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Application Notes K V coefficient · Valve sizing Calculation of the valve flow coefficient K V The procedure specified in the IEC 60534 standard is applied to determine the valve flow coefficient K V . The relevant device-spe- cific data can be found in the associated data sheets. The equations below are given to allow a preliminary, simpli- fied calculation of the valve flow coefficient to be performed. Please note that these equations do not take account of the influ- ence of the connection fittings and the flow limitation in case of critical flow velocities. Selection of the valve flow coefficient K VS On the basis of the calculated valve flow coefficient K V , the ap- propriate valve flow coefficient K VS for the relevant valve type can be selected from the associated data sheet. If realistic operating values have been used for the calculation, the following applies in general: For self-operated regulators: K Vmax = 0.75 · K VS For motor-operated valves: K Vmax = 0.9 · K VS Edition March 2012 Application Notes AB 05 EN p 1 Upstream pressure p 2 Downstream pressure H Travel V . Volume flow rate in m³/h (gases) W Mass flow rate in kg/h (liquids, steam) r Density in kg/m³ (general, also in liquids) r 1 Density upstream of the valve in kg/m³ (in gases and vapors) J 1 Temperature in °C upstream of the valve Medium Liquids Gases Steam Pressure drop m³/h kg/h m³/h kg/h kg/h p 2 > p 2 1 K V = V . r 1000 Dp K V = W 1000 p rD K V = V . G 519 r D G T pp2 1 K V = W 519 T pp 1 G 2 rD K V = W 3162 . v p 2 D Dp< p 2 1 p 2 < p 2 1 K V = V 259.5 p . G 1 rG 1 T K V = W 259.5 p1 T G 1 r K V = W 3162 . 2v * p1 Dp> p 2 1 where: p 1 [bar] Absolute pressure p abs p 2 [bar] Absolute pressure p abs Dp [bar] Absolute pressure p abs (differential pressure p 1 – p 2 ) T 1 [K] 273 + J 1 V . G [m³/h] Flow rate of gases, related to 0 °C and 1013 mbar r [kg/m³] Density of liquids r G [kg/m³] Density of gases at 0 °C and 1013 mbar v 1 [m³/kg] Specific volume (v´ found in the steam table) for p 1 and J 1 v 2 [m³/kg] Specific volume (v´ found in the steam table) for p 2 and J 1 v* [m³/kg] Specific volume (v´ found in the steam table) for p1 2 and J 1

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  • Application Notes

    KV coefficient Valve sizing

    Calculation of the valve flow coefficient KVThe procedure specified in the IEC 60534 standard is applied todetermine the valve flow coefficient KV. The relevant device-spe-cific data can be found in the associated data sheets.The equations below are given to allow a preliminary, simpli-fied calculation of the valve flow coefficient to be performed.Please note that these equations do not take account of the influ-ence of the connection fittings and the flow limitation in case ofcritical flow velocities.

    Selection of the valve flow coefficient KVSOn the basis of the calculated valve flow coefficient KV, the ap-propriate valve flow coefficient KVS for the relevant valve typecan be selected from the associated data sheet.If realistic operating values have been used for the calculation,the following applies in general: For self-operated regulators: KVmax = 0.75 KVS For motor-operated valves: KVmax = 0.9 KVS

    Edition March 2012

    Application Notes AB 05 EN

    p1 Upstream pressurep2 Downstream pressureH Travel

    V.

    Volume flow rate in m/h (gases)W Mass flow rate in kg/h (liquids, steam) Density in kg/m

    (general, also in liquids)1 Density upstream of the valve in kg/m

    (in gases and vapors)1 Temperature in C upstream of the valve

    Medium Liquids Gases Steam

    Pressure drop m/h kg/h m/h kg/h kg/h

    p2 >p2

    1

    KV = V.

    1000 pKV =

    W

    1000 p

    KV =V.

    G

    519

    G Tp p2

    1 KV =W

    519Tp p1

    G 2 KV =

    W3162.

    vp2

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