Relief Capacity of Rupture disc and relief valve

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SUMMARY

The discussion focuses on calculating the relief capacity of a 10" rupture disc and relief valve set at 180 psig, venting into the atmosphere with water at 140°F. The user encountered discrepancies between the ASME and API equations, yielding capacities of 10,200 Klb/hr and 2,200 Klb/hr, respectively. The user seeks clarification on which equation is appropriate, emphasizing that the BPVC should take precedence in this scenario. The discussion highlights the importance of selecting the correct methodology for accurate relief capacity calculations.

PREREQUISITES
  • Understanding of rupture disc and relief valve functionality
  • Familiarity with ASME and API equations for pressure relief
  • Knowledge of fluid properties, specifically water at 140°F
  • Basic principles of pressure vessel code (BPVC) compliance
NEXT STEPS
  • Research the ASME and API equations for pressure relief capacity calculations
  • Study the BPVC guidelines relevant to rupture discs and relief valves
  • Learn about the Crane Technical Paper for pressure relief calculations
  • Explore case studies on discrepancies in relief capacity computations
USEFUL FOR

Engineers, safety professionals, and designers involved in pressure relief systems, particularly those working with rupture discs and relief valves in industrial applications.

martane
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I need to compute for the relief capacity (gpm or lb/hr) of a 10" rupture disc with relief valve set at 180psig. Vented out into the atmosphere. Assume fluid is water at 140F. I tried using ASME and API Equation but they give different answers. Can someone tell me the correct answer and what equation to use. Thankd
 
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at 180psig, I would imagine BPVC would take precedence.
 
What was the capacity you computed? Using eq. From crane i computed 10200 Klb/hr from ASME i computed 2200 Klb/hr.
 

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