Page 104 - HUDCO-BPA21
P. 104

SANITATION
          SANIT   A TION


         Ÿ To meet the water requirements of units coming up      state-of-the-art  GE  Membrane  Technology  (ultra              followed  by  Flocculation-Clarification  in  Claritube   the Moving Bed Biological Reactor.
            inside Mangalore SEZ, Mangalore SEZ Ltd (MSEZL)       filtration)  for  re-use  of  Secondary  Treated  Sewage         Flocculator (CTF).                                 Claritube Flocculator (CTF):
            was provided with the wastewater from 3 STPs as one   Water from Kavoor STP during the year of 2011.               Ÿ Filtration by Membrane-based Ultrafiltration system.
            of  the  sources.  Since  the  Netravathi  river  is  being   Ÿ State-of-the-art plant with process automation and the                                                   Ÿ The  Sewage  from  MBBR  flows  to  the  Claritube
            utilized for drinking purposes, drawing of additional   plant is being controlled and monitored through PLC-       Ÿ Disinfection using ClO2 with onsite ClO2 unit.         Flocculator. At the inlet of CTF alum is dosed in the
                                                                                                                                                                                        flash mixer. The solids separated here are settled and
            water  was  not  allowed  from  the  river  hence  the   based SCADA system.                                       Ÿ Sludge handling Filter Press Unit.                     the sludge formed is withdrawn from the Claritube
            MSEZL had to settle with the wastewater from 3 STPs                                                                Ÿ The tertiary treated sewage is then stored in a tank,
                                                               Ÿ Plant  is  commissioned  and  MSEZL  is  supplying                                                                     Flocculator which is taken to the sludge sump.
            as one of the Sources.                                                                                                from where it is pumped to SEZ area.
                                                                  treated  water  to  MRPL/MSEZL  from  November                                                                     Ÿ The Claritube Settler comprises of Tube settler formed
         Ÿ Several meetings were carried out with MSEZL and
                                                                  2012.                                                        Stilling Chamber:                                        by specially designed Tube Modules. In tube settler
            formed SPV-Mangalore STP Limited for reusing the
            secondary treated sewage water.                    Ÿ Tertiary  Treatment  Plant  is  mainly  designed  for         The treated sewage outlet from the existing STP is raw   the effective surface area required for the separation of
                                                                  removal of TSS, turbidity and for further reduction of       water for Stilling Chamber (SC), where the turbulence is   suspended solids is provided in relatively much less
         Mangaluru  City  Corporation  has  provided  the  below                                                               reduced. The sewage pumped to Stilling Chamber with      volume compared to conventional clarifiers.
                                                                  BOD & COD from secondary treated sewage water.
         mentioned civil & mechanical structures and handed over                                                               1162m3/hr to the downstream units.                    The Tube settler is divided into four zones.
         to SPV.                                               Ÿ The designed parameter of TTP is given in the table           Moving Bed Biological Reactor (MBBR):
         1. Inlet Chamber                                         below.                                                                                                             Ÿ  Distribution zone
                                                                                                                               Ÿ The  main  pollutants  in  the  treated  sewage  are   Ÿ  Inlet zone
         2. Screen Removal
                                                               Parameter of TTP                                                   represented  in  the  form  of  Biochemical  Oxygen   Ÿ  Settling zone
         3. Grit Chamber                                                                                                          Demand  (BOD)  and  Chemical  Oxygen  Demand
                                                                                                                                                                                     Ÿ  Discharge zone
         4. Parshall Flume                                      Sl.   Parameter   Unit   Inlet     Outlet                         (COD).                                             Ultra filtration:
                                                                No.
         5. UASB                                                                                                               Ÿ The  bio-reactions  are  carried  out  in  the  controlled
                                                                1.  pH               -     6.5-7.5     7.0-7.5                    environment  in  the  Moving  Bed  Bio-Reactor     Ÿ The clear overflow from CTF gravitates through the
         6. Preaeration                                                                                                                                                                 UFC  channel  to  UFMT.  ZW-1000  UF  Membrane
                                                                2.  TSS            mg/l     30          < 1                       (MBBR). The bioreactor comprises of a tank, fitted
         7. Aeration                                                                                                                                                                    system is used for treating the clarifier outlet water.
