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Thread: Blowdown calculation

  1. Blowdown calculation

    Anyone know where to look for some equations pertaining to blowing down a vessel. What I am looking for is what happens to the LNG in the vessel as the pressure is released and the fluid is sent to a flare.
    All I could find was in API 521 where it talked about depressurization, but the calculation had heat included, which I would not
    Anyone have any ideas

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  3. #2

    Re: Blowdown calculation

    I was asked to calculate ***hing simmilar - the time to depressurise a gas pipeline.
    Now my situation its simpler (I have only gas - no phase changes)
    My steps were as follow:
    Calculate standart system volume at initial conditions (Pi; ti - std m3)
    Calculate standart system volume at final conditions (Pfn; tfn - std m3)
    Set the number of steps (n) which system will follow during depressurising Pi to Pi-n..... to Pf
    Calculate compressibility factor for each of new sets of conditions which system will follow during depressurising
    Calculate the volume difference in system between each step of condition Vi - Pi-n (V diff - std m3)
    Given the system set of conditions (P, t) and the valve or oriffice parameters - calculate the flow time

    Cumulative time is your total depressurising time. Calculations will look similar as table below:

    P Z Volume Volume (std) Vdiff t cumm time
    100 0.7 1000 5000
    800 0.75 800 4000 1000 20 20
    600 0.8 600 3000 1000 18 38

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