Construction of Giresun Wastewater Treatment Plant  Tender Dossier Volume 3 Employer’s Requirements  74 of 74  3.5.2.3 Non-performance Damage for failure to meet the Chemical Consumption for Nitrogen  Removal  3.5.3 Non-Performance Damages for failure to meet the natural gas consumption  commitment  3.5.4 Non-performance Damage for failure to meet the Spare Parts Guarantee  3_Vol3_d4.3_Section 3_Plant Description_GIR_rev08  The amount of spare parts written in Schedule 10.6 of Volume 4 is only for tender evaluation purpose.  Non-performance damage is not applicable for this item.  N; a fixed number as determined in the Employer Requirements (10 in here)  The non-performance damage to be paid to the Employer by the Contractor in the event of the actual  consumption is more than committed shall be calculated as follows:  Value = [kg Methanol / kg T-N removed (actual) – kg Methanol / kg T-N removed (committed) x  annual T-N load x cost of chemical x N  kg Methanol / kg T-N removed (actual) = the measured and calculated chemical consumption in kg  Methanol/kg T-N removed as follows:  Actual annual methanol consumption measured for total nitrogen removal as explained above divided  by the measured actual annual removed total nitrogen.  kg Methanol / kg T-N removed (committed) = committed chemical consumption in kg Methanol /kg  T-N removed as follows:  Unit rates given in Schedule 11.6 by the Contractor shall be calculated according to the actual T-N  load as explained above.  Annual Total nitrogen load is the average total nitrogen load for Stage 1 which is  462,820  kg Cost of chemical (methanol) = 500 € /ton  N; a fixed number as determined by the Employer ( 10  in here)  The non-performance damage to be paid to the Employer by the Contractor in the event of the actual  consumption is more than committed shall be calculated as follows:  Value = [m$^{3}$ (actual) –m$^{3}$ (committed)] x annual suspended solid load x cost of gas x N  m$^{3}$ (actual) = the measured liquefied natural gas consumption in m$^{3}$ as follows: Actual annual gas consumption measured for the sludge drying plant as explained above divided by  the actual annual solid measured  kWh/m$^{3}$ (committed) = committed gas consumption in kWh/m3 as follows:  Unit rates given in Schedule 11.7 by the Contractor shall be calculated according the actual suspended  solid load as explained above.  Annual Suspended Solid load is the average SS load for Stage 1 – 2032 which is  2,317,020  kg  Cost of gas = 0.550 € / m$^{3}$ (based on standardized liquefied natural gas corresponding to 9155  kcal/m$^{3}$) 