| Process Model Objects | Variable | Unit | Value | Process Model Objects | Variable | Unit | Value |
| Anoxic Tank-1 | Maximum Volume Tank Depth Pumped Flow Initial Reactor Volume Start with Full Tank | m3 m m3/hr m3 | 307.2 6.0 170.0 270.0 Off | Air Blower | Solids Capture Rate Flowrate | % Nm3/hr | 95.0 650 |
| Aeration Tank-1 | Tank Depth Maximum Volume Pumped Flow | M m3 m3/hr | 6.0 328.0 70.0 | Clarifier | Surface Area Depth Pumped Flow Sludge Disposal Cost | m2 m m3/hr $/m3 | 44.8 3.5 70.0 553.6 |
| CH3COOH Dosing | Chemical Purity Cost of Chemical Flowrate | % $/kg L/hr | 45.0 1.03 31.0 | Polymer Dosing | Use Local Temperature Local Liquid Temp. Chemical Type Chem. Dosage, in Mass Chemical Purity Cost of Chemical |
C
Kg/hr % $/ kg | On 21.0 PAC-Al2(OH)n cl(6n) 450.0 0.2 2.0 |
| NaOH Dosing | Use Local Temperature Local Liquid Temp. Chemical Purity Cost of Chemical Flowrate |
C % $/KG L/hr | On 21.0 50.0 0.42 6.0 | Sludge Buffer Sump | Maximum Volume Tank Depth Pumped Flow Initial Reactor Volume Start with Full Tank | m3 m m3/hr m3 | 230.0 6.0 70.0 192.0 Off |
| Anoxic Tank-2 | Maximum Volume Tank Depth Initial Reactor Volume Start with Full Tank | m3 m m3 | 153.6 6.0 140.0 0ff | Sludge Thickener | Surface Area Depth Pumped Flow Sludge Disposal Cost | m3 m m3/hr $/m3 | 18.5 3.5 19.0 553.6 |
| Aeration Tank-2 | Tank Depth Maximum Volume Pumped Flow | M m3 m3/hr | 6.0 140.0 170.0 | Sludge Centrifuge | Pumped Flow Sludge Disposal Cost | m3/hr $/m3 | 1.75 553.5 |
| FeCl3 Dosing | Chem. Dosage, in Mass Chemical Purity Cost of Chemical | Kg/hr % $/kg | 7197 40 0.26 | NaOCl Dosing | Use Local Temperature Local Liquid Temp. Chemical Type Chemical Purity Cost of Chemical Flowrate |
C
% $/kg L/hr | On 22.0 Sodium Hypochlorite 10.0 0.16 10.0 |
| Treated Wastewater | Maximum TDS Max. Total Hardness | mg/L mg/L | 30.0 120.0 |
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| Sludge Disposal | Sludge Disposal Cost | $/tonne | 55.36 |
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| System | Ratio of Soluble BOD to soluble COD Liquid Temperature Blower Inlet Air Temp. |
% C C |
93.3 43.0 32.0 |
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