retrofit of the pukalani wwtp water reuse in paradise
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Retrofit of the Pukalani WWTP Water Reuse in Paradise May 17, 2013 - PowerPoint PPT Presentation

Retrofit of the Pukalani WWTP Water Reuse in Paradise May 17, 2013 Project Location 2 Project Location 3 Project Location 4 Project Location Central Maui Pukalani hole in the sky Variable Rainfall (15-80 in/year) 5 Service


  1. Retrofit of the Pukalani WWTP Water Reuse in Paradise May 17, 2013

  2. Project Location 2

  3. Project Location 3

  4. Project Location 4

  5. Project Location Central Maui Pukalani – “hole in the sky” Variable Rainfall (15-80 in/year) 5

  6. Service Area 787 Connections  200,000 gpd Possible expansion to double existing size (400,000 gpd) 6

  7. Reuse Area Pukalani Golf Course 160 Acres 105 in/year ET 25-90 in/year of irrigation demand 330 to 1200 AF/year of irrigation demand 7

  8. Regulatory Reference HDOH “Guidelines for the Treatment and Use of Recycled Water” = CA Title 22 Water Recycling Criteria HDOH R-1 water = Disinfected Tertiary Recycled Water HDOH R-2 water = Disinfected Secondary-23 Recycled Water 8

  9. The Problem? Existing Pukalani WWTP Produced R-2 water  No filtration  Ineffective disinfection Provided supplemental irrigation water to 180- acre Pukalani Golf Course In violation of HDOH Guidelines  R-2 water can only be applied to golf courses subsurface (it was being sprinklered)  Access was not controlled and overspray into yards and on the public was quite possible  R-2 water, even if allowed in sprinkler systems isnot allowed within 500 feet of residences or parks. 9

  10. The Challenge Aging infrastructure  30 year old Oxigest  Salt corrosion No redundancy At capacity Very little space 10

  11. Space Challenge 11

  12. Existing Facility R-2 (Secondary-23) facility Treatment Process Performance Bar Rack Removal of Large Screenings Oxigest Package WWTP Secondary Treatment (Aeration/Clarification) Storage Reservoir (2-MG) Chlorine Contact, Storage on Non- Irrigation Days 12

  13. New Facility R-1 (Tertiary-2.2) facility Treatment Process Performance 1 mm fine screens Removal of Large Screenings Flow Equalization Shave Daily Peaks Anaerobic /Aerobic Bioreactor Secondary Treatment Membrane Filtration 0.2-0.4 micron Kubota flat plate Effluent turbidity < 0.2 NTU 95% of the time 80 mJ/cm 2 dose, 65% min UVT UV disinfection Storage Reservoir (2-MG) Storage on Non-Irrigation Days 13

  14. Fine Screens 14

  15. Equalization 15

  16. Bioreactor 16

  17. Membranes 17

  18. Mechanical Room 18

  19. UV Reactors 19

  20. Design Flows Phase 1 Design Phase 2 Design WWTP Design Membrane Membrane WWTP Design Membrane Flow Design Flow Design Flow Flow Design Flow (mgd) (mgd) Duration (mgd) (mgd) Average 0.200 0.200 0.400 0.400 Daily Average Day 0.230 0.230 0.460 0.460 Maximum Month 8-days Maximum 0.400 0.56 (non- 0.800 1.125 Day consecutive) Peak Hour 0.843 0.56 4 hours 1.500 1.125 20

  21. Out with the Old 21

  22. Cost? $7M for 200,000 gpd ($35/gpd) Expansion to 400,000 gpd possible for < $1M (total of approximately $20/gpd) 22

  23. Performance is Good 23

  24. Performance is Good 24

  25. Project Success 25

  26. Questions 26

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