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Stone%20media%20TF%20design

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Calculate the BOD loading, hydraulic loading, BOD removal efficiency, and ... The required minimum wetting rate=0.5L/m2*s. Assume a secondary clarifier depth ... – PowerPoint PPT presentation

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Title: Stone%20media%20TF%20design


1
Stone media TF design
  • Example 1
  • Calculate the BOD loading, hydraulic loading, BOD
    removal efficiency, and effluent BOD
    concentration of a single-stage trickling filter
    based on the following data
  • Design assumptions
  • Influent flow 1530 m3/d
  • Recirculation ratio 0.5
  • Primary effluent BOD 130 mg/L
  • Diameter of filter 18 m
  • Depth of media 2.1 m
  • Water temperature 18oC

2
Stone media TF design
  • Solution)
  • (1) BOD loading rate (kg/m3/d)
  • BOD load BOD Conc. x Influent flow
  • 130 mg/L x 1530
    m3/d 198.9 kg/d
  • Volume of filter surface area of filter x
    depth
  • p (18 m x 18m)/4 X
    2.1 m 533 m3
  • BOD loading rate BOD load / volume of filter
  • 0.37 kg/m3/d

3
Stone media TF design
  • Solution)
  • (2) Hydraulic loading rate (m3/m2/d)
  • Total flow to the media influent
    recirculation flow
  • 1530 m3/d
    (1530 m3/d x 0.5)
  • Surface area of filter p (18 m x 18m)/4
    254 m3
  • Hydraulic loading rate Total flow to the
    media / area of filter
    9.04 m3/m2/d

4
Stone media TF design
  • Solution)
  • (3) Effluent BOD (mg/L)
  • BOD removal efficiency for first-stage filter at
    20oC,

5
Stone media TF design
  • Example 2
  • A municipal wastewater having a BOD of 200 mg/L
    is to be treated by a two-stage trickling filter.
    The desired effluent quality is 25 mg/L of BOD.
    If both of the filter depths are to be 1.83 m and
    the recirculation ratio is 21, find the required
    filter diameters. Assume the following design
    assumptions apply.
  • Design assumptions
  • Influent flow 7570 m3/d
  • Recirculation ratio 2
  • Depth of media 1.83 m
  • Water temperature 20oC
  • BOD removal in primary sedimentation 35
  • E1E2 0.65

6
Stone media TF design
  • Example 2

BOD200mg/L
BOD25mg/L
Primary Clarifier
Secondary Clarifier
TF2
TF1
7
Stone media TF design
  • Solution)
  • (1) Compute the recirculation factor

(12)/ (10.2)2 2.08
8
Stone media TF design
  • Solution)
  • (2) Compute the BOD load for the first filter
  • BOD load BOD Conc. x Influent flow
  • 200mg/L(1-0.35) x 7570 m3/d
    1234kg/d
  • (3) Compute the volume for the first stage
  • V 388 m3

9
Stone media TF design
  • Solution)
  • (4) Compute the diameter of the first filter
  • A V/depth 388 m3/1.83m 212 m2
  • Diameter 16.4 m
  • (5) Compute the BOD load for the second filter
  • BOD load to the second filter
  • (1-E1) x BOD load to the first filter
  • (1-0.646) x 1234 kg BOD/d
  • 437 kg BOD/d

10
Stone media TF design
  • Solution)
  • (6) Compute the volume for the first stage
  • V 1096 m3
  • (7) Compute the diameter of the first filter
  • A V/depth 1096 m3/1.83m 599 m2
  • Diameter 27.6 m

11
Stone media TF design
  • Solution)
  • (8) Compute the BOD loading to each filter
  • (9) Compute the hydraulic loading to each filter

12
Plastic media
13
Plastic media
  • Schulze formula
  • The liquid contact time (t) of applied wastewater
  • Where
  • t liquid contact time, min
  • D depth of media (m)
  • q hydraulic loading, (m3/m2/h)
  • C, n constants related to specific surface
    configuration of media

14
Plastic media
  • hydraulic loading (q)
  • Where
  • Q influent flow rate L/min
  • Afilter cross section area m2

15
Plastic media TF design
  • Schulze formula
  • Where
  • Se BOD concentration of settled filter
    effluent, mg/L
  • So influent BOD concentration to the filter,
    mg/L
  • kwastewater treatability and packing
    coefficient, (L/s)0.5/m2
  • Dpacking depth, m
  • q hydraulic application rate of primary
    effluent, excluding recirculation, L/m2s
  • nconstant characteristic of packing used
    (assumed to be 0.5).

16
Plastic media TF design
  • Example 3
  • Given the following design flow rates and primary
    effluent wastewater characteristics, determine
    the following design parameters for a trickling
    filter design assuming 2 reactors at 6.1 m depth,
    cross-flow plastic packing with a specific
    surface area of 90 m2/m3, a packing coefficient n
    value of 0.5, a 2-arm distributor system. The
    required minimum wetting rate0.5L/m2s. Assume
    a secondary clarifier depth of 4.2m and k value
    of 0.23.
  • Design conditions

Item unit Primary effluent Target effluent
Flow m3/d 15,140
BOD mg/L 125 20
TSS mg/L 65 20
Temp oC 14
17
Plastic media TF design
  • Example 3
  • Calculate the followings
  • Diameter of TF, m
  • Volume of packing require, m3

18
Plastic media TF design
  • Solution
  • (1) Diameter of tower trickling filter, m
  • Correct k for temperature effect

19
Plastic media TF design
  • Solution
  • (1) Diameter of tower trickling filter, m
  • Determine the hydraulic loading rate
  • Determine the tower area
  • Determine the tower diameter

20
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