News Center

——  NEWS CENTER  ——

News Center
Contact Us

Xi'an Shenghongchuang Instrument Co., Ltd.

Contact: Mr. Zhang

Mobile: 15529283736
Email: shc-sensor@qq.com

Address: Fortune Building, Sanqiao Street, Xixian New Area, Xi'an, Shaanxi Province

Can a differential pressure transmitter for constant-pressure water supply reduce frequent water pressure fluctuations?
Added to Favorites:125

After a project is delivered, the issue most likely to trigger complaints is often not "no water," but fluctuating water pressure: flow at the end of the network decreases during peak periods, while pressure surges during low-demand periods; variable-frequency pumps repeatedly accelerate and decelerate, pipelines occasionally vibrate, and the maintenance frequency of valves and pumps also increases. When facing such issues, many project managers ask: Can a differential pressure transmitter for constant-pressure water supply reduce frequent water pressure fluctuations?

The answer is: A differential pressure transmitter does not directly "eliminate" fluctuations, but it can convert pressure differential changes that are otherwise difficult to assess into continuous and reliable control signals, providing a speed-control basis for variable-frequency drives, PLCs, or controllers. When measuring points are properly selected, control logic is appropriately matched, and pipeline network conditions are basically sound, a differential pressure transmitter for constant-pressure water supply can significantly improve pressure fluctuation problems caused by uncontrolled differential pressure. If only the instrument is replaced without addressing root causes such as pump set selection, PID parameters, and pipeline leakage, the effect will be limited.

First distinguish: does the system require "constant pressure" or "constant differential pressure"?

Constant-pressure water supply does not mean that the pressure at every location must be exactly the same. Building or industrial park pipeline networks differ in pipe diameter, length, elevation difference, and instantaneous water demand. As flow rate increases, both friction losses and local resistance change. Even if the pump room outlet pressure is stable, the pressure at the most unfavorable point may drop; conversely, when water demand is low, pressure near the source may be relatively high.

A standard pressure transmitter typically measures the gauge pressure in a certain pipe section and is suitable for applications where the pump room outlet pressure, pressure tank pressure, or terminal pressure is the main control target. A differential pressure transmitter for constant-pressure water supply, however, measures the pressure difference between two pressure tapping points and is more suitable for determining whether "water supply is truly delivered where needed." For example, the differential pressure between the main supply and return water pipes, before and after a pump, or before and after a filter can all reflect the operating condition of the system.

For water supply systems that need to maintain a supply-return differential pressure, a zoned differential pressure, or experience significant changes in terminal operating conditions, a differential pressure signal is more informative than single-point pressure. It enables the control system to focus not only on one value at the pump outlet, but also to detect actual transmission resistance and demand changes in the pipeline network.

Why does water pressure fluctuate frequently? The instrument is only one part of the system

Common on-site fluctuations are not all caused by insufficient sensor accuracy. Before determining the retrofit direction, project managers are advised to analyze the issue separately.

  • Sudden changes in water demand: Simultaneous startup and shutdown of multiple devices, shifts in centralized water-use periods, and rapid valve opening and closing can all cause instantaneous flow changes.
  • Pump set and pipeline network mismatch: Excessive pump head margin, excessive flow from a single pump, or prolonged low-flow operation can easily result in pressure surges and frequent startup and shutdown.
  • Inappropriate control parameters: If the PID proportional gain is too high, the system will "respond too aggressively"; improper integral settings may cause slow oscillation and repeated correction.
  • Unreasonable measuring point location: If the pressure tapping port is near the pump outlet, an elbow, a valve, or a highly disturbed area, the reading may not represent the actual condition of the pipeline network.
  • Interference in the signal chain: Improper handling of variable-frequency drives, motors, cable routing, or grounding methods may cause the controller to receive fluctuating signals.
  • Mechanical and pipeline network issues: Abnormal check valve operation, failure of a bladder tank, air ingress into pipes, filter clogging, or leakage can also amplify pressure fluctuations.

Therefore, the value of a differential pressure transmitter lies in providing reliable process data rather than replacing hydraulic design and control commissioning. A stable measurement signal can prevent a variable-frequency drive from repeatedly adjusting speed due to misjudgment; however, if the system itself has water hammer, severe leakage, or an unsuitable pump type, these issues must also be addressed.

How differential pressure signals participate in constant-pressure water supply control

A common application method is to install a differential pressure transmitter between two pressure points that require priority assurance, and connect its 4–20 mA or other standard signal to a variable-frequency control cabinet, PLC, or intelligent digital display control instrument. The controller compares the real-time differential pressure with the set differential pressure: when the differential pressure is below the set value, pump speed is appropriately increased; when it is above the set value, pump speed is reduced or the operating pump set is switched.

