Interparticle forces in fluidised bed filtration of hot gases

The lack of a suitable system for hot gas cleaning is the greatest obstacle to the development of gasification combined-cycle power generation. In this work, a shallow 0.15 m diameter fluidised bed of 1 mm sand particles was used as a filter for 0.5-10 mum gasifier char particles redispersed in nitr...

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Main Author: Seville, Jonathan
Published: University of Surrey 1987
Subjects:
660
Online Access:https://ethos.bl.uk/OrderDetails.do?uin=uk.bl.ethos.377269
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spelling ndltd-bl.uk-oai-ethos.bl.uk-3772692018-09-11T03:16:56ZInterparticle forces in fluidised bed filtration of hot gasesSeville, Jonathan1987The lack of a suitable system for hot gas cleaning is the greatest obstacle to the development of gasification combined-cycle power generation. In this work, a shallow 0.15 m diameter fluidised bed of 1 mm sand particles was used as a filter for 0.5-10 mum gasifier char particles redispersed in nitrogen at 700-900°C and 1 bar a. Earlier work has suggested that, for a correctly-designed low free-area distributor, initial collection efficiencies greater than 99% at 2 could be realised but that poor retention limits the overall filtration efficiency. As an aid to retention, heavy fuel oil was sprayed continuously into the bed using a concentric-tubs atomiser. With this arrangement, theoretically-predicted filtration efficiencies were approached for particles below; 7 mum in size, but the overall performance was seriously marred by secondary aerosol originating from the addition of the oil itself. The results suggested that two modes of filter operation are possible; at lower gas and retention-aid flowrates the challenging aerosol is retained on the collector; at higher gas and retention-aid flov/rates the challenging aerosol is agglomerated and re-emitted from the bed in a distribution with a larger mean size. The operation of various instruments for particle size measurement below 10 mum has been reviewed, and their capabilities have been compared by experiment. The method selected (collection in a liquid impinger, followed by off-line analysis by "Coulter Counter") is described in detail. The addition of a liquid retention-aid to a fluidised bed can cause modification of its fluidisation behaviour, leading eventually to catastrophic defluidisation. Theoretical and experimental aspect of these effects are discussed, leading to the development of an experimental method for direct measurement of interparticle forces, and an expression for the transition condition between Geldart's (1973) groups A and B.660Fluidised bed filtration studyUniversity of Surreyhttps://ethos.bl.uk/OrderDetails.do?uin=uk.bl.ethos.377269http://epubs.surrey.ac.uk/844391/Electronic Thesis or Dissertation
collection NDLTD
sources NDLTD
topic 660
Fluidised bed filtration study
spellingShingle 660
Fluidised bed filtration study
Seville, Jonathan
Interparticle forces in fluidised bed filtration of hot gases
description The lack of a suitable system for hot gas cleaning is the greatest obstacle to the development of gasification combined-cycle power generation. In this work, a shallow 0.15 m diameter fluidised bed of 1 mm sand particles was used as a filter for 0.5-10 mum gasifier char particles redispersed in nitrogen at 700-900°C and 1 bar a. Earlier work has suggested that, for a correctly-designed low free-area distributor, initial collection efficiencies greater than 99% at 2 could be realised but that poor retention limits the overall filtration efficiency. As an aid to retention, heavy fuel oil was sprayed continuously into the bed using a concentric-tubs atomiser. With this arrangement, theoretically-predicted filtration efficiencies were approached for particles below; 7 mum in size, but the overall performance was seriously marred by secondary aerosol originating from the addition of the oil itself. The results suggested that two modes of filter operation are possible; at lower gas and retention-aid flowrates the challenging aerosol is retained on the collector; at higher gas and retention-aid flov/rates the challenging aerosol is agglomerated and re-emitted from the bed in a distribution with a larger mean size. The operation of various instruments for particle size measurement below 10 mum has been reviewed, and their capabilities have been compared by experiment. The method selected (collection in a liquid impinger, followed by off-line analysis by "Coulter Counter") is described in detail. The addition of a liquid retention-aid to a fluidised bed can cause modification of its fluidisation behaviour, leading eventually to catastrophic defluidisation. Theoretical and experimental aspect of these effects are discussed, leading to the development of an experimental method for direct measurement of interparticle forces, and an expression for the transition condition between Geldart's (1973) groups A and B.
author Seville, Jonathan
author_facet Seville, Jonathan
author_sort Seville, Jonathan
title Interparticle forces in fluidised bed filtration of hot gases
title_short Interparticle forces in fluidised bed filtration of hot gases
title_full Interparticle forces in fluidised bed filtration of hot gases
title_fullStr Interparticle forces in fluidised bed filtration of hot gases
title_full_unstemmed Interparticle forces in fluidised bed filtration of hot gases
title_sort interparticle forces in fluidised bed filtration of hot gases
publisher University of Surrey
publishDate 1987
url https://ethos.bl.uk/OrderDetails.do?uin=uk.bl.ethos.377269
work_keys_str_mv AT sevillejonathan interparticleforcesinfluidisedbedfiltrationofhotgases
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