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        <datestamp>2026-09-24T09:05:06Z</datestamp>
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          <dc:title>Supported data of the article: From Fluidisation to Swirling: Flow Regime Identification in a Toroidal Fluidised Bed Using Imaging and Pressure Drop</dc:title>
          <dc:creator>Abdulbasit Hasan Mahdi Mahdi (22705793)</dc:creator>
          <dc:creator>Vladimir Zivkovic (22734632)</dc:creator>
          <dc:creator>Jonathan McDonough (22719089)</dc:creator>
          <dc:creator>Greg Mutch (7237307)</dc:creator>
          <dc:subject>Chemical engineering design</dc:subject>
          <dc:subject>Swirling fluidised bed</dc:subject>
          <dc:subject>TORBED</dc:subject>
          <dc:subject>Process intensification</dc:subject>
          <dc:subject>Particle entrainment</dc:subject>
          <dc:subject>Minimum fluidisation velocity</dc:subject>
          <dc:description>&lt;p dir="ltr"&gt;The research focuses on the hydrodynamic behaviour of the TORBED fluidised bed using fine silica particles with an average size of 90 µm. The pressure drop was measured using a pressure drop transducer, and the data were analysed based on pressure drop and the standard deviation to identify the bed regimes. The experimental conditions covered flow rates from 2 to 30 L/min and bed loadings from 1 to 4 g. The silica particles were divided into three samples: raw silica, silica sieved through a 38 µm mesh, and silica sieved through a 75 µm mesh.&lt;/p&gt;</dc:description>
          <dc:date>2026-09-24T09:05:06Z</dc:date>
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