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EEESD’08  The 4th IASME/WSEAS International Conference  Algarve, Portugal, June 11-13, 2008 IMPLEMENTATION OF CLEAN DEVELOPMENT MECHANISM (CDM) METHODOLOGIES IN NATURAL GAS CHP PLANT
Table of contents ,[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object]
Introduction ,[object Object],[object Object],[object Object],[object Object],[object Object],[object Object]
Analysis of energy requirements in “Sojaprotein”  ,[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object]
Analysis of energy requirements in “Sojaprotein”  Annual energy consumption and energy costs in Sojaprotein.  Basic units Conversion factor Energy consumption Energy costs [GJ] [€] Natural gas 10412213 [m 3 ] 0,0342 355995,72 2   825   669,2 Electricity  24867840  [kWh] 3.6 x 10 –3 89524,22 856   495,8 Total:  445 519,9 3 682 165
Analysis of energy requirements in “Sojaprotein” ,[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object]
Analysis of energy requirements in “Sojaprotein” ,[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object]
Cogeneration plant selection Nominal Operation Characteristics of Cogeneration Plant .  Load [%] 100 100 100 100 100 Inlet Air Temperature  [°C] 11 -20 0  10 20 Power [MW] 10.5 5 11. 90 11.1 8 10.6 1 9.9 4 Efficiency Factor, Electric [%] 31.9 5 32.4 8 32.3 1 31.9 6 31.5 0 Combustion Products Quantity [kg/s] 41.80 46. 20 43.6 7 41.9 8 40.0 6 Outlet Combustion Products Temp.  [°C] 487 459 477 486 494
Cogeneration plant selection
Techno – economic study Costs = investment + maintenance + additional quantity of gas for cogeneration plant  Income = generated electricity  UNPROFITABLE (annual profit < annual costs) Actual electricity price for industry, being significantly lower from electricity price in neighborhood countries! ( Hungary  0,1012 e/kWh,  Romani a 0,0894 e/kWh,  Bu lgaria  0,0588 e/kWh  the price include all taxes  2007.) Investment Cost O&M Cost Gas price Electricity price 5000000 [e] 15  [e/h] 0,29 [e/m 3 ] 0,0366 [e/kWh]
CDM project and CHP ,[object Object],[object Object],[object Object],[object Object],Some approved CDM methodology applicable for combined energy production projects: ACM002, ACM006, ACM0012, AM0014, AM0024, AM0036.
Selection of CDM methodology Applicability of the mentioned methodologies is influenced directly by the conditions defined within each methodology. Based on the analysis carried out on the applicability of methodologies,   AM0014   was selected. Methodology AM0014 enable its application for combined heat and power generation, using natural gas as a fuel, with certain limitations.
Application of CDM methodology Baseline Scenario – Power and Heat Energy Supply Through applied methodology AM0014 for the selected CHP plant in Sojaprotein,  the achieved savings could be  51,034.5 eq/year  or approx.  360,000 €/year , using equivalent emission value for 1t CO 2  eq = 7 euro . Heat Energy Supply Power Supply Existing facility From existing boiler house using  natural gas as a fuels Grid-connected New SPI Plant Construction of a new boiler house, using natural gas as a fuel Grid-connected
Application of CDM methodology ABEC BF  - Annual baseline scenario energy consumption [GJ/year] 455,600 CAHO - Annual heat energy production in a combined plant  [GJ/year] 410,040 e b  - Coefficient of efficiency for boilers in industrial facilities (proposed value for calculation) [-] 0.9 AOH - Annual operation hours of facility [h/year] 6700 NoWD - Number of working days [w.d./year] 335 Baseline scenario TBE th  - Total equivalent emission of CO 2,  produced by natural gas combustion in baseline scenario t CO 2 /year 103,591 Project scenario TPE th Total equivalent emission of CO 2,  produced by natural gas combustion in project scenario  t CO 2 /year 52 556,5 Achieved savings through CDM project application:  t CO 2 /year 51 034,5
Conclusion   Based on the results obtained from techno-economic study, it could be concluded that the construction of selected cogeneration plant is unprofitable one in this moment, due to an actual power cost . Referring the selection of CDM methodology for combined power and heat energy, the analysis of approved methodologies was done . O nly the technical analysis of CDM project application is shown in this paper, without any financial analysis, as well as any analysis of the project “supplementary“ .
