IMAGE 3: PCV with electric motor operator and downstream swing check valve
Learn what situations may call for check valves or pump control valves.
DeZurik, Inc.

Surge protection is a critical element in the design and operation of pumping systems. Pressure surges, commonly referred to as water hammer, are caused by abrupt changes in fluid velocity. These pressure surges pose significant risks to pipelines, pumps and associated equipment. Effective surge protection mitigates these risks, which ensures operational efficiency and system longevity. Selecting the most suitable device, such as pump control valves (PCVs) or check valves, is essential to managing surge dynamics effectively. 

This article examines the principles of surge protection and evaluates the advantages and limitations of PCVs and check valves. Additionally, it provides guidance for selecting the appropriate system solution based on specific application requirements.

IMAGES 1a-1d: The above graphics depict wave travel and the pressure changes during downsurge and upsurge periods (Images courtesy of DeZURIK, Inc.)
IMAGES 1a-1d: The above graphics depict wave travel and the pressure changes during downsurge and upsurge periods (Images courtesy of DeZURIK, Inc.)

Understanding Surge Dynamics

Pressure surges occur whenever fluid velocity in a pipeline changes rapidly. This generates transient waves that move through the system, causing fluctuations in pressure. These pressure fluctuations can place stress on pipeline infrastructure, leading to mechanical failures. Surges can cause pipeline deformation, ruptures, equipment damage, cavitation and higher maintenance costs. 

Common causes of pressure surges include abrupt pump starts or stops, rapid valve opening and closures and unexpected power failures. These events create sudden shifts in flow velocity, which disrupt the hydraulic equilibrium of the system. For example, when a pump stops suddenly, the momentum of the moving fluid continues, generating a surge wave that travels back through the pipeline. Several factors affect the magnitude of these surges. These include pipeline characteristics, the rate of change of fluid velocity and system design. 


Surge protection devices maintain system stability. These devices include PCVs, check valves, surge relief valves, surge tanks and control valves. They absorb excess energy, dissipate pressure waves and regulate flow during transient events. Images 1a-1d show the fluid pressure dynamics between a pump, a check valve and a large reservoir during a shutdown. 

IMAGE 2: Valve selection guidelines based on design criteria
IMAGE 2: Valve selection guidelines based on design criteria

PCVs: Precision Flow Management

PCVs control fluid velocity changes during normal operation and prevent reverse flow on pump stop. They rely on a powered actuator for flow control and require stored energy for power failures. Actuators are commonly hydraulic but could also be pneumatic or electric. 

PCVs are critical during pump startup and shutdown, where they minimize fluid velocity changes and pressure spikes. This controlled operation reduces the risk of surges and related system stress. To prevent reverse flow, PCVs incorporate a check feature that closes smoothly when the pump stops. 

PCVs can also improve energy efficiency by minimizing pressure losses and reducing unnecessary pump cycling. This extends the service life of the equipment. It also decreases maintenance requirements and operational wear, leading to overall          cost savings.

Check Valves: Simplified Surge Mitigation

Unlike PCVs, check valves are simpler, flow-dependent devices designed to prevent reverse flow. Their operation is based on differential pressure and utilizes various mechanisms such as swing, piston or spring-loaded discs. Spring-assisted closure valves provide rapid response to reverse flow, ensuring minimal backflow. In contrast, slow-closing, oil-dampened check valves allow limited reverse flow while effectively reducing slam and limiting pressure surges.


Check valves have fewer moving parts, require less maintenance and are compact and cost-effective. They are common in fire protection systems, booster pump systems, variable frequency drive (VFD) pump systems and gravity-fed pipelines; however, they do not regulate flow like PCVs and can cause secondary pressure waves when closing rapidly. Supplementary dampening measures may be required in some applications, thereby increasing overall costs. 

IMAGE 3: PCV with electric motor operator and downstream swing check valve
IMAGE 3: PCV with electric motor operator and downstream swing check valve

PCVs vs. Check Valves

Valve selection depends on system operational characteristics such as flow rates, pressure conditions and the frequency of flow variations. PCVs are ideal for systems experiencing frequent flow changes, as they can be remotely adjusted to maintain stability and protect against pressure surges or drops. In contrast, check valves are suited for applications with relatively constant flow rates, primarily preventing backflow to safeguard equipment.

In high-risk systems, such as those with long pipelines or high fluid velocities, PCVs offer superior protection by dynamically responding to sudden pressure or flow velocity changes. For systems with moderate surge risks, check valves equipped with dampening devices help maintain unidirectional flow while minimizing slam-related damage.

In addition to system dynamics, budget constraints and maintenance resources influence valve selection. PCVs involve higher upfront costs but offer long-term operational savings through enhanced energy efficiency and reduced mechanical wear. On the other hand, check valves present a cost-effective initial investment. However, they may require additional surge mitigation measures that may potentially offset their cost advantage.

Regulatory and safety requirements also influence valve selection. Industry and compliance standards may mandate specific surge protection devices. Evaluating these requirements alongside system-specific factors ensures the valve solution aligns with operational and compliance objectives. Additionally, conducting a surge analysis with input from valve manufacturers provides valuable insights, helping to determine the most effective system solution. Refer to Image 2 for guidance on selecting valves.


Additional Surge Solutions

In certain cases, a combination of PCVs and check valves may be utilized to achieve optimal surge protection, as seen in Image 3. PCVs can manage flow changes during normal operations, while a check valve offers mechanical backup protection against reverse flow upon power loss. Additional devices such as air release valves, VFDs or hydropneumatic surge tanks can improve system resilience. These integrated solutions address the limitations of individual components, ensuring comprehensive surge protection.

Effective surge protection is a vital aspect of pumping system design, ensuring operational efficiency, equipment longevity and overall system safety. Pumps require the installation of either check valves or PCVs to prevent reverse flow, mitigate water hammer and protect system components from pressure surges. When there is not a likelihood for surges to happen during normal operation, check valves are typically used. If there is potential for surges to happen during normal starting and stopping, then a PCV may be suggested.

PCVs excel in complex fluid systems, providing precise regulation of fluid velocity changes to mitigate surges during pump operation. They are ideal for high-risk applications but involve higher initial and maintenance costs. Check valves, by contrast, are simple, cost-effective devices designed to prevent reverse flow. While suitable for steady state systems, they lack the flow regulation needed to manage surges and may require additional dampening measures.

Selecting the appropriate solution depends on system requirements, surge potential, reverse flow prevention and budget. In some cases, combining PCVs, check valves and supplemental surge control measures provides the most comprehensive protection. To design effective solutions, each pumping system must be evaluated individually, considering its unique operational demands and specific surge risks. 

A thorough analysis of system dynamics helps ensure the selection of the most suitable valve. Collaborating with valve manufacturers during the design phase provides critical insights into optimal system configuration, enhancing both operational efficiency and system integrity.  


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