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Waste Water Recycling
VisionEarthcare Pvt Ltd (VEC), SINE IIT Bombay
www.visionearthcare.com/home/soil-bio-technology, contactus@visionearthcare.com
WhatsApp: +91-9987542130, LL: +91-22-27718444
CAMUS-SBTTM
Continuous Advanced Multistage System using Soil Bio Technology
CAMUS-SBTTM Waste Water Recycling
www.visionearthcare.com ,contactus@visionearthcare.com, whatsapp: 9769605447
IIT Bombay Patent Authorization
VEC:Trademarks
● VEC is authorized SBT / CAMUS-
SBT Technology Provider
● Un-Authorized/Un-Approved
implementations of SBT technology
is a Criminal Violation of Indian and
International Patent and Trademark
Laws
● Unauthorized Implementing Agency
and Beneficiaries will be liable for
prosecution by Vision Earthcare
including damages
Credentials and Qualifications
MOU with Maharashtra Govt as Technology Provider
Typical Water Test Results
Meets CPCB Norm
● BOD < 10mg/L
● TSS < 10mg/L
● COD < 50mg/L
Our Clients
CAMUS-SBT vs ASP : Process Flow
Aeration Basin
Blowers/Diffusers:
High Energy and Maintenance
Sludge Bed
Preliminary
Screening
WetWell
Primary
Clarifier
Secondary
Clarifier
Thickener
ACF
Disinfection
sludge
recycle
BOD: 300
TSS : 300
BOD:30
TSS:20
BOD: <10
TSS : <5
Typically
CPCB E
Preliminary
Screening
WetWell
RST
Settler
Equilizer Bio Mound
(BM1)
Bio Mound (BM2)
(BM3)
BOD: 300
TSS : 300
BOD: 50
TSS : 30
BOD: ~5
TSS : ~1
ACF
Disinfection
CPCB A
CPCB
B/C/D
Continuous Aerobic Multi-Stage Soil Bio Technology (CAMUS-SBT)
ComponentsofSBT
9
Culture
Bio Mounds (BM1/2)
Soil Liquid Processing
Pheretima Elongata
White Worms
Bio Mounds (BM3)
Vermicomposting: Solids Processing
Eisenia Fetida
Red Worms
Technology Comparison
Assessment of various wastewater parameters Technologies
Performance after Secondary Treatment (BOD<30) CSBT ASP MBBR SBR UASB+ASP MBR WSP
Effluent BOD (mg/L) <20 <20 <30 <10 <20 <5 <40
Effluent Suspended Solids (mg/L) <30 <30 <30 <10 <30 <5 <100
Fecal Coliforms (log unit) 6-7 2-3 2-3 3-4 2-3 5-6 2-3
T-NH3 removal efficiency (%) 70-80 10-20 10-20 70-80 10-20 70-80 10-20
Performance after tertiary treatment (BOD<10)
Effluent BOD (mg/L) <10 <10 <10 <10 <10 <10 <10
Effluent Suspended Solids (mg/L) <5 <5 <5 <5 <5 <5 <5
Effluent NH4N(mg/L) <1 <1 <1 <1 <1 <1 <1
Effluent TP(mg/L) <0.5 <0.5 <0.5 <0.5 <0.5 <0.5 <0.5
Effluent total coliform MPN/100 ml 10 10 10 10 10 10 10
Area requirement (m2/MLD)
Average area secondary treatment (BOD<30) 300 800 450 450 1000 450 6000
Average area secondary treatment (BOD<10) 600 900 550 550 1100 450 6100
Operation & Maintenance
Energy consumption in secondary treatment (kwhr/ML) 60 180 220 150 120 300 2
Energy consumption in tertiary treatment(kwhr/ML) 60 180 220 150 120 300 2
Energy consumption for sludge handling(kwhr/ML) 1 1 1 1 1 1 1
Total Energy consumption (kwhr/ML) 121 361 441 301 241 601 5
Chemical requirement
Polymer /coagulants Low High High High High High High
Disinfection Low High High High High High High
Other chemicals Low High High High High High High
Skilled Manpower No Yes Yes Yes Yes Yes No
Source : Adapted from IIT Kanpur STP comparison Ganga Action Plan : 003_GBP_IIT_EQP_S&R_Ver 1 Dec 2010
Process Flow X(KLD) = 5 to 50
Typical Small STP (50-500KLD)
● SC: Screen Chamber
● RST: Raw Sewage Tank
