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Recent content by laliyo

  1. laliyo

    Distance between rupture disc and PSV

    Thanks all. I did move away from this alternative since the RD and PSV are not close coupled.
  2. laliyo

    Distance between rupture disc and PSV

    Hello, Does anyone know if a rupture disc can be installed at a larger distance from PSV ? I am thinking of installing a rupture disc on a STHE-2 (see the sketch), which is not in use on shell side and hence empty, but still being used on tube side. So a tube rupture case is valid.Presently...
  3. laliyo

    Activated carbon bed

    thanks everyone for their reply. The app is for gas phase (mostly air with around 100-300 ppm of VOCs) ,24/7 operation. Other thing is , the air is totally saturated with water vapor . Based on preliminary sizing, looks like 2 m in diameter and 3-4 m in height(for 12-14 weeks of service). We...
  4. laliyo

    Total condenser - tube rupture case

    Hello, I have a total condenser (inlet 100 % vapor - Outlet 100% Liquid), where based on design pressure ratio of Shellside/Tubeside, the catastrophic tube rupture is a valid case. Now , if the fluid is 100% vapor on both side or 100 % liquid on both side or 2-phase on both side, I know how to...
  5. laliyo

    Activated carbon bed

    Hello, Does anyone has experience with activated carbon bed installation? we are doing some investigation of carbon bed and my question is , can it be installed outdoors where ambient temperatures can go as low as -40 deg C ? thanks
  6. laliyo

    Pressure drop through an adsorber

    Sorry...the link is not working. I will upload it......http://files.engineering.com/getfile.aspx?folder=72dc2393-de04-412e-aac0-0e72014a9c5b&file=adsorption.ppt
  7. laliyo

    Pressure drop through an adsorber

    I think attached PP presentation might help you......http://www.ees.ufl.edu/homepp/cywu/env4121/adsorption.ppt
  8. laliyo

    Minimum flow over Carbonbed adsorber

    your heat generation in he bed will depend upon type of contaminants in air.Each specie will have a different heat of adsorption. I believe, if your air flowrate and VOC concn vary constantly,it would be difficult to come at a perticular number of flow... Best you can do is keep a certain...

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