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STP Study M/s HydrotechParyavaran India Pvt Ltd CAA II UC  Chennai Auto Ancillary Industrial Infrastructure Up gradation Company Ambattur Industrial Estate  Near HCL Unit - V Chennai
STP  (Gross Size 30 mt x70 mt)
View of STP from Top
Coarse Bar Screen (Constructed earlier but renovated  by the firm ) Coarse  Bar Screen  Circular Tank Diameter 3 m depth 5 mt
Grit Chamber - constructed earlier  Grit  Chamber  I Diameter 4.5 mt  depth 6.5 mt  RCC const Grit Chamber  Ii Dia 5.0 mt depth 6.5 RCC Construction
Pumping Station  Submersible Pump set  2 no ( 1 +1 standbye)  each  of  7.5  HP  Collection tank dia 4.0 mt depth 6.5 mt RCC
Bye Pass structure Not  in use @the Time of visit
STP Control Unit (Inside Brick Masonry Room)
CI Inlet Pipe( i/d 300 mm 2 no) to Equalization Tank
Collection Tank Cum Equalization Tank Inlet (One  Inlet pipe  no effluent)  Excess effluent again fed to tank Diameter 11 mt  Depth RCC Const 3.8 mt
Over flow Out  Let  at Equalization Tank
Electric Control of Two no Submersible Pumps at Equalization Tank
Stilling Chamber Rectangular- RCC
Fine Bar Screen Two numbers
Grit Chamber
FAB II   (dia 7.3 mt ) Out let of FAB II to Clarifier Media in FAB II
MBBR Bio Reactor FAB I Oil and Grease in F AB I MBBR Media in FAB I
Return sludge in FAB I Return sludge Pump 2 HP Return  Sludge fed in to FAB  I Pipe dia 63 mm
Air Compressor Unit( 3 no Compressors)
Air compressor distribution Header
Sludge and Grit Out lets to sludge bed Grit  out let from Grit Chamber Sludge out at FAB I
RCC Clarifier  (Dia 8.7 mt)
Clarifier Out fall to disinfection  Settled Effluent at the out let of clarifier
Disinfection unit
Steel structures ( like stair and Platform)
Sludge Bed
Sludge infilitrate collection sump
Sludge Distribution
Out Let Houdi and Out let into pond
Katcha Pond used to collect Treated effluent
Raw sewage and Treated Sewage
Lab at Site
Inspecting Team
Observations Oil and grease has been observed in the FAB I so this needs to be removed at preliminary stage by constructing oil and grease trap . This may constructed by department also Return sludge is being fed in to FAB I . Normally in MBBR return sludge is not fed  STP was not running at Full capacity at the time of visit and no discharge meter was installed to check the flow Disinfection needs to be done regularly Handling and Disposal of sludge  agreement needs to be finalized with the operator   Plant was in good working condition . Lab should have more testing equipment Flow meter should be installed at STP Following officers were present during visit 1. Mr S Srinivasan Director  and Mr N Palaniraja Chennai auto Ancillary Industrial Infrastructure Up gradation Company  2.Mr RakeshVermaSr Manger Projects M/s Hydro Tech Paryavaran India Pvt Ltd  3Mr S Selvam  Site Engineer M/s Hydro Tech Paryavaran India Pvt Ltd  Mr S Srinivasan is satisfied with the performance of the Plant  executed by M/s Hydro Tech Paryavaran India Pvt Ltd  Project was allotted on June 19 2006 vide CAAIIUC/STP and WTP /920 dt 19/6/2006 and completion time was 15 months and it was completed June 17 2009 .The delay needs to be explained .and cost overruns  if any needs to be checked .

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Stp study chhenai

  • 1. STP Study M/s HydrotechParyavaran India Pvt Ltd CAA II UC Chennai Auto Ancillary Industrial Infrastructure Up gradation Company Ambattur Industrial Estate Near HCL Unit - V Chennai
  • 2. STP (Gross Size 30 mt x70 mt)
  • 3. View of STP from Top
  • 4. Coarse Bar Screen (Constructed earlier but renovated by the firm ) Coarse Bar Screen Circular Tank Diameter 3 m depth 5 mt
  • 5. Grit Chamber - constructed earlier Grit Chamber I Diameter 4.5 mt depth 6.5 mt RCC const Grit Chamber Ii Dia 5.0 mt depth 6.5 RCC Construction
  • 6. Pumping Station Submersible Pump set 2 no ( 1 +1 standbye) each of 7.5 HP Collection tank dia 4.0 mt depth 6.5 mt RCC
  • 7. Bye Pass structure Not in use @the Time of visit
  • 8. STP Control Unit (Inside Brick Masonry Room)
  • 9. CI Inlet Pipe( i/d 300 mm 2 no) to Equalization Tank
  • 10. Collection Tank Cum Equalization Tank Inlet (One Inlet pipe no effluent) Excess effluent again fed to tank Diameter 11 mt Depth RCC Const 3.8 mt
  • 11. Over flow Out Let at Equalization Tank
  • 12. Electric Control of Two no Submersible Pumps at Equalization Tank
  • 14. Fine Bar Screen Two numbers
  • 16. FAB II (dia 7.3 mt ) Out let of FAB II to Clarifier Media in FAB II
  • 17. MBBR Bio Reactor FAB I Oil and Grease in F AB I MBBR Media in FAB I
  • 18. Return sludge in FAB I Return sludge Pump 2 HP Return Sludge fed in to FAB I Pipe dia 63 mm
  • 19. Air Compressor Unit( 3 no Compressors)
  • 21. Sludge and Grit Out lets to sludge bed Grit out let from Grit Chamber Sludge out at FAB I
  • 22. RCC Clarifier (Dia 8.7 mt)
  • 23. Clarifier Out fall to disinfection Settled Effluent at the out let of clarifier
  • 25. Steel structures ( like stair and Platform)
  • 29. Out Let Houdi and Out let into pond
  • 30. Katcha Pond used to collect Treated effluent
  • 31. Raw sewage and Treated Sewage
  • 34. Observations Oil and grease has been observed in the FAB I so this needs to be removed at preliminary stage by constructing oil and grease trap . This may constructed by department also Return sludge is being fed in to FAB I . Normally in MBBR return sludge is not fed STP was not running at Full capacity at the time of visit and no discharge meter was installed to check the flow Disinfection needs to be done regularly Handling and Disposal of sludge agreement needs to be finalized with the operator Plant was in good working condition . Lab should have more testing equipment Flow meter should be installed at STP Following officers were present during visit 1. Mr S Srinivasan Director and Mr N Palaniraja Chennai auto Ancillary Industrial Infrastructure Up gradation Company 2.Mr RakeshVermaSr Manger Projects M/s Hydro Tech Paryavaran India Pvt Ltd 3Mr S Selvam Site Engineer M/s Hydro Tech Paryavaran India Pvt Ltd Mr S Srinivasan is satisfied with the performance of the Plant executed by M/s Hydro Tech Paryavaran India Pvt Ltd Project was allotted on June 19 2006 vide CAAIIUC/STP and WTP /920 dt 19/6/2006 and completion time was 15 months and it was completed June 17 2009 .The delay needs to be explained .and cost overruns if any needs to be checked .