● CT: Collection tank
● BR: Bio Reactor 1&2
Typical Medium STP (0.5-10MLD)
● FC: Fine Screen Chamber
● GC: Grit Chamber
● TS: Tube Settler
● EQT: Equalization tank
● BM: Bio Mound
Typical Medium STP (0.5-10MLD)
● FC: Fine Screen Chamber
● GC: Grit Chamber
● TS: Tube Settler
● EQT: Equalization tank
● BM: Bio Mound
Typical Large STP >10MLD
● FC: Fine Screen Chamber
● GC: Grit Chamber
● CLF: Clarifiers
● AD: Anaerobic Digestors
● BM: Bio Mounds
17
Press/Media
18
Genesis of CAMUS-SBT @ IITB
Typical Process Walk Through of 25 MLD Plant
MediaMedia
CAMUS-SBT Media Regeneration
Media
Organics
Adsorb on
Media
Surface
Waste Water percolates
on media
Clean water Drip down
out of the media
Bacterial Colonies start
growing by feeding on
adsorbed organics for
food,
Media
Earthworms (White) Feed
on the bacterial Colonies
CO2
released
CO2
released
Media is now
available for the
next cycle
adsorption surface
is regenerated by
bacterial grazing
Grazing by
earthworms
creates new
surface free of
bacteria, converting
the biomass to
CO2
Why CSBT: Energetics of Carbon Cycle
Atmosphere CO2
750
Live 0
(10 yrs)
Water
as Dissolved CO2 and Life
4000
Live 1-5
(0.2 yrs)
Soil
as Dead Reserves
1600
Live 0
(300 yrs)
Land
as Animals
100-150
Live 150
(2 yrs)
Land
as Plant
500
Live 500
(50 yrs)
Soil
as Fossil Fuel
4000
Live 0
(300 yrs)
Photosynthesis
110
Respiration
12
Physical Mass Transfer 50
Biological 60
Litter 18
Respiration
60
Human Activities
6
Energy Required for Life
● Land : 3 KJ/g live
C/yr
● Water : 500 KJ/g live
C/yr
21
ProcessChemistry
CSBT Reactor Configurations
Chandrashekar S, Shankar HS: Bio-Remediation of Waste Water Streams using SBT: AICHE 2009
CAMUS-SBT is designed
with minimal mechanical
equipment
Frequently Asked Questions
• What is the extent of pre-treatment? (How much COD, TSS and TDS are removed)
– Fine screens and Grit removal chamber
– Equalization tank balances peak flows
– Pre-Treatment Primary Clarifier / Tube Settler for BOD and TSS separation
– Removal efficiency of 60% is in BOD and TSS in the clarified stream
– Clarifier sludge is processed in a Anaerobic Digestor with Phosphate Accumulating Organisms (PAO)
– Digested sludge further vermicomposted in BM3 to produced phosphate rich organic fertilizer
• What is the range of fluctuating load
– CAMUS-SBT plants are designed as per CPHEEO norms as regards to peak flows
– Plants are designed to handle flows from 5% to 100%
– Shock loads of 30% over design load can accommodated for 1-2 days (requires extra consumables)
• flocculant/coagulant dosing to capture more TSS/BOD/COD and load on Bio Mounds
• Feed rate or loading rate i.e. Hydraulic and Organic loading rates at each stage?
– Fine Screen and Grit Chambers are Designed at Peak Hydraulic Flow
– Equalization Tank at CPHEEO norms of 2 hours at peak flow
– Clarifiers at Average Hydraulic Flow using 1.5 cum/sqm/hr overflow rate
– Anaerobic Digestor designed at 10-20 days detention time
– BioMound 1 Hydraulic Loading Rate = 0.1 cum/sqm/hr (2.4 cum/sqm/day), COD loading rate = 0.35
kg/cum/day
– Bio Mound 2 designed at Hydraulic Loading Rate = 0.2 cum/sqm/hr (4.8cum/sqm/day), COD loading
rate of 0.30 kg/cum/day 24
Frequently Asked Questions
• What happens to the CAMUS- SBT plants in Monsoon?
