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3-Dimensional Particle Tracking in a Fluid Dynamically Downscaled Fluidized Bed Using Magnetoresistive Sensors

Sette, Erik, 1984 (author)
Chalmers tekniska högskola,Chalmers University of Technology
Köhler, Anna, 1989 (author)
Chalmers tekniska högskola,Chalmers University of Technology
Pallarès, David, 1975 (author)
Chalmers tekniska högskola,Chalmers University of Technology
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Johnsson, Filip, 1960 (author)
Chalmers tekniska högskola,Chalmers University of Technology
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 (creator_code:org_t)
ISBN 9789811020223
2016-07-31
2016
English.
In: Clean Coal Technology and Sustainable Development. Proceedings of the 8th International Symposium on Coal Combustion (ISCC). Tsinghua Univ, Beijing, Peoples rep of China, 19-22 July, 2015. - Singapore : Springer Singapore. - 9789811020223 ; 0, s. 317-322
  • Conference paper (peer-reviewed)
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  • This paper presents a measurement technique for continuous tracking of particles in 3-dimensional bubbling fluidized beds operated according to scaling laws. By applying Glicksman's full set of scaling laws to both bulk solids and tracer particle, the bed is assumed to be fluid dynamically similar to a combustor operated at 900 C-circle with the tracer particle corresponding to a fuel particle with properties similar to anthracite coal. Two different gas distributors with varying pressure drop are used to investigate the influence of bed design on fuel mixing. Flow structures formed around rising gas bubbles, the so-called bubble paths, are identified, and the tracer particle traverses the entire bed for a gas distributor yielding a high pressure drop. For a gas distributor yielding a low pressure drop, flow structures are less pronounced, and the tracer particle is not circulating the entire bed.

Subject headings

TEKNIK OCH TEKNOLOGIER  -- Maskinteknik -- Energiteknik (hsv//swe)
ENGINEERING AND TECHNOLOGY  -- Mechanical Engineering -- Energy Engineering (hsv//eng)

Keyword

Bubbling fluidized bed
Fluid dynamically downscaling
combustion
3-dimensional tracking

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