                                                                              0
                                                                3.  BOD5 at 20  C  mg/l     20          <2                        with  an  aeration  grid.  The  bacterial  activity  needs   The basic purpose of the UF system is to remove the
         8. Clarifier                                                                                                              dissolved oxygen, to synthesize the organic matter.
                                                                4.  COD            mg/l     100         < 30                                                                            fine colloidal impurities and thereby removes BOD.
         9. CCT- Let off natural drains                                                                                            This  is  supplied  by  passing  air  in  form  of  small
                                                                5.  Nitrogen       mg/l   15 (Total     < 5                       bubbles.                                           Ÿ The complete UF system is automated and processes
         10. Thickener & Sludge Recirculation
                                                                                          Nitrogen)  (Ammonical                                                                         are typically operated in the following modes.
         11. Drying Bed                                                                               Nitrogen)                Ÿ The air is passed at the bottom of the tank so that the
                                                                                                                                  complete  volume  of  the  tank  is  utilized.  Dissolved   -   Permeation
         The treatment Process Involves:                        6.  Fecal Coliform  MPN      -        <1/100ml
                                                                                                                                  oxygen can be used by the bacteria.                   -   Backwash
         Tertiary Treatment Plant                               7.  Turbidity      NTU       -          <0.5                                                                            -   Maintenance Clean (MC)
                                                                                                                               Ÿ The  bacterial  population  is  present  on  the  media,
         Ÿ MSEZL  has  taken  up  the  construction  of  5  MGD                                                                   which forms an integral part of the reactor system. The   -   Recovery Clean (RC)
                                                               Advantage of TTP water reuse
            (22.7MLD)  Tertiary  Treatment  Plant  (TTP)  using                                                                   media is made of small plastic elements. Millions of   -   Stand-by
                                                               Ÿ Reduction  in  the  dependency  on  natural  water
                                                                                                                                  such pieces are present in the reactor.               -   Shutdown
                                                                  resources.
                                                                                                                               Ÿ A very large surface area is available for the bacterial   Disinfection System:
                                                               Ÿ Reduction  of  financial  burden  on  Mangalore  City             population to grow. The bacteria grow on the plastic   Ÿ The treated filtered sewage is then added with ClO2
                                                                  Corporation for O&M of STP.                                     media by using the organic content in the raw sewage   for Disinfection. Chlorine Dioxide is generated using
                                                               Ÿ Avoiding  disposal  of  secondary  treated  sewage  in           and the dissolved oxygen available. Due to constant   Acid Chlorite technology.
                                                                  natural river body thereby minimization of pollution            aeration, the media is set in whirling motion so that   Sludge handling:
                                                                  loads  on  freshwater  sources  and  improving                  continuous mixing takes place.
                                                                                                                                                                                     Ÿ The  sludge  from  the  Claritube  Flocculator  (CTF)
                                                                  Environmental quality.                                       Ÿ The  bacterial  layer  growth  on  the  media  surface
                                                                                                                                                                                        flows to Sludge Sump (SC) and then it is pumped to
                                                               Ÿ Employment generation.                                           increases to a certain extent and then gets sloughed off   Filter Press (PS) for Solid Liquid Separation.
                                                                                                                                  after a specific period.
                                                               Tertiary Treatment process:                                                                                           Ÿ The dewatered sludge is further used for Green Belt
                                                                                                                               Ÿ Around 60% to 70% of the BOD is further reduced in
                                                               Ÿ Biological  treatment  comprising  of  Aerobic                                                                         development.
                                                                  Treatment  in  Moving  Bed  Bio-Reactor  (MBBR)                                                                    Final Storage Tank:
         STP and TTP Flowchart
                                                                                                                                                                                 { 91 }
                                                                                                                                                                                 { 91 }
                                                          { 90 }                                                                                                                 { 91 }
   99   100   101   102   103   104   105   106   107   108   109