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Soneerawater
Treatment system overview
• Continuous flow system using electrofloccultraton
– Filter and membrane free
– No added chemicals, reagents, flocculants or clarifiers
• Removes the widest array of contaminants
• Power saving up to 80%
• Opex cost saving up to 80%
• A 40’ container can treat up to 0.2MGD
Technology overview: How the process works
Effluent Enters Clean water in end
chamber
Chemical reactions occur in
middle chambers
Technical Aspects
• Uses a bubble – ion barrier to remove pollutants
• Pollutants automatically removed during operation
• Removes most pollutants better than DAF
• Removal rates typically 95% to 98%
• Power usage depends upon pollutant loading, typically 0.3 to
0.7kWh/m3
• Fast throughput, typically 1hr from polluted to cleaned water
• Fully scalable
Treatment Capability
 Halogenated hydrocarbons
 Benzene ring structures
 Most natural and many synthetic dyes
 Ink, pigments and paint
 Monomers and polymers
 Decaying animal and vegetable matter
 Asbestos, clay and other suspended
solids
 Some low atomic number ions, B, F ,Mg,
Al, Ca
 Nitrates and nitrites
 Removal of other Kjeldahl nitrogen
variable
 BOD/COD – large molecules
<300ug/MOL difficult to remove
 Free and emulsified fats, oils, grease
 >C6 Hydrocarbons
 Cations with atomic number>23
 (including hexavalent chromium)
 Anions with atomic number >33
(including bromide and iodide)
 Chemicals such as cyanide, arsenate,
phosphate
 Pathogens such as algae, bacteria and
viruses
 Soaps and detergents (MBAS active
substances)
 Removal of radioactive contaminants
Process Results
1. Oil & petroleum in stagnant water with algae treated in 60 minutes
2. Raw sewage treated within 45 minutes
Removal
Rates
Material Raw
mg/L
Cleaned
mg/l
% Removal
Faecal Coliforms 72,000,000.00 1300 (est) 100.00
E. coli 1,800,000.00 9,000.00 99.50
BOD5 102.60 4.50 95.60
COD 145,500.00 5,320.00 96.30
Total Kjeldahl Nitrogen 81.00 46.00 43.20
Total Nitrogen 48.00 34.00 29.20
Nitrate 4.20 0.20 95.20
Ammonia-N 0.24 <0.03 >88.9
Oxidised-N 0.20 <0.1 >50
TOC 6,091.00 36.80 99.40
TSS 1,900.00 19.00 99.00
Colour 24.20 <1 >95.9
Turbidity >2000 20.00 >99
Oil & Grease 81,440.00 20.00 99.98
Grease 150.00 <3 >98
Petroleum Hydrocarbons 1,200.00 15.00 98.80
Ethanol 9.30 <0.05 >99.5
Acetone 0.69 <0.05 >94.2
Benzene 0.12 <0.001 >99.2
Toluene 0.99 <0.001 >99.9
Ethyl Benzene 2.1 <0.005 >99.8
Xylenes 4.8 <0.005 >99.9
TRH C6-C9 8.7 0.002 >99.8
TRH C10-C14 9.1 2.6 71.4
Aluminium 16 0.66 95.9
Arsenic 0.73 0.01 98.6
Barium 5.6 0.13 97.7
Boron 0.42 0.17 59.5
Cadmium 0.049 <0.001 >98
Calcium 36 16 55.6
Cobalt 0.06 0.01 83.3
Copper 260 0.27 99.9
Dissolved Oxygen 0.26 8.9 97.1
Iron 1.009 0.014 98.7
Lead 5.4 <0.01 >99.8
Magnesium 5.6 2.5 55.4
Manganese 0.28 <0.01 >96.4
Nickel 0.02 0.003 85
Phosphorus 27.5 0.4 98.5
Selenium 0.04 0.01 75
Tin 0.85 <0.01 >98.8
Titanium 1.1 <0.01 >99.1
Vanadium 0.8 <0.01 >87.5
Zinc 180 0.42 99.8
Arizona Demonstration System
Treating sewage at Surprise WWTP
Floating the contaminants
Removing the waste
Treatment results from Surprise WWTP
• Raw Sewerage
to
• Clean Water
Unique Features
• No filters to clog; No chemicals to pollute
• 98% of contaminants removed
• Very low energy use - typically 20kW for 275,000 GPD
• Can be solar powered
• Automated process with Remote monitoring
• Scalable from 10,000G/D to over 10MG/D
• Complements other water treatment processes
• Very small footprint – 0.2MGD fits into a shipping container
• Less than 5% of the water is removed with the waste
• The waste is inert, non leachable; suitable for landfill or fertilizer
• Highly suitable system for environmentally sensitive sites
Australian Systems
1. Operational mine site in Sydney. Tasked to clean storm water and mining effluent before
it enters the National Park and drinking water catchment. Delivering 200,000gal/day
2. Small 20’ system at the Adelaide sewage plant
3. Other sites include:
a. Providing drinking water in National parks
b. Providing drinking water in two State prisons
c. Providing drinking water in a large seasonal caravan park
d. Cleaning ballast water from a Sydney Marina
e. Recycling water used to clean council garbage trucks
f. Providing primary and secondary treatment for a food manufacturer
Trade Demonstration Day at Surprise WWTP
Small footprint and mobile
Point of Contact
Darrell Behan Peter Thusat
CEO VP Marketing
Ph: +1 480 570 2703 Ph: +1 216 221 1233
E: darrell@soneerawater.com E: peter@soneerawater.com

