In many liquid hydrocarbon applications, such as onshore and offshore pipelines, storage terminals and marine loading and unloading, surge relief systems are necessary to protect equipment, personnel and the environment from surge pressures generated by thermal expansion, valve closures, and pump trips. The system design must incorporate a complex range of factors including the potential for pressure increase, consideration of the volumes that pass by the pressure relief equipment, and the system capacity to contain pressure.

Rapid changes in flow velocity can produce rapid pressure surges. If these surges are not controlled immediately before they exceed the pressure limits, they can damage your equipment and become a serious safety and environment hazard (see figure 1).

Typical Pressure/Time Response with and without Surge Relief Protection
Figure 1: Typical Pressure/Time Response with and without Surge Relief Protection

A surge relief valve protects your system from build-up of pressure surges. Surge pressures are created from:

  • Closure of an automatic emergency shutdown device (ESD valve)
  • Rapid closure or opening of a manual or power operated valve
  • Slamming shut of a non-return valve
  • Starting or stopping of a pump

Consider these Factors Before Selecting a Surge Relief Valve

Selecting the right pressure relief valve for the intended application is extremely important. Factors that must be considered are:

  • Valve response time: Valve response time is extremely important in controlling peak surges and does vary by valve type. For instance, a gas-loaded relief valve is considerably faster than a pilot-operated valve.
  • Valve flow coefficient (Cv): Cv is a formula used to determine the correct size valve required and is defined as the quantity of water (in gallons/minute) that will flow through a wide open valve with 1 psi drop. It is recommended that the required Cv should not exceed 85% of the selected valve size actual Cv. Valve Cv varies by size type and manufacturer.
  • Excess pressure above set point to reach required flow rate: When line pressure exceeds the force (bias pressure) keeping the valve closed, the valve begins to open. As the valve opens, the bias force or pressure increases; so should the line pressure if the valve is to stay open. This bias force varies by type and operating characteristics, such as between a hydraulically balanced or unbalanced design of a valve.
  • Valve characteristic control curve: Defines the relationship between both opening and closing characteristics (strokes) of a valve and flow rate under constant pressure conditions. There are three characteristic control curves: linear, equal percentage, and fast. Valve stroke is the percent opening of the valve and is tied to percent flow (%Cv).

Choose Surge Relief Valves that Deliver Results

Although many design approaches can help alleviate surge pressure, a surge relief valve should be installed to protect your system. Some of the benefits of using Emerson’s Daniel surge relief valves include:

  • High flow capacities or coefficients (Cv) means smaller and / or fewer valves to save installation costs and weight
  • Fast response – rapid opening, controlled closing without slamming shut (allow the valve to “track the surge”)
  • Oil reservoir helps extend the life of the seals and in addition eliminates the possibility of nitrogen gas permeating the seals with reduced nitrogen consumption
  • Line pressure operated – no separate power source required
  • 45 degree valve design allows for vertical operation of the piston. This ensures that the valve opening does not get affected by debris when the valve cycles during an occasional surge
  • Ratio of nitrogen pressure to set pressure is 1:1 (less force exerted by spring)
  • Linear action valves are the preferred choice for surge control application
Left: Daniel Nitrogen Loaded Pressure Relief Valves. Right: Daniel Pilot Operated Pressure Relief Valves.
Figure 2: Left – Daniel Nitrogen Loaded Pressure Relief Valves. Right – Daniel Pilot Operated Pressure Relief Valves.

Valves such as Daniel Nitrogen Loaded Pressure Relief Valves are suitable for all types of petroleum products, including dirty or high viscosity products and have exceptionally fast response. They can also be used to maintain a minimum back pressure for more efficient operating conditions.  On the other hand, the Daniel Pilot Operated Pressure Relief Valves are suitable for low viscosity refined products, have relatively slow response, and are completely self-contained.

Optimize Your Pipeline Integrity with Complete Surge Relief Solutions from Emerson

Emerson provides effective solutions for surge systems to address the challenges of ensuring pipeline integrity and environmental protection, meeting regulatory requirements, maximizing pipeline capacity, and decreasing ownership costs.

From single valve installations to complex turnkey skid mounted solutions, Emerson’s surge relief systems are a single-source solution proven to minimize risk and deliver precise control.

Each of Emerson’s surge relief systems is designed to specific requirements using a complete hydraulic transient analysis to meet the challenges of today’s petroleum and environmental needs. For more information on Emerson’s surge relief technologies, systems, and services, please review this guide.

To learn more about modular surge relief solutions that ensure pipeline pressures do not exceed the Maximum Allowable Operating Pressure (MAOP) of the system, check out this webinar replay.

Packaged, easy-to-integrate surge relief systems from Emerson provide comprehensive surge protection and flow measurement to ensure pipeline integrity and HSE protection.
Figure 3: Packaged, easy-to-integrate surge relief systems from Emerson provide comprehensive surge protection and flow measurement to ensure pipeline integrity and HSE protection.