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Physical Unit Operations screening
By
R M Bhadaraka
Screening
 First operation employed in wastewater treatment.
 It is necessary to retain floating matter and coarse solids as a pieces of
cloths garbage so as to protect pumps and other units from clogging.
 The retained material at screens is called as screenings.
 For proper functioning it required to clean the screens.
 A good designer shall provided two screen units as standby.
 Screens may consist of vertical or inclined bars(bar racks or bar screens),
wire mesh or perforated plates having either circular or rectangular
opening.
 Screens are kept Grit Chamber.
Classification of Screen
Sr No. Classify Spacing
1 Coarse Screen ≥ 50mm
2 Medium Screen 20 to 50mm
 Bar Screens are inclined at 30 to 60 to direction of flow to increase a the area of
Screening.
 Screens are fixed permanently and may either be manually cleaned or mechanically
cleaned.
 The amount of screening may be 0.03 to 0.08 𝑚3/million litre of wastewater.
Screening
 If Screening formed are 0.05 𝑚3
/ML for a wastewater treatment plant
with 50 MLD flow of wastewater the totally daily amount of screening
may be around 50 X 0.05 = 2.5 𝑚3
 Screenings can be disintegrated digested incinerated or buried.
Sr No. Design Parameter Manually Cleaned Mechanically Cleaned
1 Velocity through rack (m/s) 0.3 – 0.6 0.6 – 1.0
2 Bar size
Width(mm)
Depth (mm)
4 – 8
25 - 50
8 – 10
50 – 75
3 Spacing between bars mm 25 – 75 10 – 50
4 Slope from horizontal degrees 45 – 60 75 – 85
5 Allowable head loss in clogged condition 150 150
Head Loss
 Head loss through the bar rack is calculated form following formulae.
𝑯 =
𝑽 𝟐
− 𝒗 𝟐
𝟐𝒈
𝟏
𝟎. 𝟕
Where,
H = Head loss through bar rack in meters
V = Velocity through rack, m/s
v = velocity in upstream of bar rack, m/s
g = Acceleration due to gravity
= 9.81 𝑚
𝑠2
𝑯 =0.0728 (𝑽 𝟐
− 𝒗 𝟐
)
Note : this equation used to find out head loss in clean or partially clogged bar screen
Head Loss
H = β
𝑾
𝒃
𝟒
𝟑
h sinθ
Where,
W = Maximum cross sectional width of bars facing the wastewater flow, meters
b = Minimum clear bar spacing
h = velocity head of wastewater
β = Bar shape factor value of bar shape factor for clean bar rack.
Sr no. Type of bar β
1 Sharp edge rectangular bar 2.42
2 Rectangular with semi circular face facing upstream 1.79
3 Rectangular with both ends semi circular 1.67
4 Circular bars 1.83
Note : this equation used to find out head loss of clean bar screen
Quantity of Screening
 Quantity of screening depend upon type of screen, weather and
characteristic of wastewater.
 Narrow opening will collect more screening.
 Hot weather shall increase water use and waste water generation shall be
more.
 Quantity of screening may be 0.03 to 0.08 𝑚3
𝑀𝐿
 It may be taken average 0.05 𝑚3
𝑀𝐿
Characteristic of Screening
 Screening contain approximately 80% moisture and has a normal Wt-
density of 960 kg/𝑚3

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Physical unit operations

  • 1. Physical Unit Operations screening By R M Bhadaraka
  • 2. Screening  First operation employed in wastewater treatment.  It is necessary to retain floating matter and coarse solids as a pieces of cloths garbage so as to protect pumps and other units from clogging.  The retained material at screens is called as screenings.  For proper functioning it required to clean the screens.  A good designer shall provided two screen units as standby.  Screens may consist of vertical or inclined bars(bar racks or bar screens), wire mesh or perforated plates having either circular or rectangular opening.  Screens are kept Grit Chamber.
  • 3. Classification of Screen Sr No. Classify Spacing 1 Coarse Screen ≥ 50mm 2 Medium Screen 20 to 50mm  Bar Screens are inclined at 30 to 60 to direction of flow to increase a the area of Screening.  Screens are fixed permanently and may either be manually cleaned or mechanically cleaned.  The amount of screening may be 0.03 to 0.08 𝑚3/million litre of wastewater.
  • 4. Screening  If Screening formed are 0.05 𝑚3 /ML for a wastewater treatment plant with 50 MLD flow of wastewater the totally daily amount of screening may be around 50 X 0.05 = 2.5 𝑚3  Screenings can be disintegrated digested incinerated or buried. Sr No. Design Parameter Manually Cleaned Mechanically Cleaned 1 Velocity through rack (m/s) 0.3 – 0.6 0.6 – 1.0 2 Bar size Width(mm) Depth (mm) 4 – 8 25 - 50 8 – 10 50 – 75 3 Spacing between bars mm 25 – 75 10 – 50 4 Slope from horizontal degrees 45 – 60 75 – 85 5 Allowable head loss in clogged condition 150 150
  • 5. Head Loss  Head loss through the bar rack is calculated form following formulae. 𝑯 = 𝑽 𝟐 − 𝒗 𝟐 𝟐𝒈 𝟏 𝟎. 𝟕 Where, H = Head loss through bar rack in meters V = Velocity through rack, m/s v = velocity in upstream of bar rack, m/s g = Acceleration due to gravity = 9.81 𝑚 𝑠2 𝑯 =0.0728 (𝑽 𝟐 − 𝒗 𝟐 ) Note : this equation used to find out head loss in clean or partially clogged bar screen
  • 6. Head Loss H = β 𝑾 𝒃 𝟒 𝟑 h sinθ Where, W = Maximum cross sectional width of bars facing the wastewater flow, meters b = Minimum clear bar spacing h = velocity head of wastewater β = Bar shape factor value of bar shape factor for clean bar rack. Sr no. Type of bar β 1 Sharp edge rectangular bar 2.42 2 Rectangular with semi circular face facing upstream 1.79 3 Rectangular with both ends semi circular 1.67 4 Circular bars 1.83 Note : this equation used to find out head loss of clean bar screen
  • 7. Quantity of Screening  Quantity of screening depend upon type of screen, weather and characteristic of wastewater.  Narrow opening will collect more screening.  Hot weather shall increase water use and waste water generation shall be more.  Quantity of screening may be 0.03 to 0.08 𝑚3 𝑀𝐿  It may be taken average 0.05 𝑚3 𝑀𝐿
  • 8. Characteristic of Screening  Screening contain approximately 80% moisture and has a normal Wt- density of 960 kg/𝑚3