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Archive | 2002

THE ROLE OF ALKALI SULFATES AND CHLORIDES IN POST CYCLONE DEPOSITS FROM CIRCULATING FLUIDIZED BED BOILERS FIRING BIOMASS AND COAL

Bengt-Johan Skrifvars; Tor Laurén; Rainer Backman; Mikko Hupa

High amounts chlorine and sulphur in a fuel is generally connected with ash related operational problems in the boiler in which the fuel is fired. The problems occur as fireside deposits in different locations of the fluegas channel or as corrosion problems. Sulphur and chlorine together with alkali and earth alkali metals are known to strongly affect the thermal behaviour of the ash. First melting temperatures as low as 515 °C may be found if unsuitable amounts of alkali, sulphur and chlorine is present in the ash. A vast experience on the matter exists from coal firing [Sarofim and Helble 1994; Bryers 1992; Harb and Smith, 1990] as well as from firing different types of waste sludges [Backman et al., 1987] Backman et al., 1996; Salmenoja et al., 1996]. Forrest derived fuels such as wood, bark or forest residue (branches and tops) contain usually low amounts of sulphur and chlorine. The low potential for sulphur dioxide emissions from combustion of these kind of fuels as well as the indication of a fairly well behaving ash in most kind of combustion systems, are generally considered as two important advantages for the fuels. Sometimes these general indications are applied also on any type of biomass. This may, however, lead to serious errors since other biomasses such as straw or annually grown energy crops may contain significant amounts of both chlorine and sulphur [Nordin 1993]. In Fig. 1 the amount of chlorine and sulphur is shown for a number of different fuels, including coal, peat, wheat straw and forest derived fuel. Fluidized bed combustion is regarded as a very flexible combustion system with a capacity to burn a wide range of fuels. From the ash behaviour point of view the low combustion temperature of some 800–900 °C is favourable compared to conventional pulverised systems since operational problems due to a low melting ash are assumed to be avoided. The FBC technique has, however, limits. Common knowledge from conventional


18th International Conference on Fluidized Bed Combustion | 2005

The Åbo Akademi Database: Ash Behavior Measurements in Full-Scale Boilers

Bengt-Johan Skrifvars; Patrik Yrjas; Tor Laurén; Mikko Hupa; Martin Dittrich

This poster paper presents an overview of the Abo Akademi full-scale boiler ash behavior measurement database. The database contains data from some 20 full-scale boiler measurement campaigns during which the ash behavior in the boiler has been monitored identically. The measurements have been done in 3 different bubbling fluidized bed boilers and 2 circulating fluidized bed boilers during 11 different campaigns. For comparison data from 2 pulverized fuel fired boilers as well as from 2 grate fired boilers have also been included. The data collection includes conventional analyses of the fuels or fuel mixes used during the measurements, ash deposition measurements performed with the air-cooled probe technique, chemical analyses of the collected deposits (front and back side separately, chemical analyses of the boiler fly ashes, and recordings of chosen relevant boiler operation parameters such as boiler load, air-distribution, and flue gas temperatures. The poster paper presents ash deposition data, so called Rate-of-build-up values (RBU, g/m2 h) as a function of fuel mixes, probe surface temperatures and boiler type. The poster also presents compositional data of the collected deposits such as the chlorine content as a function of fuel mix and probe surface temperature.Copyright


Fuel | 2004

Ash behaviour in a pulverized wood fired boiler-a case study

Bengt-Johan Skrifvars; Tor Laurén; Mikko Hupa; R. Korbee; P. Ljung


Fuel Processing Technology | 2013

The fate of chlorine, sulfur, and potassium during co-combustion of bark, sludge, and solid recovered fuel in an industrial scale BFB boiler

Emil Vainio; Patrik Yrjas; Maria Zevenhoven; Anders Brink; Tor Laurén; Mikko Hupa; Tuula Kajolinna; Hannu Vesala


Energy & Fuels | 2005

The fouling behavior of rice husk ash in fluidized-bed combustion. 2. Pilot-scale and full-scale measurements

Bengt-Johan Skrifvars; Patrik Yrjas; Tor Laurén; Jouni Kinni; Honghi Tran; Mikko Hupa


Fuel Processing Technology | 2016

Effect of temperature gradient on composition and morphology of synthetic chlorine-containing biomass boiler deposits

Daniel Lindberg; Jonne Niemi; Markus Engblom; Patrik Yrjas; Tor Laurén; Mikko Hupa


Energy & Fuels | 2011

Role of ZnCl2 in High-Temperature Corrosion in a Bench-Scale Fluidized Bed Firing Simulated Waste Wood Pellets

Dorota Bankiewicz; E. Alonso-Herranz; Patrik Yrjas; Tor Laurén; H. Spliethoff; Mikko Hupa


Fuel | 2016

Low-temperature corrosion in co-combustion of biomass and solid recovered fuels

Emil Vainio; Hanna Kinnunen; Tor Laurén; Anders Brink; Patrik Yrjas; Nikolai DeMartini; Mikko Hupa


Fuel Processing Technology | 2007

Development and evaluation of a long-term deposit probe for on-line monitoring of deposit growth

Anders Brink; Tor Laurén; Patrik Yrjas; Mikko Hupa; Joachim Friesenbichler


Fuel | 2014

Fate of bromine and chlorine in bubbling fluidized bed combustion – Formation of alkali halide aerosols

Hao Wu; Tor Laurén; Patrik Yrjas; Pasi Vainikka; Mikko Hupa

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Mikko Hupa

Åbo Akademi University

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Patrik Yrjas

Åbo Akademi University

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Anders Brink

Åbo Akademi University

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Emil Vainio

Åbo Akademi University

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Hao Wu

Åbo Akademi University

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Jonne Niemi

Åbo Akademi University

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