Particle breakage in agitated dryers

In agitated dryers the motion of the impeller leads to shear deformation within the bed, which causes attrition. The attrition caused by the prevailing stresses and strains in a particle bed exposed to simple, well defined shear deformation in an annular shear cell has been extensively studied in th...

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Main Author: Hare, Colin Leo
Published: University of Leeds 2010
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Online Access:http://ethos.bl.uk/OrderDetails.do?uin=uk.bl.ethos.578680
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spelling ndltd-bl.uk-oai-ethos.bl.uk-5786802015-03-20T05:07:46ZParticle breakage in agitated dryersHare, Colin Leo2010In agitated dryers the motion of the impeller leads to shear deformation within the bed, which causes attrition. The attrition caused by the prevailing stresses and strains in a particle bed exposed to simple, well defined shear deformation in an annular shear cell has been extensively studied in the literature, however little effort has been made to better understand more complex shearing flows. A method of predicting particle breakage in agitated dryers is introduced here. The method uses models based on the Distinct Element Method (DEM), validated by torque and Positron Emission Particle Tracking (PEPT) measurements, to estimate the stress and strain rate distributions throughout the dryer bed. The attrition of Paracetamol and Aspirin under shear deformation in an annular shear cell is assessed and relationships of attrition to stress and strain developed. These relationships are combined with the stress and strain rate distributions obtained from the DEM to predict the attrition in a small-scale dryer. The attrition of Paracetamol and Aspirin in the small-scale dryer is measured experimentally and compared to the prediction. The relationship of Paracetamol attrition to stress and strain correlates well with the shear cell results; this is not the case for Aspirin. The prediction of Paracetamol attrition in the dryer therefore compares well to that measured experimentally, whereas the prediction of Aspirin attrition is less successful as the attrition resulting from the prevailing stresses and strains is not adequately described. The methodology developed here is generic and can be applied to a wide range of processes, such as dense pneumatic conveying, milling and grinding etc. III664.0284University of Leedshttp://ethos.bl.uk/OrderDetails.do?uin=uk.bl.ethos.578680Electronic Thesis or Dissertation
collection NDLTD
sources NDLTD
topic 664.0284
spellingShingle 664.0284
Hare, Colin Leo
Particle breakage in agitated dryers
description In agitated dryers the motion of the impeller leads to shear deformation within the bed, which causes attrition. The attrition caused by the prevailing stresses and strains in a particle bed exposed to simple, well defined shear deformation in an annular shear cell has been extensively studied in the literature, however little effort has been made to better understand more complex shearing flows. A method of predicting particle breakage in agitated dryers is introduced here. The method uses models based on the Distinct Element Method (DEM), validated by torque and Positron Emission Particle Tracking (PEPT) measurements, to estimate the stress and strain rate distributions throughout the dryer bed. The attrition of Paracetamol and Aspirin under shear deformation in an annular shear cell is assessed and relationships of attrition to stress and strain developed. These relationships are combined with the stress and strain rate distributions obtained from the DEM to predict the attrition in a small-scale dryer. The attrition of Paracetamol and Aspirin in the small-scale dryer is measured experimentally and compared to the prediction. The relationship of Paracetamol attrition to stress and strain correlates well with the shear cell results; this is not the case for Aspirin. The prediction of Paracetamol attrition in the dryer therefore compares well to that measured experimentally, whereas the prediction of Aspirin attrition is less successful as the attrition resulting from the prevailing stresses and strains is not adequately described. The methodology developed here is generic and can be applied to a wide range of processes, such as dense pneumatic conveying, milling and grinding etc. III
author Hare, Colin Leo
author_facet Hare, Colin Leo
author_sort Hare, Colin Leo
title Particle breakage in agitated dryers
title_short Particle breakage in agitated dryers
title_full Particle breakage in agitated dryers
title_fullStr Particle breakage in agitated dryers
title_full_unstemmed Particle breakage in agitated dryers
title_sort particle breakage in agitated dryers
publisher University of Leeds
publishDate 2010
url http://ethos.bl.uk/OrderDetails.do?uin=uk.bl.ethos.578680
work_keys_str_mv AT harecolinleo particlebreakageinagitateddryers
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