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  • Users: hal1981
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  1. hal1981

    Reducing pressure of liquid in constant temperature

    Hi We have an ammonia vessel @ 150 bar and -23 C connected to another vessel @ 18 bar and -23 C. level of first vessel controlled by liquid output and pressure of second vessel controlled by manipulating output gas flow rate of this vessel. Ammonia input flow rate of second vessel is 42117 kg/h...
  2. hal1981

    heat exchanger input output orientation

    Hi! How can I find hot/cold input/output line of heat exchangers? Thanks!
  3. hal1981

    vent and minimum flow

    Hi! i see a pumps used in ammonia storage (LPS) have a both vent line and minimum flow line. Vent line back to storage where the suction line came, but minimum flow line return to the storage top! What is the difference between this lines?
  4. hal1981

    H2S stripper tower

    Hi all, i worked in Ammonia unit, and we have a small H2S removal section. H2S stripper tower in this section has a thermosyphon reboiler warm up by steam. A small flash drum installed on top of stripper. When a liquid level of flash drum increased, the top temperature of stripper decreased. I...
  5. hal1981

    what is the diffrence between orifices!

    Hi all! does any one can explain difference between swaged orifice, restriction orifice and line sized orifice!
  6. hal1981

    centrifugal electric motor driven pump

    Hi all i'm very confused about centrifugal electric motor driven pump! what happened to pump amperage, when discharging valve closed 50% and less 10%? thanks

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