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Innovations in Oxidation Technologies to treat difficult wastewaters Dr Peter Barratt Business Manager Environmental & Clean Technology Air Products (Europe) Oxidation: The range of technologies Ozone Thermal Wet Oxidation Ozone Non- or poorly& biodegradable Biological Incineration Organic Component Aerobic Biological Stabilization or Thermal Wet Oxidation Aerobic Biological Biodegradable 1 2 3 4 5 Organics Concentration (%) Requiring Destruction 2 TNAV April 2005 10 High Purity Oxygen in Water for Aerobic Biology… why? Increased Saturation Concentration (Cs) – Oxygen in Air – Oxygen = = 9.1mg/l @ 20oC 43 mg/l @ 20oC Rate of Oxygen Mass Transfer – dC/dt = KLa (Cs - C) – Pure oxygen maximises the oxygen deficit, so oxygen dissolves faster Process benefits – Microbes enjoy well oxygenated conditions 3 TNAV April 2005 The Activated Sludge Process Clarifier Feed Mixed Liquor or “Sludge” Treated water Settled Sludge Returned Activated Sludge (RAS) Excess Sludge 4 TNAV April 2005 The Activated Sludge Process Clarifier Feed Treated water Mixed Liquor or “Sludge” OXYGEN 5 TNAV April 2005 Settled Sludge Returned Activated Sludge (RAS) Excess Sludge OXYGEN Classical Oxygenation by sidestream oxygen injection Pure Oxygen Typically from Liquid Oxygen The OXY-DEP® process Venturi-type device Secondary Ejector Water Intake Recirculation Pump 6 TNAV April 2005 Activated Sludge Basin Paper Industry lagoon 7 TNAV April 2005 New development OXY-DEP® VSA On-site generated oxygen Technology – Oxygen generator (Vacuum Swing Absorption) linked to a low energy mixer – Standard sizes: • 150 lpm (262kg/d) • 500 lpm (875kg/d) • 2800 lpm (5000kg/d) – Simplicity and cost in line with aeration – Process benefits of oxygen 8 TNAV April 2005 OXY-DEP® VSA OXYGEN GENERATOR MIXER-OXYGENATOR 9 TNAV April 2005 Aerobic Biological Treatment Aeration • Typically 1 - 2kgCOD/m3/day – MLSS 1.5 – 5g/l • Up to 0.5kgNH3-N/m3/day Oxygenation • High Rate Biological Treatment processes – Typically 2 – 5kgCOD/m3/day • MLSS 3 – 20g/l – Up to 5kgNH3-N/m3/day 10 TNAV April 2005 OXY-DEP® MB Process Membrane OXY-DEP reactor Effluent O2 Inlet Feed 11 TNAV April 2005 Wash tank OXY-DEP® MB benefits Refractory COD is treatable High rate system – Above 30kgCOD/m3/day Low waste sludge production rate – zero in 3 months (rendering) Provides potentially re-usable water 12 TNAV April 2005 Oxygen - common uses in aerobic biological treatment Increase treatment capacity of an existing aerated plant Reduce odours, foams and aerosols Cater for peak organic and ammonia loads as required Improve sludge quality Reduce regulatory risk and improve environmental image 13 TNAV April 2005 Direct Ambient Oxidation Oxidation Processes • Rising Main Injection (sewers) – avoids H2S and corrosion • Sulphide (S-) Oxidation – e.g. lagoons • Ozone – Hard COD and colour removal O2 & O3 14 TNAV April 2005 Ozone Unstable oxidant Generated on site Precursor to .OH Water treatment In conjunction with biological treatment 15 TNAV April 2005 CHEMOX Reactor for O3 Gas Outflow Impinging Zone Liquid Outflow Guide Tube Main Tube Nozzle Liquid Feed Gas Inflow Pump 16 TNAV April 2005 CHEMOX - landfill leachate Existing Plant CHEMOX 1.8 O3 :COD ratio* > 2.2 4 hours HRT 10.3 hours 500 mg/l CODin 500 mg/l <150 mg/l CODout <150 mg/l 4 kWh/kgO3 Powerdiss 8 kWh/kgO3 *: 17 TNAV April 2005 ozone applied/COD removed CHEMOX - landfill leachate Existing Plant CHEMOX 1.8 O3 :COD ratio* 4 hours > 2.2 10.3 hours COST ADVANTAGE 500 mg/l COD 500 mg/l HRT in <150 mg/l CODout <150 mg/l 4 kWh/kgO3 Powerdiss 8 kWh/kgO3 17% lower in capital 29% lower in operation * : ozone applied/COD removed 18 TNAV April 2005 Other Ozone Applications Sludge solids oxidation – Activated sludge in-process Pathogen removal in reused water Alternative clean oxidant in chemical synthesis Selective destruction of problem bacteria e.g. bulking 19 TNAV April 2005 Oxygen reuse technology after ozone production Normally, conversion of O2 to O3 is 6% to 12% by weight. Therefore: – Oxygen off-gas use in other processes – Long Loop Recycle (LLR) – Short Loop Recycle (SLR) • O2 and O3 separated after the ozoniser, and O2 recycled to produce O3 • 98% conversion of O2 20 TNAV April 2005 SLR Benefits - example Straight Through Total $2.50 40% Savings Cost $2.00 15% Savings SLR Total $1.00 $0.50 4 Capital Power Oxygen 8 12 16 Ozone Concentration [wt%] 21 TNAV April 2005 tell me more www.airproducts.com Please see our web-based Wastewater Treatment Plant Risk Assessment tool