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Thread: Hydrocarbon Losses Quantification (Low Pressure Storage)

  1. Hydrocarbon Losses Quantification (Low Pressure Storage)

    Hi,

    Any ideas / calculation methodology to estimate hydrocarbon losses out large diameter liquid storage tanks? I need to quantify any dampening to vapor generation considering factors such as insulation.

    Thanks a lot.

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  3. Re: Hydrocarbon Losses Quantification (Low Pressure Storage)

    Th3 equation i liked is w=370×(deltaP ×density ×d^5)^0.5
    W=flow in lb÷h
    DeltaP=friction loss in lb÷in^2(psi) per 100 ft
    Density
    D=inside diameter of pipe in inches
    This is a form of Fanning or Darcy formula with friction factor=0.0055
    This friction factor corresponds to approximately the following
    Commercial steel pipes
    No. Reynolds=10^5
    Williams and Hazen C factor=110
    For other friction factors multiply the right sid3 for
    (0.0055÷friction factor)^0.5
    The friction factor can b3 approximaTed by
    Laminar flow f=16÷Re
    Commercial pipes f=0.054÷Re^0.2
    Smooth tubes f=0.046÷Re^.2
    Extremely rough pipes f=0.013
    Where Re is the well known. In this case
    Friction factor=hl÷(4×(L÷D)×(u^2÷(2g)))
    hl÷friction head in feet
    L length in Feet
    D diameter in feet

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  5. Re: Hydrocarbon Losses Quantification (Low Pressure Storage)

    Be careful wh3n applying the friction factor. Sometim3s it is d3finid aa
    f=hl÷((L÷D)(u^2÷(2×g))
    For compressible fluids fo3 non critical flow deltap less to 10% P1
    P1= upstream pressure, psia
    If deltaP major to 10% P1
    DeltaP=P1-P2=2×P1÷(P1+P2)×(0.323×(fL÷d+ln(P1÷P2)÷24× S1×U1^2)
    Assusme isothermal flow of ideal gas
    S1 especific gravity
    d pipe diameter
    f friction factor
    L length of pipe
    DeltaP=Pressure dropt 7n psi
    M m8lecular wt.
    P1,P2=Upstream and downstream pressure in psi ABS
    S1 relative to water = 0.00150

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