Schedule No 11: Commitments on Unit Rates for OPEX Schedule 11.1 Hydraulic Load Schedule 11.2 Organic Load Schedule 11.4 Chemical for Sludge Conditioning Schedule 11.5 Chemical for Phosphorus Removal Schedule 11.6 Chemical for Nitrogen Removal Item No Parameter Unit 25% 50% 75% 100% a Flow m$^{3}$/year 2.132.330,00 4.264.660 6.396.990 8.529.320 b Tenderer's Power Consumption for Hydraulic Load kWh/year c Unit Rate (c=b/a) kWh/m 3 0,00000 0,00000 0,00000 0,00000 HYDRAULIC LOAD Item No Parameter Unit 25% 50% 75% 100% a Inlet Organic Load (at the plant inlet) kg COD/year 1.048.645 2.097.290 3.145.935 4.194.580 b Tenderer's Value for Organic Load at the Effluent kg COD/year c Tenderer's Value for Organic Load Removed (c=a-b) kg COD/year 1.048.645 2.097.290 3.145.935 4.194.580 d Tenderer's Power Consumption for Organic Load kWh/year e Unit Rate (e=d / c) kWh/kg COD  removed 0,00000 0,00000 0,00000 0,00000 ORGANIC LOAD Item No Parameter Unit 25% 50% 75% 100% a Inlet Suspended Solid Load (at the plant inlet) kg SS/year 579.255 1.158.510 1.737.765 2.317.020 b Tenderer's Value for Dried Sludge kg SS dried/year c Tenderer's Power Consumption for Sludge Load kWh/year d Unit Rate (d=c / b) kWh/kg SS  removed #DIV/0! #DIV/0! #DIV/0! #DIV/0! SLUDGE LOAD Item No Parameter Unit 25% 50% 75% 100% a Inlet Suspended Sludge Load (at the plant inlet) kg SS/year 579.255 1.158.510 1.737.765 2.317.020 b Tenderer's Value for Amount of Excess Slduge kg SS/year c Tenderer's Chemical Consumption for Excess Sludge  Thickening (as dry polymer) kg PE/year d Tenderer's Value for Dewatered Sludge kg SS  dewatered/year e Tenderer's Chemical Consumption for Sludge Dewatering  (as dry polymer) kg PE/year f Tenderer's Total Chemical Consumption for Sludge  Conditioning (as dry polymer) (f=c+e) kg PE/year g Unit Rate (g=f / d) kg PE/kg SS  removed #DIV/0! #DIV/0! #DIV/0! #DIV/0! Item No Parameter Unit 25% 50% 75% 100% a Total Phosphorus Load (at the plant inlet) kg TP /year 20.714 41.428 62.141 82.855 b Total Phosphorus Load at the Effluent kg TP /year 2.132 4.265 6.397 8.529 c Total Phosphorus Load Removed (c = a - b) kg TP /year 18.581 37.163 55.744 74.326 d Tenderer's Chemical Consumption for Phosphorus  Removal (as 40% FeCl3) kg FeCl3 /year e Unit Rate (e = d/c) kg FeCl3 / kg TP removed - - - CHEMICAL FOR PHOSPHORUS Schedule 11.3 Sludge Load