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    113 80 330 FD 202 - Rev1 17

    Uploaded by

    Maria Eduarda Andrade

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    © All Rights Reserved
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    113 80 330 FD 202 - Rev1 17

    Uploaded by

    Maria Eduarda Andrade
    20 views1 page

    Original Title

    113-80-330-FD-202_Rev1-17

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    © © All Rights Reserved

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    20 views1 page

    113 80 330 FD 202 - Rev1 17

    Uploaded by

    Maria Eduarda Andrade

    Copyright:

    © All Rights Reserved
    Download as PDF, TXT or read online from Scribd
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    Nº Rev.

    CALCULATION SHEET MC-2041118-001-CB 0


    CUSTOMER: SHEET:
    SIEMENS LTDA. 2 of 6
    TITLE:

    CONTROL VALVE
    v.2.0.0.0
    Valve/Regulator Sizing Calculation
    Customer: SIEMENS LTDA Emerson Process Mgt Brazil
    Contact: Contact: Diego Domingues
    Customer Reference: Projeto Galvani - Siemens Sales Office Reference: Lead Time:
    Item: 1 Rev: Qty: 1 Quote: 122-DD-161212-0029190/(No Name Rev: 3
    Assigned)
    Tags: 113-330-PV-024 Date Last Modified: 02/15/2017
    Description: NPS 2 HPS 667 Size 40i 67CF Series Acc
    Service Description: Válvula de controle de selagem posterior

    Sizing Type: Ideal Steam Flow is Turbulent Solving for: Cv Noise is IECAerodynamic Flow is Mass
    Variable Name Units Minimum Normal Maximum
    SERVICE & SIZING
    Inlet Pressure (P1) kg/cm2g 48.30000 48.30000 53.00000
    Outlet Pressure (P2) kg/cm2g 2.10000 2.10000 2.20000
    Inlet Temperature (T1) deg C 312.0000 399.0000 407.0000
    Mass Flow Rate Gas (w) kg/h 272.2000 250.6000 237.6000
    Pressure drop ratio factor (Xt) 0.611 0.611 0.611
    Pressure Recovery Factor (Fl) 0.960 0.960 0.960
    Valve style modifier (Fd) 0.350 0.350 0.350
    Atmospheric Pressure psi 14.69 14.69 14.69

    Pipe Size Up in 4 4 4
    Pipe Schedule Up 80S 80S 80S
    Pipe Size Down in 4 4 4
    Pipe Schedule Down 80S 80S 80S
    Nominal Valve Diameter (dv) in 2.000 2.000 2.000
    Aerodynamic Distance (Rn) m 1.000 1.000 1.000

    Sizing Coefficient (Cv) 0.624 0.635 0.552


    % Open 70 70 66
    dP Choked kg/cm2 28.63534 28.63535 31.36344
    dP/P1 Valve 0.936 0.936 0.940
    Specific heats ratio (gamma) 1.330 1.330 1.330
    Molecular Weight/Specific Gravity M 18.010 18.010 18.010
    Inlet fluid density (Rho1) kg/m3 20.45 16.72 18.16
    Fp 1.00 1.00 1.00

    NOISE CALCULATION
    Valve/Trim Globe/Angle Globe/Angle Globe/Angle
    LpAeTrim1m dB(A) 79 78 78
    LpAeOutlet1m dB(A) < 50 < 50 < 50
    LpAeValve1m dB(A) 79 78 78
    LpAValveRn dB(A) 79 78 78

    VELOCITY OUTPUTS
    Valve Outlet Area(Ao) in2 2.800 2.800 2.800
    M1 Pipe Mach 0.001 0.001 0.001
    Mo Valve Mach 0.057 0.059 0.054
    M2 Pipe Mach 0.014 0.014 0.013
    V1 Pipe m/s 0.4984 0.5614 0.4900
    Vo Valve m/s 32.5544 36.5989 33.9251
    V2 Pipe m/s 7.9285 8.9135 8.2623
    C1 Pipe m/s 599.5784 642.6070 646.4199
    Co Valve m/s 567.0098 624.7955 627.5557
    C2 Pipe m/s 567.0098 624.7955 627.5557
    WARNINGS
    Note: The Note: The Note: The
    downstream downstream downstream
    temperature is temperature is temperature is
    estimated on the estimated on the estimated on the
    basis of a constant basis of a constant basis of a constant
    enthalpy expansion enthalpy expansion enthalpy expansion
    across the control across the control across the control
    valve. valve. valve.
    Item Notes:

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