Full-text resources of PSJD and other databases are now available in the new Library of Science.
Visit https://bibliotekanauki.pl

PL EN


Preferences help
enabled [disable] Abstract
Number of results
2011 | 32 | 4 | 391-399

Article title

The influence of sampling point on solids suspension density applied in scaling of the hydrodynamics of a supercritical CFB boiler

Content

Title variants

Languages of publication

EN

Abstracts

EN
The article presents the results of laboratory tests carried out on a scaling model of the 966MWth fluidised-bed boiler operating in the Lagisza Power Plant, made on a scale of 1:20 while preserving the geometrical similarity. The tests were carried out for scaled-down material taken from different locations on the circulation contour in the state of full boiler loading. To reflect the hydrodynamic conditions prevailing in the combustion chamber, solids with properly selected density and particle size distribution were used. The obtained results have made it possible to determine the location for taking the most representative granular material sample.

Publisher

Year

Volume

32

Issue

4

Pages

391-399

Physical description

Dates

published
1 - 12 - 2011
online
15 - 2 - 2012

Contributors

author
  • Faculty of Environmental Protection and Engineering, Institute of Advanced Energy Technologies, Częstochowa University of Technology, ul. Dąbrowskiego 69, 42-200 Częstochowa, Poland
author
  • Faculty of Environmental Protection and Engineering, Institute of Advanced Energy Technologies, Częstochowa University of Technology, ul. Dąbrowskiego 69, 42-200 Częstochowa, Poland

References

  • Glicksman L. R., Hyre M., Woloshun K., 1993. Simplified scaling relationships for fluidized beds. Powder Technol., 77, 177-199. DOI: 10.1016/0032-5910(93)80055-F.[Crossref]
  • Horio M., Grace J.R., Avidan A.A., Knowlton T.M. (Eds.), 1997. Circulating Fluidized Beds, Blackie Academic and Professional, London.
  • Ishii H., Nakajima T., Horio M., 1989. The clustering annular flow model of circulating fluidized bed. J. Chem. Eng. Japan, 22, 484-490.
  • Knowlton T.M., Karri S.B.R., Issangya A., 2005. Scale-up of fluidized-bed hydrodynamics. Powder Technol., 150, 272-277. DOI: 10.1016/j.powtec.2004.11.036.[Crossref]
  • Mirek P., 2011. A simplified methodology for scaling hydrodynamic data from Lagisza 460MWe supercritical CFB boiler. Chem. Process Eng., 32, 245-253. DOI: 10.2478/v10176-011-0019-1[Crossref][WoS]
  • Nian-Sheng Cheng, 2009. Comparison of formulas for drag coefficient and settling velocity of spherical particles. Powder Technol., 189, 395-398. DOI: 10.1016/j.powtec.2008.07.006.[Crossref]
  • Van der Meer E.H., Thorpe R.B., Davidson J.F., 1999. Dimensionless groups for practicable similarity of circulating fluidised beds. Chem. Eng. Sci., 54, 5369-5376. DOI: 10.1016/S0009-2509(99)00270-5.[Crossref]

Document Type

Publication order reference

Identifiers

YADDA identifier

bwmeta1.element.-psjd-doi-10_2478_v10176-011-0031-5
JavaScript is turned off in your web browser. Turn it on to take full advantage of this site, then refresh the page.