Air Vessel Sizing for Water Hammer Prevention in Pipelines

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    Air Vessel Sizing for Water Hammer Prevention in Pipelines

    Figure 1: Pipeline Prole

    Reference: Simple Guide for Design of Air Vessels for Water Hammer Protection ofhttp://www2cemetuedutr/!ce"#$/lin%s/docs/&'"#$(We)*iles/air(cham)erpdf 

    http://www2.ce.metu.edu.tr/~ce534/links/docs/CE534-WebFiles/air-chamber.pdfhttp://www2.ce.metu.edu.tr/~ce534/links/docs/CE534-WebFiles/air-chamber.pdf

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    Figure 2: Maimum an! minimum "ea! envelopes #ase! on incompressi#le $o% t

    Figure ': Air an! Vessel Volumes

     +erms ,n a)o-e charts:

    ((((((((((((((((((( .0

    where:

    S1 Dimensionless parameter

    g

    Static head a)o-e pump discharge no33le plus destination pressure .in head

    A

    L Length of pipeline4 m

    ,nitial Pipeline Velocit54 m/s

    minimum static head a)o-e pump discharge no33le plus destination pressur

    ma6imum static head a)o-e pump discharge no33le plus destination pressu

    S7 ,nitial gas -olume in -essel4 m#

    gra-itational acceleration4 89 m/s2

    Ho 

    &ross(sectional area of pipeline4 m2

    -7 

    Hmin

     

    Hma6

     

    2

    0

    00'

    v L A

     H  g S S 

    ××××

    =

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    *or maorit5 air -essel -olume calculations consider the following -alues

    and

    4.0

    0

    min = H 

     H 

    4.1

    0

    max=

     H 

     H 

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    *rom ;*igurre 2; 4 S1

    2$>m

    8#

    S $8

    S with S* $8

    277m

    $?"m

    Air -essel -olume4 m#

    Sw  ,nitial water -olume in -essel4 m#

    .Hmin

     / H7 7$0

    Hmin

     / H7 

    H7 

    dp 

    -7 

    Safet5 factoron VesselVolume.L/D0

    -essel 

    m2

    S7 m#

    hmin

     

    Sw  m#

    m#

    m#

    D-essel

     

    L-essel

    ,

          @    u      t      l    e      t

    Air Vessel

    &ompressed Air or itrogen

          d      7

    Li=uid

    0

    2

    0

    0

     H  g 

    v L AS 

    ×

    ××

    =

    wS S S    += 0

    min

    2

    0

    h g 

    v L AS w

    ×

    ××=

    min0min  H  H h   −=

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    2 Si3e needs to )e -eriBed )ased on point num)er to ensure that -elocit5 is %ept at or )e

    )nlet (onnection

    (((((((((((.>0

    where:

    ,nlet connection si3e4 mm

    pipeline si3e4 mm

    *utlet (onnection +!o,

    do is generall5 72" to 7" times the pipe diameter d

    p

    di 

    dp 

    Pipeline

    2

    14/1

    max

    2

    0 ×   

      

     

    ×=

    h g 

    v

     p

    i

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    ((((((((((((.?0

    04 we get

    (alculations +)nlet - *utlet Size,Inputs

    877 mm

    $ m/s

    $7m

    Outputs

    22" mm

    98inch

    98mm

    $?inch

    Selecte! Size

    7 inch

    > inch

    Prepared )5: An%ur Sri-asta-a

    &hemical 'ngineer

    Since Hma6

    $CH74

    dp 

    -7 

    H7 

    do 

    di 

    do 

    di 

    an%ur27>Ehotmailcom

    0maxmax  H  H h   −=

    0max  4.0   H h   ×=

    2

    1

    4.0

    4/1

    0

    2

    0 ×   

      

     

    ××=

     H  g 

    v

     p

    i

    mailto:ankur_2061@hotmail.commailto:ankur_2061@hotmail.com

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      umping Lines

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    eor&

    terms04 m

    e .in head terms04 m

    re .in head terms04 m

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    let

    di

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    low 7 m/s in the outlet piping

    dp

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