UNECE Convention on Long-range Transboundary Air Pollution

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Presentation transcript:

UNECE Convention on Long-range Transboundary Air Pollution Improvements of the EGTEI Cost Calculation Tool for Emission Reduction Measures in LCPs EGTEI Technical Secretariat 08 October 2014

Agenda Current tool and methodology Implementation of new development UNECE Convention on Long-range Transboundary Air Pollution Agenda Current tool and methodology Implementation of new development VBA-Programming EPA-Method for NOx Part Load Operation Use of sodium bicarbonate as reagent for DSI FGD Next Steps

Agenda Current tool and methodology Implementation of new development UNECE Convention on Long-range Transboundary Air Pollution Agenda Current tool and methodology Implementation of new development VBA-Programming EPA-Method for NOx Part Load Operation Use of sodium bicarbonate as reagent for DSI FGD Next Steps

What is currently available? UNECE Convention on Long-range Transboundary Air Pollution What is currently available? Methodology for cost estimation of abatement options of SO2, NOx and TSP (Total Suspended Particulates) emissions for Large Combustion Plants (LCP) with a thermal capacity larger than 50 MWth (document describing the methodology) Costs defined for plants constituted of boilers only (one boiler linked to a chimney) Coals, heavy fuel oil, natural gas and biomass co-firing with coal EXCEL tool developed (and its user manual): Costs estimated for different regulatory objectives in term of ELVs (Emission Limit Values) Costs being calculated for a plant with characteristics defined by the user Current tool and methodology

What is currently available? UNECE Convention on Long-range Transboundary Air Pollution What is currently available? Reduction techniques considered: NOx: primary measures, SNCR (Selective Non Catalytic Reduction) and SCR (Selective Catalytic Reduction) TSP: electrostatic precipitator (ESP) and fabric filter (FF) SO2: wet flue gas desulphurisation by limestone forced oxidation (LSFO – Limestone Forced Oxidation), semi dry (LSD - Lime Spray Dryer) and dry desulphurisation (DSI - Duct Sorbent Injection), (with use of lime only) Current tool and methodology

General cost methodology UNECE Convention on Long-range Transboundary Air Pollution General cost methodology   Total annual cost Annualisation of investment   Composition of OPEX   Fixed operating cost   Variable operating cost   P = interest rate | n = equipment lifetime | unit = equipment, reagent and electricity consumption, disposal, etc. Current tool and methodology

General cost methodology UNECE Convention on Long-range Transboundary Air Pollution General cost methodology Coal, oil, gas, solid biomass (wood) in co combustion with coal Fuels Fuel approach Detailed and general approach Plants Boilers Pollutants NOx, SO2, PM Technologies NOx: LNB, SCR, SNCR SO2: wet FGD, lime spray dryer, (dry process to be included) PM: FF, ESP Current tool and methodology

General cost methodology UNECE Convention on Long-range Transboundary Air Pollution General cost methodology Plant and fuel data input Calculation of boiler outlet emission loads Setting stack emission goals Choice of potential abatement technologies Economic assessment Current tool and methodology

Agenda Current tool and methodology Implementation of new development UNECE Convention on Long-range Transboundary Air Pollution Agenda Current tool and methodology Implementation of new development VBA-Programming EPA-Method for NOx Part Load Operation Use of sodium bicarbonate as reagent for DSI FGD Next Steps

Demonstration of the general design and important functions UNECE Convention on Long-range Transboundary Air Pollution VBA Programming Demonstration of the general design and important functions VBA Programming

Conclusion and Discussion UNECE Convention on Long-range Transboundary Air Pollution Conclusion and Discussion Important functions: Input boxes and read-only data Reference Boxes Reduction of options, according to selected measure Drop down menus and checkboxes Reference values and error pop-ups Discussion topics: Currency definition (€ vs. local currency) Printing function Definition of reference values VBA Programming

Reference Values TBD VBA Programming UNECE Convention on Long-range Transboundary Air Pollution Reference Values Category Minimum Maximum Reference Carbon in Ash [% in ash] 25 5 Ash-retained-in-Boiler [% of total ash] 80 S-retained-in-Boiler [% of total sulfur] 10 No. of Catalyst Layers 1 2 Primary Spec. Equipment Investment (liquid/gaseous) [€/kWth] 100 SCR Spec. Equipment Investment (liquid/gaseous) [€/kWth] SNCR Spec. Equipment Investment (liquid/gaseous) [€/kWth] Lifetime Reduction of Catalyst through Biomass Co-firing [%] 60 20 TBD VBA Programming

Agenda Current tool and methodology Implementation of new development UNECE Convention on Long-range Transboundary Air Pollution Agenda Current tool and methodology Implementation of new development VBA-Programming EPA-Method for NOx Part Load Operation Use of sodium bicarbonate as reagent for DSI FGD Next Steps

Methodology is more detailed and complex UNECE Convention on Long-range Transboundary Air Pollution Overview US EPA provided a methodology for emission reduction cost calculation (Reference: Air Pollution Control Cost Manual, US EPA, 2002) The EPA method is implemented in the EGTEI tool for SO2 and PM and shall also be used for NOx The document addresses SCR and SNCR systems (no 1° measures) within these restrictions: Only coal fired systems SNCR with urea as reagent and from 0 to 50% NOx reduction Minimum boiler size: 75 MWth Methodology is more detailed and complex More input data is necessary Accuracy of results may be better (further testing is necessary) Factors for cost calculation are up to 15 years old and hardly perspicuous Slight Modifications are reasonable to fit the needs of EGTEI EPA Method for NOx

