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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...- LuNL
- Thread
- Replies: 17
- Forum: Boiler and Pressure Vessel engineering
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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...- LuNL
- Thread
- Replies: 7
- Forum: Safety Relief Valve engineering (PSV)
