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  1. ReliefSystemEngineer

    Emergency / Vacuum Vents Sizing ( Low Pressure Tanks)

    Hi, I'm working on Emergency / Vacuum Vents sizing on Low Pressure Tanks. I need help / guidance with calculations of relief rate for the following two cases: 1]Filling Hot Tank with Cold Liquid 2]Hot Feed to tank on startup with cooler material in tank. How do I calculate the relief rate for...
  2. ReliefSystemEngineer

    Relief Valve on Steam Header

    Hi All, Should their be a Relief Valve after a Steam Letdown Station on a Steam Header(in general) ? We are planning to merge a 35#Steam Header into an Abandoned 15#Steam Header. The idea is to install a 35# -15# Letdown station on the 18" 35#Steam Header. The 15# Steam will be used by various...
  3. ReliefSystemEngineer

    Non-ASME Relief Valves

    Hello, For a Non-ASME Relief Device(Set@ 2psig) Protecting a Non-ASME Ceritified Vessel(MAWP 2psig @ 270ºF) is the 3% and 10% RULE for INLET & OUTLET PIPING PRESSURE DROP APPLICABLE ? Thanks, Parimal
  4. ReliefSystemEngineer

    Pressure Increase in Thermal Relief

    Hello Everybody, I have a relief device protecting the tube side of a shell & tube heat exchanger(Process Water Heater). The Fluid Composition is as follows:- Tube Side - Water(90 psig normal operating, max. 150 psig) heated from 50 to 60ºC. Shell Side - 35#Steam. Relief Device Set @ 150 psig...

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