Conversion of Stoker fired Boiler Plants into CoFiring FBC Boiler systems

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Conversion of Stoker fired Boiler Plants into CoFiring FBC Boiler systems presented at the Final NetbioCof Conference July 2007 at Budapest, Hungary Dipl.-Ing. Wolfgang Bengel BMP Biomasse Projekt GmbH www.bmp-biomasse.de

Co-Firing of Biomass and Fossil Fuel in FBC Utilization of Biomass as Fuel, replacing part of Fossil Fuel is getting increasingly important to improve the CO2-balance and lower energy cost, especially for industry and district heating systems. Adjustment of the FBC Technology to the particular combustion characteristics of various types of Biomass can make FBC Systems an efficient tool to contribute to the solution of the waste (MSW) problem, and provide access to improving agro-energy industry. The major advantage of the FBC Technology is the complete combustion of such material at optimum conditions (at comparatively low temperatures and low emission levels). This has been verified by numerous boiler plants. Eastern Europe has a high potential of traditional grate fired industrial boilers, not in use right now, due to low priced natural gas supply until year 2005

Differences between Stoker and FBC Boilers Items making the Difference between Stoker and FBC Boilers Stoker System FBC Fuel Spectrum - + + Water Content - + Fuel Fines - + + Coarse Fuel + - Combustion Temperature 1100 C 850 C Ash Softening Point - + + Emissions - + Excess Air Ratio 2.0 1.3 Exhaust Gas Volume - + + NOx Formation - + + SO 2 & HCl Retention - - + Boiler Efficiency - + Parasitic Load + + - Plant Efficiency - + Investment Cost - +

Typical Traveling Grate Stoker

Declined Traveling Grate to be replaced by FBC Remove complete grate system

HP Steam Boiler with Biomass fired FBC (Currently under Construction near Karlsruhe, Germany) Lift boiler structure Replace grate part by fluidized Bed system Add open floor bubbling bed Ash circulation system Add circulation pump

Conversion of an 8,5 t/h RDF fired Stoker into an CoFiring FBC Boiler Boiler Specs after before Steam Generation [t/h] 11.0 8.5 Fuel Rating [MW] 9.97 7,84 Live Steam Pressure [bar] 41 41 Live Steam Temperature [ C] 410 410 Licensed Pressure [bar] 48 48 Feed Water Temperature [ C] 105 105 Exhaust Gas Temperature [ C] 200 200 Boiler Efficiency [%] 84.0 82.5 Fuel Feeding Rate (3500 Kcal/Kg) [Kg/h] 2,451 2,000 Combustion Air Flow [Nm³/h] 13,850 21308 Flue Gas Flow [Nm³/h] 15,740 24215 Main Dimensions (Incinerator) FBC Cross Section [m x m] 2.50 x 4.00 Boiler Foot Print [m x m] 2.70 x 4.20

Main Advantages of Converting Stokers into FBC Stokers with traveling grates need excess air at levels of about n = 2.0 whereas AFBC can operate at levels of n = 1.3 This raises boiler efficiency due to lower flue gas loss because of reduced flue gas flow rates With in-bed heating surfaces power is raised by nearly 30 % from 8,5 t/h to 11t/h steam capacity Without in-bed heating surfaces 20-25% less power because of lower flue temperature and less evaporator surface Certain emissions are lowered without secondary means and measures

Means & Measures for Boiler Conversion from Stokers to FBC Cut off part of first boiler draft and remove traveling grate Reinforce support structure (as necessary) Lift boiler bodies (if necessary) Replace traveling grate by FBC incinerator Add up in-bed heating surfaces for forced or convective circulation

Equipment to be added / changed at conversion Fuel feeding system (screws or spreaders) Incinerator (water walls) Ceramic liner (for 2 sec at 850 C) Insulation, Start up burner, gas or oil FD-fans (primary and secondary) Circulation pumps for in-bed surfaces (depending on capacity) I&C

Cost of Converting the 8 MW RDF fired Stoker fired Boiler is cheaper and faster than buildig a new system Cost of the entire Conversion is approx. 1,3 1,5 Mill. Boiler Capacity is raised by approx. 30% No NEW Permits and approvals required, All auxilliaries can be retained Basic advantage: fast solution to meet future requirements of EU environmental Standards and regain part fuel independence Along with rising cost for fossile fuel imports, any local fuel i.e. RDF, MSW, Agro- Waste will soon be in line with EU and national fuel standards and subject to fuel blending. National waste policy will turn into recycling polycy and consider any combustible as valuable fuel, reuse of any carbon-product can save CO2 and minimize methanisation of dumpsites and agro-waste.

Thank you very much for your kind attention. BMP Biomasse Projekt GmbH and their engineers are at any time in the position to consult to and reply to your Biomass/Coal combustion Problem. The decision to refurbish an existing boiler plant for Biomass/Coal firing or to built a new boiler system can only be decided on a detailed survey of the actual situation and clear prognosis of the future demand. Commercial benefits and longtime successful operation are neatly linked to a sustainable and environmentally sound investment Dipl.-Ing Wolfgang Bengel BMP Biomasse Projekt GmbH Tel 0049 151 550 16934 www.bmp-biomasse.de Peter Grziwa and MartinSchneiders Bisanz Anlagenbau GmbH