Calculation Scheme SNCR UNECE Convention on Long-range Transboundary Air Pollution Calculation Scheme SNCR US EPA Methodology: EGTEI Methodology: Plant and operating characteristics Specific Investment CAPEX Reagent consumption Power consumption OPEX SNCR Plant and operating characteristics Reagent consumption and tank size Plant consumption (Power, Water) Investment and cost calculation (CAPEX, OPEX) EPA Method for NOx

Calculation Scheme SCR UNECE Convention on Long-range Transboundary Air Pollution Calculation Scheme SCR US EPA Methodology: EGTEI Methodology: Plant and operating characteristics Specific Investment CAPEX Reagent consumption Power consumption Catalyst cost OPEX SCR Plant and operating characteristics Catalyst volume SCR reactor dimensions Reagent consumption and tank size Power consumption Catalyst replacement Investment and cost calculation (CAPEX, OPEX) EPA Method for NOx

How to deal with outdated empirical factors? UNECE Convention on Long-range Transboundary Air Pollution Discussion Topics How to deal with outdated empirical factors? EPA as option or as replacement? Modifications: + Catalyst regeneration + Biomass co-firing – Additional coal and ash for vaporization of water in SNCR (insignificant effect) – Correction of errors Testing data available to compare both methods? Part Load Operation

Agenda Current tool and methodology Implementation of new development UNECE Convention on Long-range Transboundary Air Pollution Agenda Current tool and methodology Implementation of new development VBA-Programming EPA-Method for NOx Part Load Operation Use of sodium bicarbonate as reagent for DSI FGD Next Steps

Renewable energies expect rising flexibility of electricity providers UNECE Convention on Long-range Transboundary Air Pollution Goals and Achievments Renewable energies expect rising flexibility of electricity providers Part load operation might be necessary Part load operation Process Temperature Formation of emissions Operation of reduction technologies Process Efficiency Fuel consumption Capacity Factor Specific Reduction Costs Part Load Operation

Part Load Operation Part Load Operation UNECE Convention on Long-range Transboundary Air Pollution Part Load Operation Full Load Hours Fuel Consumption Emission adoptions (NOx) Annual Emissions Emissions per Operating Hour Emissions per Year Boiler Outlet Emissions (per Nm3) LHV Specific Flue Gas Volume Fuel Consumption Flue Gas Volume Part Load Operation

UNECE Convention on Long-range Transboundary Air Pollution Discussion Topics Modeling all the existing steam cycle configurations would completely overload the excel tool and make it unusable Users shall insert net efficiencies at different part load levels as input data Is this data available for both, retrofits and new plants? How big is the typical range? A calculation of the emission factors (especially for NOx) at different part load levels seems to be impossible without complex modeling Are there empirical values? How big is the influence of these effects? Are load levels higher than 100% relevant for practical use? Are there differing design parameters for reduction measures, that are planned to be used in more flexible LCPs? Different injection zones for SNCR Flue gas bypasses for SCR (to bypass the preheater) Part Load Operation

Agenda Current tool and methodology Implementation of new development UNECE Convention on Long-range Transboundary Air Pollution Agenda Current tool and methodology Implementation of new development VBA-Programming EPA-Method for NOx Part Load Operation Use of sodium bicarbonate as reagent for DSI FGD Next Steps

Dry sorbent adsorption UNECE Convention on Long-range Transboundary Air Pollution Dry sorbent adsorption Different configuration possible Different type of reagent possible: lime, sodium bicarbonate… Assumption for the cost methodology: presence of an ESP to remove fly ashes and addition of a fabric filter to conduct the desulphurisation FF used as a reactor and a system of dedusting Investments due to the installation of the FF and reagent preparation and injection system (assumed to be about 30 % of the FF investment) Operating costs linked to the FF use. Additionnal costs for lime injection neglected In the current version: only lime considered Development in progress to introduce sodium bicarbonate Use of sodium bicarbonate

Dry sorbent adsorption with NaHCO3 UNECE Convention on Long-range Transboundary Air Pollution Dry sorbent adsorption with NaHCO3 Sodium bicarbonate consumption Stoichiometric ratio NaHCO3 consumption Efficiency Min. average Max. 70% 0.7 0.92 80% 0.8 0.835 0.87 1,05 1,10 1,14 90% 0.9 1 1.15 1.18 1.31 1.51 95% 1.2 1.3 1.58 1.71 Sodium bicarbonate costs : around 250 €/t depending on quantity bought By products: waste disposal (≈250 €/t NaHCO3 ), waste treatment for recycling possible (≈ 120 €/t NaSO4) Use of sodium bicarbonate

Agenda Current tool and methodology Implementation of new development UNECE Convention on Long-range Transboundary Air Pollution Agenda Current tool and methodology Implementation of new development VBA-Programming EPA-Method for NOx Part Load Operation Use of sodium bicarbonate as reagent for DSI FGD Next Steps

problem of unavailability of data UNECE Convention on Long-range Transboundary Air Pollution Next Steps Implementation of EPA methodology, part load operation, use of sodium bicarbonate in VBA Further testing problem of unavailability of data Updating technical document and user manual Next Steps