– Rain water impinging on the Bio reactors will percolate down rapidly and captured in treated water.
– Bio reactors are designed for hydraulic percolation rates of upto 5 cum/sqm/day
– Heaviest 1 day rainfall ever recorded worldwide is 2.5 cum/sqm/day (Reunion Island)
– Cherrapunji on average gets approximately 0.8 cum/sqm/day in monsoons
– Overflow in Collection tanks ensure that the Bio Reactor/Bio Mounds is not flooded.
• What is the input and output of the CAMUS-SBT?
– CAMUS-SBT plants are designed to meet CPHEEO/Client requirements for a given output.
• A comparative study of technology with respect to area and costs
• upto 1 MLD,1-5MLD, 5-10 MLD, 10-50 MLD etc?
– Please see Technology Cost Slides
• How are phosphates are removed in the CAMUS-SBT System?
– Phosphate removal takes place largely in Raw Sewage Tank / Clarifier / Anaerobic digestor by
flocculation/coagulation/settling/bio accumulation via Phosphate accumulating organisms.
– Small amounts of Lime (pH management)+FeCl3 is added in the Raw water tank that precipitates the
Phosphates as HydroxyApatite. pH of 6.5-7.5 is maintained
– In Larger plant the bottom phosphate rich sludge from Clarifier/Settlers is pumped as slurry to BM3
and is converted to vermi compost.
– In smaller plants the inorganic sludge at the bottom of Raw Sewage tank is periodically harvested
(Once in 4 years)
– The biomounds themselves remove approximately 2mg/L 25
Our Partner Initiatives
• Zerodor Waterless Urinals
– Ekam Eco Solutions, IIT Delhi
• DrySan Waterless Toilet
– CTECH, IDC IIT Bombay
• Air Quality (AQI) Monitoring System
– Indiaspend, IIT Bombay
• Water Quality Monitoring System
– Logic Ladder
• Intercepted / Small Bore Sewers
– Clearford

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Vision Earthcare Soil Bio Technology for Waste Water Recycling

  • 1. Waste Water Recycling VisionEarthcare Pvt Ltd (VEC), SINE IIT Bombay www.visionearthcare.com/home/soil-bio-technology, contactus@visionearthcare.com WhatsApp: +91-9987542130, LL: +91-22-27718444 CAMUS-SBTTM Continuous Advanced Multistage System using Soil Bio Technology
  • 2. CAMUS-SBTTM Waste Water Recycling www.visionearthcare.com ,contactus@visionearthcare.com, whatsapp: 9769605447
  • 3. IIT Bombay Patent Authorization
  • 4. VEC:Trademarks ● VEC is authorized SBT / CAMUS- SBT Technology Provider ● Un-Authorized/Un-Approved implementations of SBT technology is a Criminal Violation of Indian and International Patent and Trademark Laws ● Unauthorized Implementing Agency and Beneficiaries will be liable for prosecution by Vision Earthcare including damages
  • 5. Credentials and Qualifications MOU with Maharashtra Govt as Technology Provider
  • 6. Typical Water Test Results Meets CPCB Norm ● BOD < 10mg/L ● TSS < 10mg/L ● COD < 50mg/L
  • 8. CAMUS-SBT vs ASP : Process Flow Aeration Basin Blowers/Diffusers: High Energy and Maintenance Sludge Bed Preliminary Screening WetWell Primary Clarifier Secondary Clarifier Thickener ACF Disinfection sludge recycle BOD: 300 TSS : 300 BOD:30 TSS:20 BOD: <10 TSS : <5 Typically CPCB E Preliminary Screening WetWell RST Settler Equilizer Bio Mound (BM1) Bio Mound (BM2) (BM3) BOD: 300 TSS : 300 BOD: 50 TSS : 30 BOD: ~5 TSS : ~1 ACF Disinfection CPCB A CPCB B/C/D Continuous Aerobic Multi-Stage Soil Bio Technology (CAMUS-SBT)