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Electroflocculation Water Treatment System Removes 80% of Contaminants

  • 2. Treatment system overview • Continuous flow system using electrofloccultraton – Filter and membrane free – No added chemicals, reagents, flocculants or clarifiers • Removes the widest array of contaminants • Power saving up to 80% • Opex cost saving up to 80% • A 40’ container can treat up to 0.2MGD
  • 3. Technology overview: How the process works Effluent Enters Clean water in end chamber Chemical reactions occur in middle chambers
  • 4. Technical Aspects • Uses a bubble – ion barrier to remove pollutants • Pollutants automatically removed during operation • Removes most pollutants better than DAF • Removal rates typically 95% to 98% • Power usage depends upon pollutant loading, typically 0.3 to 0.7kWh/m3 • Fast throughput, typically 1hr from polluted to cleaned water • Fully scalable
  • 5. Treatment Capability  Halogenated hydrocarbons  Benzene ring structures  Most natural and many synthetic dyes  Ink, pigments and paint  Monomers and polymers  Decaying animal and vegetable matter  Asbestos, clay and other suspended solids  Some low atomic number ions, B, F ,Mg, Al, Ca  Nitrates and nitrites  Removal of other Kjeldahl nitrogen variable  BOD/COD – large molecules <300ug/MOL difficult to remove  Free and emulsified fats, oils, grease  >C6 Hydrocarbons  Cations with atomic number>23  (including hexavalent chromium)  Anions with atomic number >33 (including bromide and iodide)  Chemicals such as cyanide, arsenate, phosphate  Pathogens such as algae, bacteria and viruses  Soaps and detergents (MBAS active substances)  Removal of radioactive contaminants
  • 6. Process Results 1. Oil & petroleum in stagnant water with algae treated in 60 minutes 2. Raw sewage treated within 45 minutes
  • 7. Removal Rates Material Raw mg/L Cleaned mg/l % Removal Faecal Coliforms 72,000,000.00 1300 (est) 100.00 E. coli 1,800,000.00 9,000.00 99.50 BOD5 102.60 4.50 95.60 COD 145,500.00 5,320.00 96.30 Total Kjeldahl Nitrogen 81.00 46.00 43.20 Total Nitrogen 48.00 34.00 29.20 Nitrate 4.20 0.20 95.20 Ammonia-N 0.24 <0.03 >88.9 Oxidised-N 0.20 <0.1 >50 TOC 6,091.00 36.80 99.40 TSS 1,900.00 19.00 99.00 Colour 24.20 <1 >95.9 Turbidity >2000 20.00 >99 Oil & Grease 81,440.00 20.00 99.98 Grease 150.00 <3 >98 Petroleum Hydrocarbons 1,200.00 15.00 98.80 Ethanol 9.30 <0.05 >99.5 Acetone 0.69 <0.05 >94.2 Benzene 0.12 <0.001 >99.2 Toluene 0.99 <0.001 >99.9 Ethyl Benzene 2.1 <0.005 >99.8 Xylenes 4.8 <0.005 >99.9 TRH C6-C9 8.7 0.002 >99.8 TRH C10-C14 9.1 2.6 71.4 Aluminium 16 0.66 95.9 Arsenic 0.73 0.01 98.6 Barium 5.6 0.13 97.7 Boron 0.42 0.17 59.5 Cadmium 0.049 <0.001 >98 Calcium 36 16 55.6 Cobalt 0.06 0.01 83.3 Copper 260 0.27 99.9 Dissolved Oxygen 0.26 8.9 97.1 Iron 1.009 0.014 98.7 Lead 5.4 <0.01 >99.8 Magnesium 5.6 2.5 55.4 Manganese 0.28 <0.01 >96.4 Nickel 0.02 0.003 85 Phosphorus 27.5 0.4 98.5 Selenium 0.04 0.01 75 Tin 0.85 <0.01 >98.8 Titanium 1.1 <0.01 >99.1 Vanadium 0.8 <0.01 >87.5 Zinc 180 0.42 99.8
  • 9. Treating sewage at Surprise WWTP
  • 12. Treatment results from Surprise WWTP • Raw Sewerage to • Clean Water
  • 13. Unique Features • No filters to clog; No chemicals to pollute • 98% of contaminants removed • Very low energy use - typically 20kW for 275,000 GPD • Can be solar powered • Automated process with Remote monitoring • Scalable from 10,000G/D to over 10MG/D • Complements other water treatment processes • Very small footprint – 0.2MGD fits into a shipping container • Less than 5% of the water is removed with the waste • The waste is inert, non leachable; suitable for landfill or fertilizer • Highly suitable system for environmentally sensitive sites
  • 14. Australian Systems 1. Operational mine site in Sydney. Tasked to clean storm water and mining effluent before it enters the National Park and drinking water catchment. Delivering 200,000gal/day 2. Small 20’ system at the Adelaide sewage plant 3. Other sites include: a. Providing drinking water in National parks b. Providing drinking water in two State prisons c. Providing drinking water in a large seasonal caravan park d. Cleaning ballast water from a Sydney Marina e. Recycling water used to clean council garbage trucks f. Providing primary and secondary treatment for a food manufacturer
  • 15. Trade Demonstration Day at Surprise WWTP Small footprint and mobile
  • 16. Point of Contact Darrell Behan Peter Thusat CEO VP Marketing Ph: +1 480 570 2703 Ph: +1 216 221 1233 E: darrell@soneerawater.com E: peter@soneerawater.com