Pressure Relieving Systems (PSV)
Guidelines on pressure safety valves (PSVs), backpressure management, API standards, and relief scenarios for overpressure protection.
Fundamentals of Pressure Relieving Systems
Pressure relieving systems, centered on Pressure Safety Valves (PSVs), safeguard equipment from overpressure by venting excess fluid to flares or vents. API standards like 520 (sizing/installation) and 521 (scenarios/depressurizing) provide essential frameworks, ensuring compliance with ASME codes.
PSV Types and Selection
- Conventional Spring-Loaded: For constant backpressure <10% set pressure.
- Balanced-Bellows: Handles variable backpressure 21–50% set pressure.
- Pilot-Operated: Up to 70% variable backpressure; ideal for clean, high-ΔP services.
- Pair with rupture discs upstream for corrosion protection or leakage prevention—weep holes monitor disc integrity.
Key terms:
- Set Pressure: Inlet pressure triggering opening.
- MAWP: Maximum Allowable Working Pressure.
- Accumulation: Pressure rise over MAWP during relief (≤10% non-fire contingency; per API 521).
Backpressure Considerations
- Superimposed: Pre-relief header pressure.
- Built-Up: Flow-induced post-opening rise. Exceeding 10% on conventional PSVs reduces lift/capacity; chattering (rapid open/close) stems from inlet ΔP >3% set pressure—size orifices conservatively to avoid.
Relief Scenarios and Sizing
Common causes: Blocked outlets (inlet flow continues), tube rupture (high-P leak to low-P side), instrument failure (controller malfunction), thermal expansion (blocked/heated liquids).
- Fire Case: Heat input via wetted area; assume saturated vapor T if unknown; insulation credit reduces flux.
- Flashing Liquids: Use HEM model for two-phase flow.
- Oversizing Risks: Instability/chattering damages seats.
System Components
- Inlet piping ΔP ≤3% set pressure (API 520).
- Flare K.O. drums remove liquids pre-flare.
- Depressurizing/Blowdown: Rapid inventory reduction in emergencies (API 521).
- Orifice Designations: API 526 (D–G series).
Coefficient of discharge (K_d) factors into flow equations. Choked flow (sonic velocity) caps mass flow independent of downstream P.
These flashcards target API-compliant practices and troubleshooting for reliable relief.
According to API RP 520, what is the maximum allowable pressure drop in the inlet piping to a pressure relief valve?
The pressure drop in the piping between the protected equipment and its relief valve shall not exceed 3% of the set pressure.
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