Dpk_Coventional Baffle Flocculator

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  • 8/17/2019 Dpk_Coventional Baffle Flocculator

    1/3

  • 8/17/2019 Dpk_Coventional Baffle Flocculator

    2/3

    Water Treatment

    Package Plant Design

    Hydraulic Flocculator

    Design

    2 of 3

    Design criteria for hydraulic flocculation

    MWH,pp 760

    Camp number to be between 25000 to 100000

    Detention time to be more than 8 minutes

    Polytec, NZ

    USQ pp.136

    Design Calculations

    Q = 2.5 ML/D

    Raw Water, Q = m3/s

    Detention Time = 483 s > s= min > min

    Try Channel Velocity = m/s > 0.15 but less than 0.45

    Actual Channel Velocity = m/s

    Baffle width = m Assumed

    Average water height = m

    r = 1000.0 kg/m3

    g = 9.81 m/s2

    head loss, for EACH 180 degrees turnwhere, k = 2.5 to 4.

    say, k = 3

    h = 0.01 m

    Number of Turns = 39

    head loss,   DH = m

    8

    0.2

    0.24

    0.0289

    0.2

    8.05

    0.482

    0.3

    480

  • 8/17/2019 Dpk_Coventional Baffle Flocculator

    3/3

    Water Treatment

    Package Plant Design

    Hydraulic Flocculator

    Design

    3 of 3

    Dynamic Viscosity,   m = N.s/m2 (at 20 degrees)

    G = OK

    C = G.t

    = OK

    Tank Water Volume

    Required V, = m3 for min detention time

    L = m

    W = m

    Av H = m plus free board = m

    Total Tank depth = m

    H loss = m

    Volume, V = m3 OK

    Thus, put 3 no. Flocculator each with 13 baffles.

    Summary:

    L = m

    W = m

    H = m

    No. Baffles = m say, no.13

    2.1

    0.6

    13.98

    Velocity Gradient:

    Velocity Gradient:

    Camp Number:

    0.6

    13.0

    13.89

    4.6

    13.8

    2.1

    0.48

    0.24

    0.1

    0.001

    69.751484

    33,481 

    8