-pressure gas services, that combination of simplicity and reliability is hard to beat.