This closed-loop adjustment is not simply "speed up when low and slow down when high." In actual projects, reasonable filtering, deadband, and response time should be set for signals to prevent temporary disturbances from being excessively amplified. For example, an instantaneous differential pressure change caused by rapid operation of a local valve does not necessarily require the pump to immediately make a major speed adjustment; the controller should make smooth corrections based on system inertia.

For parallel multi-pump water supply, differential pressure signals can also be used to determine when to add or remove pumps. When a single pump is operating close to high frequency and the differential pressure remains continuously low, the next pump can be activated according to the control logic; when demand declines and the differential pressure remains stably high, some pump sets can then be gradually taken offline. This approach better matches actual load than relying only on timed switching and can also reduce mechanical impacts caused by frequent startup and shutdown.

Five key points project managers should confirm during selection

First, do not simply assume that a larger measuring range is safer. If the range is too large, the normal operating range accounts for too small a proportion, affecting control resolution; if the range is too small, it may be exceeded during pressure surges. The range should be determined comprehensively based on the design differential pressure, normal fluctuation range, and possible peak values.

Second, consider the medium and wetted materials. For conventional clean water supply, a structure compatible with water media may be used; if the water contains impurities or disinfectants, or there is a risk of corrosion, attention should be given to wetted materials, seals, and the resistance of pressure tapping components. For systems prone to scaling, maintenance and drainage provisions should also be reserved.

Third, confirm static pressure and overload capacity. Differential pressure measurement focuses on the pressure difference between two sides, but the actual pipeline pressure borne by both sides may not be low. Under high static pressure conditions, do not look only at the differential pressure range; the allowable static pressure of the instrument and one-sided overpressure conditions must be verified.

Fourth, emphasize compatibility between output and the control system. Whether the existing control cabinet uses 4–20 mA, RS485, or another communication method directly affects wiring, commissioning, and subsequent diagnostics. Industrial sites should also consider shielded cables, separate cable routing, reliable grounding, and power supply stability to reduce electromagnetic interference from variable-frequency equipment.

Fifth, ensure that the installation location serves the control objective. If the objective is to ensure water supply at the most unfavorable point, priority should be given to collecting data from a location that represents terminal demand; if the objective is to stabilize the supply-return differential pressure, the two pressure tapping points should avoid areas of obvious disturbance, and the impulse piping should be kept unobstructed and free from significant air accumulation or blockage.

A more prudent approach to retrofit assessment

For existing constant-pressure water supply projects, it is not advisable to assume from the outset that a differential pressure transmitter must be replaced. A more practical approach is to continuously record outlet pressure, pressure at key terminals, pump frequency, number of startups and shutdowns, and flow changes during major periods, then identify whether fluctuations occur during peaks, valleys, or after specific equipment starts and stops.

If the pump room outlet is stable but terminal pressure is insufficient, or if water supply performance varies significantly among different branches, differential pressure control is often more meaningful. If the outlet pressure itself continues to fluctuate, priority should be given to checking the pressure transmitter measuring point, variable-frequency PID parameters, pressure stabilization facilities, and pump operating conditions. Where increased filter pressure loss reduces water supply capacity, differential pressure monitoring can also be used to establish maintenance warnings rather than waiting until obvious water shortage occurs at the terminal.

Xi'an Shenghongchuang Instrumentation Co., Ltd. and its production base, Shaanxi Qinkong Sensor Technology Co., Ltd., can provide supporting measurement and control products and non-standard adaptation support for pressure, differential pressure, liquid level, and control display requirements in water supply systems. For retrofit projects, what deserves greater attention is not a single instrument model, but whether the instrument range, installation method, signal integration, and existing control logic can form a complete closed loop.

Conclusion: It can improve fluctuations, provided it is used in the right location

A differential pressure transmitter for constant-pressure water supply can help the system identify actual differential pressure changes and provide feedback signals for variable-frequency adjustment of pump sets that more closely reflect pipeline network demand, thereby reducing ineffective speed regulation and some pressure fluctuations. It is particularly suitable for projects with demand-sensitive terminals, long pipeline networks, complex multi-branch distribution, or a need to maintain supply-return differential pressure.

For engineering project managers, the most reliable decision is not merely to ask whether to install one, but to first clarify the control target, source of fluctuations, and key assurance points. Only by checking the differential pressure transmitter, variable-frequency control, pump set operating strategy, and on-site pipeline network conditions together can a constant-pressure water supply system move from "barely maintained" operation to a more stable and maintainable state.

Submit