Item No Parameter Unit 25% 50% 75% 100% a Inlet Total Nitrogen Load (at the plant inlet) kg TN/year 115.705 231.410 347.115 462.820 b Tenderer's Value for TN Load at the Effluent kg TN/year c Tenderer's Value for TN Load Removed (c=a-b) kg TN/year 115.705 231.410 347.115 462.820 d Tenderer's Chemical Consumption for Nitrogen Removed kg  methanol/year e Unit Rate (e=d / c) kg methanol/kg  TN removed 0,00000 0,00000 0,00000 0,00000 Item No Parameter Unit 25% 50% 75% 100% a Inlet Suspended Solid Load (at the plant inlet)GLYPH<10> 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 Natural Gas Consumption for Dried Sludge Sm3/year d Unit Rate (d = c/b) Sm3/kg SS dried #DIV/0! #DIV/0! #DIV/0! #DIV/0! SLUDGE LOAD Item No Parameter Unit 25% 50% 75% 100% a Total power consumption kWh/year 0,00 0,00 0,00 0,00 b Power production by CHP(s) kWh/year c Net Power Consumption (c = a-b) kWh/year - - - - POWER PRODUCTION Schedule 11.7 Natural Gas for Sludge Drying Schedule 11.8 Compensation of Power Consumption (person(s) authorised to sign on behalf of the tenderer) Signature........................................................... Date: ...........................................