Conclusion   ,[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object]

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Presentation Durosevic IASME 08

  • 1. EEESD’08 The 4th IASME/WSEAS International Conference Algarve, Portugal, June 11-13, 2008 IMPLEMENTATION OF CLEAN DEVELOPMENT MECHANISM (CDM) METHODOLOGIES IN NATURAL GAS CHP PLANT
  • 2.
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  • 4.
  • 5. Analysis of energy requirements in “Sojaprotein” Annual energy consumption and energy costs in Sojaprotein. Basic units Conversion factor Energy consumption Energy costs [GJ] [€] Natural gas 10412213 [m 3 ] 0,0342 355995,72 2 825 669,2 Electricity 24867840 [kWh] 3.6 x 10 –3 89524,22 856 495,8 Total: 445 519,9 3 682 165
  • 6.
  • 7.
  • 8. Cogeneration plant selection Nominal Operation Characteristics of Cogeneration Plant . Load [%] 100 100 100 100 100 Inlet Air Temperature [°C] 11 -20 0 10 20 Power [MW] 10.5 5 11. 90 11.1 8 10.6 1 9.9 4 Efficiency Factor, Electric [%] 31.9 5 32.4 8 32.3 1 31.9 6 31.5 0 Combustion Products Quantity [kg/s] 41.80 46. 20 43.6 7 41.9 8 40.0 6 Outlet Combustion Products Temp. [°C] 487 459 477 486 494
  • 10. Techno – economic study Costs = investment + maintenance + additional quantity of gas for cogeneration plant Income = generated electricity UNPROFITABLE (annual profit < annual costs) Actual electricity price for industry, being significantly lower from electricity price in neighborhood countries! ( Hungary 0,1012 e/kWh, Romani a 0,0894 e/kWh, Bu lgaria 0,0588 e/kWh the price include all taxes 2007.) Investment Cost O&M Cost Gas price Electricity price 5000000 [e] 15 [e/h] 0,29 [e/m 3 ] 0,0366 [e/kWh]
  • 11.
  • 12. Selection of CDM methodology Applicability of the mentioned methodologies is influenced directly by the conditions defined within each methodology. Based on the analysis carried out on the applicability of methodologies, AM0014 was selected. Methodology AM0014 enable its application for combined heat and power generation, using natural gas as a fuel, with certain limitations.
  • 13. Application of CDM methodology Baseline Scenario – Power and Heat Energy Supply Through applied methodology AM0014 for the selected CHP plant in Sojaprotein, the achieved savings could be 51,034.5 eq/year or approx. 360,000 €/year , using equivalent emission value for 1t CO 2 eq = 7 euro . Heat Energy Supply Power Supply Existing facility From existing boiler house using natural gas as a fuels Grid-connected New SPI Plant Construction of a new boiler house, using natural gas as a fuel Grid-connected
  • 14. Application of CDM methodology ABEC BF - Annual baseline scenario energy consumption [GJ/year] 455,600 CAHO - Annual heat energy production in a combined plant [GJ/year] 410,040 e b - Coefficient of efficiency for boilers in industrial facilities (proposed value for calculation) [-] 0.9 AOH - Annual operation hours of facility [h/year] 6700 NoWD - Number of working days [w.d./year] 335 Baseline scenario TBE th - Total equivalent emission of CO 2, produced by natural gas combustion in baseline scenario t CO 2 /year 103,591 Project scenario TPE th Total equivalent emission of CO 2, produced by natural gas combustion in project scenario t CO 2 /year 52 556,5 Achieved savings through CDM project application: t CO 2 /year 51 034,5
  • 15. Conclusion Based on the results obtained from techno-economic study, it could be concluded that the construction of selected cogeneration plant is unprofitable one in this moment, due to an actual power cost . Referring the selection of CDM methodology for combined power and heat energy, the analysis of approved methodologies was done . O nly the technical analysis of CDM project application is shown in this paper, without any financial analysis, as well as any analysis of the project “supplementary“ .
  • 16.