  • 10. Culture Bio Mounds (BM1/2) Soil Liquid Processing Pheretima Elongata White Worms Bio Mounds (BM3) Vermicomposting: Solids Processing Eisenia Fetida Red Worms
  • 11. Technology Comparison Assessment of various wastewater parameters Technologies Performance after Secondary Treatment (BOD<30) CSBT ASP MBBR SBR UASB+ASP MBR WSP Effluent BOD (mg/L) <20 <20 <30 <10 <20 <5 <40 Effluent Suspended Solids (mg/L) <30 <30 <30 <10 <30 <5 <100 Fecal Coliforms (log unit) 6-7 2-3 2-3 3-4 2-3 5-6 2-3 T-NH3 removal efficiency (%) 70-80 10-20 10-20 70-80 10-20 70-80 10-20 Performance after tertiary treatment (BOD<10) Effluent BOD (mg/L) <10 <10 <10 <10 <10 <10 <10 Effluent Suspended Solids (mg/L) <5 <5 <5 <5 <5 <5 <5 Effluent NH4N(mg/L) <1 <1 <1 <1 <1 <1 <1 Effluent TP(mg/L) <0.5 <0.5 <0.5 <0.5 <0.5 <0.5 <0.5 Effluent total coliform MPN/100 ml 10 10 10 10 10 10 10 Area requirement (m2/MLD) Average area secondary treatment (BOD<30) 300 800 450 450 1000 450 6000 Average area secondary treatment (BOD<10) 600 900 550 550 1100 450 6100 Operation & Maintenance Energy consumption in secondary treatment (kwhr/ML) 60 180 220 150 120 300 2 Energy consumption in tertiary treatment(kwhr/ML) 60 180 220 150 120 300 2 Energy consumption for sludge handling(kwhr/ML) 1 1 1 1 1 1 1 Total Energy consumption (kwhr/ML) 121 361 441 301 241 601 5 Chemical requirement Polymer /coagulants Low High High High High High High Disinfection Low High High High High High High Other chemicals Low High High High High High High Skilled Manpower No Yes Yes Yes Yes Yes No Source : Adapted from IIT Kanpur STP comparison Ganga Action Plan : 003_GBP_IIT_EQP_S&R_Ver 1 Dec 2010
  • 12. Process Flow X(KLD) = 5 to 50
  • 13. Typical Small STP (50-500KLD) ● SC: Screen Chamber ● RST: Raw Sewage Tank ● CT: Collection tank ● BR: Bio Reactor 1&2
  • 14. Typical Medium STP (0.5-10MLD) ● FC: Fine Screen Chamber ● GC: Grit Chamber ● TS: Tube Settler ● EQT: Equalization tank ● BM: Bio Mound
  • 15. Typical Medium STP (0.5-10MLD) ● FC: Fine Screen Chamber ● GC: Grit Chamber ● TS: Tube Settler ● EQT: Equalization tank ● BM: Bio Mound
  • 16. Typical Large STP >10MLD ● FC: Fine Screen Chamber ● GC: Grit Chamber ● CLF: Clarifiers ● AD: Anaerobic Digestors ● BM: Bio Mounds
  • 19. Typical Process Walk Through of 25 MLD Plant
  • 20. MediaMedia CAMUS-SBT Media Regeneration Media Organics Adsorb on Media Surface Waste Water percolates on media Clean water Drip down out of the media Bacterial Colonies start growing by feeding on adsorbed organics for food, Media Earthworms (White) Feed on the bacterial Colonies CO2 released CO2 released Media is now available for the next cycle adsorption surface is regenerated by bacterial grazing Grazing by earthworms creates new surface free of bacteria, converting the biomass to CO2
  • 21. Why CSBT: Energetics of Carbon Cycle Atmosphere CO2 750 Live 0 (10 yrs) Water as Dissolved CO2 and Life 4000 Live 1-5 (0.2 yrs) Soil as Dead Reserves 1600 Live 0 (300 yrs) Land as Animals 100-150 Live 150 (2 yrs) Land as Plant 500 Live 500 (50 yrs) Soil as Fossil Fuel 4000 Live 0 (300 yrs) Photosynthesis 110 Respiration 12 Physical Mass Transfer 50 Biological 60 Litter 18 Respiration 60 Human Activities 6 Energy Required for Life ● Land : 3 KJ/g live C/yr ● Water : 500 KJ/g live C/yr 21
  • 23. CSBT Reactor Configurations Chandrashekar S, Shankar HS: Bio-Remediation of Waste Water Streams using SBT: AICHE 2009 CAMUS-SBT is designed with minimal mechanical equipment
