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  • Users: LuNL
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  1. LuNL

    Shell and tube HE tube rupture scenario

    Dear Engineers I have encountered a scenario study for tube rupture inside the shell and tube heat exchanger. tube side : LNG 8 barg, -157 C in, and 25 C gaseous out shell side: water/glycol, 2.5 barg, 55 C in and 35 out. I assume the possible rupture will be on the back side of the tube...
  2. LuNL

    PSV sizing using standard cubic meter per hour but confused by the working fluids

    Hi dear all Recently I got a interesting question from engineers. While doing the sizing calculation for pressure safety valves, I assumed if I use standard cubic meter per hour, it should be okay no matter the fluid is air, or other industrial gases, like GNG. Since the molar volume at...

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