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to read the full report - Ecolateral by Peter Jones

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Evaluation of Opportunities for Converting Indigenous UK Wastes <strong>to</strong> Wastes and Energy<br />

AEA/ED45551/Issue 1<br />

disposed of in a controlled landfill site. Recent European practice involves melting fly ash <strong>to</strong> form a glass<br />

that reduces <strong>the</strong> mobility of <strong>the</strong> metal ions and destroys dioxin. Following this treatment <strong>the</strong> ash can be<br />

used as aggregate or filler.<br />

Impact of waste composition on boiler performance<br />

There are two main impacts that must be managed <strong>by</strong> <strong>the</strong> designers and opera<strong>to</strong>rs of waste combustion<br />

plant; acid gas and ash fouling.<br />

Chlorine is always present in mixed waste streams and derives largely from plastics but also from paper<br />

and card. The chorine is converted in<strong>to</strong> hydrochloric acid in <strong>the</strong> combustion chamber, and this can cause<br />

excessive corrosion in <strong>the</strong> boiler, particularly at high temperatures. Restricting <strong>the</strong> temperature and<br />

pressure of <strong>the</strong> steam produced <strong>by</strong> <strong>the</strong> incinera<strong>to</strong>r limits <strong>the</strong> corrosion risk but also restricts <strong>the</strong> electrical<br />

efficiency that can be achieved.<br />

Circulating fluidised bed combus<strong>to</strong>rs have an advantage in treating wastes with a high chlorine content in<br />

that <strong>the</strong> high temperature boiler surface can be located in <strong>the</strong> circulating bed material where <strong>the</strong> chlorine<br />

concentration is lower.<br />

The oxides and salts of silicon and alkali metals are present in biomass derived wastes <strong>to</strong> a much larger<br />

extent than fossil fuels. The content increases with <strong>the</strong> proportion of annual growth material in <strong>the</strong> fuel.<br />

Thus, straw and o<strong>the</strong>r annual crop residues contain large quantities as does <strong>the</strong> bark and outer layers of<br />

trees. These components have low melting points that can lie below <strong>the</strong> temperature of <strong>the</strong> furnace, <strong>the</strong>y<br />

also have a propensity <strong>to</strong> form low melting point eutectic mixtures with o<strong>the</strong>r ash components. The liquid<br />

ash can adhere <strong>to</strong> heat transfer surfaces causing a reduction in output, sites for corrosion, and<br />

occasionally physical damage. Fluidised beds are also susceptible <strong>to</strong> agglomeration and eventual<br />

sintering and fusing due <strong>to</strong> <strong>the</strong> sticky nature of soft and liquid ash.<br />

Problems caused <strong>by</strong> ash chemistry are some of <strong>the</strong> most intractable in <strong>the</strong> industry and require <strong>the</strong><br />

application of substantial knowledge and experience in sourcing and blending feeds<strong>to</strong>cks and instituting<br />

regular boiler cleaning procedures. Suppliers of fluidised bed boilers have learned <strong>to</strong> manage <strong>the</strong><br />

chemistry of <strong>the</strong>ir bed materials <strong>to</strong> avoid low melting point eutectics <strong>by</strong> <strong>the</strong> addition of materials such as<br />

dolomite.<br />

A comprehensive review and a discussion of best practice for waste combustion is given in <strong>the</strong> supporting<br />

documentation for <strong>the</strong> Waste Incineration Directive 196<br />

Co-firing biofuels with fossil fuels<br />

The concept of co-firing biofuels with coal is one means of increasing <strong>the</strong> combustion of biomass in an<br />

existing power plant without incurring excessive capital costs. This approach has received increased<br />

attention recently, particularly in Denmark, <strong>the</strong> Ne<strong>the</strong>rlands and <strong>the</strong> US. The details of over 300 co-firing<br />

installations can be found on <strong>the</strong> IEA Bioenergy Agreement Task 32 database of co-firing installations. 197<br />

The way in which biomass is fired depends on <strong>the</strong> quantities involved. Where biomass quantities are<br />

small (2- 5%), <strong>the</strong> biomass is mixed with <strong>the</strong> coal at <strong>the</strong> mill inlet. Where biomass constitutes 5-25% of <strong>the</strong><br />

<strong>to</strong>tal fuel, shredded biomass is fired through dedicated burners. Beyond <strong>the</strong> 25% level, new concepts will<br />

be needed because combustion of that amount of biomass will have a substantial impact on both furnace<br />

and ash behaviour. Current opinion within <strong>the</strong> industry is that this will probably mean converting <strong>the</strong> fuel<br />

<strong>to</strong> gas.<br />

Current practice in <strong>the</strong> UK is <strong>to</strong> receive <strong>the</strong> fuel on site in <strong>the</strong> form of pellets that are stable, easy <strong>to</strong><br />

handle and break easily in <strong>the</strong> coal mills.<br />

196 European Integrated Pollution and Prevention and Control Bureau Waste Incineration Bref (08.06) http://eippcb.jrc.es/pages/FActivities.htm<br />

197 http://www.ieabcc.nl/database/cofiring.php<br />

111

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