  • 24. Frequently Asked Questions • What is the extent of pre-treatment? (How much COD, TSS and TDS are removed) – Fine screens and Grit removal chamber – Equalization tank balances peak flows – Pre-Treatment Primary Clarifier / Tube Settler for BOD and TSS separation – Removal efficiency of 60% is in BOD and TSS in the clarified stream – Clarifier sludge is processed in a Anaerobic Digestor with Phosphate Accumulating Organisms (PAO) – Digested sludge further vermicomposted in BM3 to produced phosphate rich organic fertilizer • What is the range of fluctuating load – CAMUS-SBT plants are designed as per CPHEEO norms as regards to peak flows – Plants are designed to handle flows from 5% to 100% – Shock loads of 30% over design load can accommodated for 1-2 days (requires extra consumables) • flocculant/coagulant dosing to capture more TSS/BOD/COD and load on Bio Mounds • Feed rate or loading rate i.e. Hydraulic and Organic loading rates at each stage? – Fine Screen and Grit Chambers are Designed at Peak Hydraulic Flow – Equalization Tank at CPHEEO norms of 2 hours at peak flow – Clarifiers at Average Hydraulic Flow using 1.5 cum/sqm/hr overflow rate – Anaerobic Digestor designed at 10-20 days detention time – BioMound 1 Hydraulic Loading Rate = 0.1 cum/sqm/hr (2.4 cum/sqm/day), COD loading rate = 0.35 kg/cum/day – Bio Mound 2 designed at Hydraulic Loading Rate = 0.2 cum/sqm/hr (4.8cum/sqm/day), COD loading rate of 0.30 kg/cum/day 24
  • 25. Frequently Asked Questions • What happens to the CAMUS- SBT plants in Monsoon? – Rain water impinging on the Bio reactors will percolate down rapidly and captured in treated water. – Bio reactors are designed for hydraulic percolation rates of upto 5 cum/sqm/day – Heaviest 1 day rainfall ever recorded worldwide is 2.5 cum/sqm/day (Reunion Island) – Cherrapunji on average gets approximately 0.8 cum/sqm/day in monsoons – Overflow in Collection tanks ensure that the Bio Reactor/Bio Mounds is not flooded. • What is the input and output of the CAMUS-SBT? – CAMUS-SBT plants are designed to meet CPHEEO/Client requirements for a given output. • A comparative study of technology with respect to area and costs • upto 1 MLD,1-5MLD, 5-10 MLD, 10-50 MLD etc? – Please see Technology Cost Slides • How are phosphates are removed in the CAMUS-SBT System? – Phosphate removal takes place largely in Raw Sewage Tank / Clarifier / Anaerobic digestor by flocculation/coagulation/settling/bio accumulation via Phosphate accumulating organisms. – Small amounts of Lime (pH management)+FeCl3 is added in the Raw water tank that precipitates the Phosphates as HydroxyApatite. pH of 6.5-7.5 is maintained – In Larger plant the bottom phosphate rich sludge from Clarifier/Settlers is pumped as slurry to BM3 and is converted to vermi compost. – In smaller plants the inorganic sludge at the bottom of Raw Sewage tank is periodically harvested (Once in 4 years) – The biomounds themselves remove approximately 2mg/L 25
  • 26. Our Partner Initiatives • Zerodor Waterless Urinals – Ekam Eco Solutions, IIT Delhi • DrySan Waterless Toilet – CTECH, IDC IIT Bombay • Air Quality (AQI) Monitoring System – Indiaspend, IIT Bombay • Water Quality Monitoring System – Logic Ladder • Intercepted / Small Bore Sewers – Clearford