PRDs- Terminology Accumulation: Increase pressure over MAWP during discharge (% of MAWP) Set Pressure: Difference between Set Pressure and Re-Seat Pressure Back Pressure: Pressure on discharge side (% of set pressure) Built up Pressure: Pressure in discharge header due to frictional loss Superimposed Pressure: Pressure in discharge header before valve open Blowdown : Difference between Set Pressure and Re-Seat Pressure
PRDs- Terminology (2) Chatter: Rapid reciprocating motion of the movable parts ( i.e. disk contacts with seat ) Lift: Increase pressure over MAWP during discharge (% of MAWP) Over Pressure: Pressure on discharge side (% of set pressure) Releasing Pressure: Pressure in discharge header due to frictional loss Seat tightness Pressure: Pressure in discharge header before valve open
PRESSURE TERMS & SETTINGS MAWP Design Pressure Operating Pressure Set Pressure Overpressure Accumulation Blowdown Where is Operating Pressure ? Any practical level below MAWP
PRESSURE RELIEVING DEVICES Safety valve The spring load is equal to force exerted on the closed disk by inlet fluid, at set pressure. Opens when inlet pressure exceeds the set pressure, overcoming the spring force Re-seats (close) at inlet pressure below the set pressure Used for general air and steam service.
PRESSURE RELIEVING DEVICES Safety valve Limits – Should not be used in the following services: Corrosive refinery service (unless isolated from the process by a rupture disk). Back pressure service. Where the discharge must be piped to remote areas. In liquid service. As pressure control or bypass valve.
PRESSURE RELIEVING DEVICES Pilot O perated PRV A pressure relief device whose main relieving valve is controlled by a small spring-loaded pressure relief valve. The pilot and the main valve may be mounted on the same connection or separately . Clifford Matthew’s Quick Guide
PRESSURE RELIEVING DEVICES Pilot O perated PRV Limits – Should not be used in the following : In-service where the fluid is dirty. Viscous service. With vapor that will polymerize. Where temperatures exceed the limits of the valve disks or diaphragms . Where corrosion build-up can impede the actuation of the valve.
PRESSURE RELIEVING DEVICES API 576 covers 5 types of rupture disks . Conventional rupture disk 4.10.2.1 Scored tension-loaded rupture disk 4.10.2.2 Composite rupture disk 4.10.2.3 Reverse-acting rupture disk 4.10.2.4 Graphite rupture disk 4.10.2.5 Rupture Disc Predetermined weak point in a pressurized system Solid material (see below) Open at Burst Pressure Does not re-seat (close)
CODE REQUIREMENT Relieving pressure shall not exceed MAWP (accumulation) by more than : 3% for fired and unfired steam boiler 10% for vessels equipped with a single pressure relief device 16% for vessels equipped with multiple pressure relief device 210% for fire contingency
PRD – INSPECTION FREQUENCY To ensure proper performance, a definite time interval between inspections should be established for every pressure relieving device on operating equipment . The maximum interval established in API 510 is 10 years but also states that the interval should be determined by the performance of the device.