Soneerawater Treatment system overview ⢠Continuous flow system using electrolysis â Filter and membrane free â 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 40â 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 â 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 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 1300 (est) 99.9 E. coli 1,800,000 9,000 99.5 BOD5 102.60 4.5 95.6 COD 145,500 5,320 96.3 Total Kjeldahl Nitrogen 81 46 43.2 Total Nitrogen 48 34 29.2 Nitrate 4.20 0.20 95.2 Ammonia-N 0.24 88.9 Oxidised-N 0.20 50 TOC 6,091 36.8 99.40 TSS 1,900 19 99.00 Colour 24.20 95.9 Turbidity >2000 20 >99 Oil & Grease 81,440 20 99.98 Grease 150 98 Petroleum Hydrocarbons 1,200 15 98.8 Ethanol 9.30 99.5 Acetone 0.69 94.2 Benzene 0.12 99.2 Toluene 0.99 99.9 Ethyl Benzene 2.1 99.8 Xylenes 4.8 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 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 X 35 increase Iron 1.009 0.014 98.7 Lead 5.4 99.8 Magnesium 5.6 2.5 55.4 Manganese 0.28 96.4 Nickel 0.02 0.003 85 Phosphorus 27.5 0.4 98.5 Selenium 0.04 0.01 75 Tin 0.85 98.8 Titanium 1.1 99.1 Vanadium 0.8 87.5 Zinc 180 0.42 99.8 Arizona-based Operational System Treating raw sewage at Surprise WWTP Floating the contaminants Removing the waste (Click picture & press play at bottom right) Treatment results in Phoenix Raw sewage & trade waste (press play) Small footprint - 125,000 GPD Skid Mounted â highly mobile 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 â 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 stormwater and mining effluent before it enters the National Park and drinking water catchment. Delivering 350,000gal/day 2. Small 20â 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 Points of Contact Glen Marshall Michael Stevens CEO VP Manufacturing & Operations Ph: +1 480 570 1852 Ph: +1 480 319 3558 E: [email protected] E: [email protected] Darrell Behan COO Ph: +1 480 570 2703 E: [email protected]