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Tertiary Filtration.

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Presentation on theme: "Tertiary Filtration."— Presentation transcript:

1 Tertiary Filtration

2 Granular Media Rapid Sand Filtration (RSF)
RSF w/o Chemicals: Removal of Residual SS (Biological Floc) RSF w/ Coagulant (Al, Fe), w/ or w/o Polymer, or Lime; Enhanced Solids Removal, P (PO43-) Precipitation WW RSF (Larger, More Variable Size, and Higher Concentrations of Particles in II-Effl.) vs. RSF in D.W. (Settled-Water Turbidity: 1 –10 NTU) WW Solids: Residual Biosolids, Chemical Flocs and Precipitates III-Filtration Serves as “Pretreatment” for Other AWT Processes General Goal: SS  5 mg/L; Turbidity  5 NTU; P  1 mg/L Performance (NTU): Figure 11-2

3 Figure 11-2

4 III/AWT RSF Design and Operation
WW RSF Generally Similar to D.W. RSF Except: Shorter Run Times (e.g.,  24 hrs, Daily Backwash) and Greater Surface Straining Media: Single (Sand or Anthracite) vs. Multi-Media (Sand, Anthracite, and/or Garnet); Shallow- vs. Deep-Bed; Coarser Media Possible Filtration Rate: 2 – >10 gpm/ft2; Constant vs. Declining Rate Biofiltration: Nitrification Unlikely Because of Low DO; De-Nitrification if Designed Accordingly (Low Filtration Rate, Supplemental C); Increased Headloss by Biological Activity; Control by “Pre”-Chlorination Activated Sludge Bioflocs Stronger and more Filterable than Trickling Filter Solids Biological Flocs are Stronger than Chemical Flocs and Use of Coarser Media is Possible; Chemical Floc Properties Improved by Polymers Performance of “Plain” Filtration Following Activated Sludge: SS = 1 – 5 mg/L

5 III- Filtration with Chemical Addition
Chemicals Added: Metal Coagulants (Al(III), Fe(III)), Organic Polymers, Lime Metal Coagulants: Al3+ (or Fe3+) + 3 OH-  Al(OH)3 (or Fe(OH)3) In AWT, Generally Operate in Sweep Floc Region Al3+ (or Fe3+) + PO43-  AlPO4 (or FePO4); Figure 6-13 Organic Polymers: Primary Coagulants (Cationic Polymers) vs. Coagulant (Filter) Aids Lime (Ca(OH)2  Ca OH-): Ca2+ + CO32-  CaCO3 Mg OH-  Mg(OH)2 3 Ca PO43-  Ca3(PO4)2 5 Ca PO43- + OH-  Ca5(PO4)3OH (hydroxyapatite)  Table 6-5

6 Figure 6-13

7 Table 6-5

8 III- Filtration with Chemical Addition – Continued
P Forms: Particulate vs. Dissolved; Table 6-4 Org-P, polyphosphates (e.g., P2O74-, hydrolyzes to orthophosphate), orthophosphate (PO43-) ; pH Effects (part of H3PO4 system); Table 6-3 Point of Application for P Removal: Before I-Sedimentation (High Doses) Before Biological Process (Inert Solids) Before II-Sedimentation (In Lieu of III-Filter, High Doses), Before III-Filtration (Lower Doses; In-Line, Static Mixer, Rapid Mixer or Flocculator)  Clarification Before Filtration if High Doses Performance: Up to 95 % P Removal; Turbidity  1 NTU Other Benefits of Chemical Clarification: High-pH Disinfection by Lime; Physical Removal of Pathogens; Chemical Precipitation of Metals (e.g., Zn(OH)2, or Adsorption onto Al(OH)3 Floc)

9 Table 6-4

10 Table 6-3


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