{"id":{"repo_id":"must-thes","oai_identifier":"oai:scholarsmine.mst.edu:doctoral_dissertations-3335"},"canonical_url":"https://search.dev.ndltd.org/etd/must-thes/oai:scholarsmine.mst.edu:doctoral_dissertations-3335","repository":{"repo_id":"must-thes","name":"Missouri University of Science and Technology","base_url":"https://scholarsmine.mst.edu/do/oai/"},"display":{"title":"Local liquid velocity measurement of trickle bed reactor using digitial industrial X-ray radiography","abstract":"<p>\"Trickle Bed Reactors (TBRs) are fixed beds of particles in which both liquid and gas flow concurrently downward. They are widely used to produce not only fuels but also lubrication products. The measurement and the knowledge of local liquid velocities (VLL) in TBRs is less which is essential for advancing the understanding of its hydrodynamics and for validation computational fluid dynamics (CFD). Therefore, this work focused on developing a new, non-invasive, statistically reliable technique that can be used to measure local liquid velocity (V<sub>LL</sub>) in two-dimensions (2-D). This is performed by combining Digital Industrial X-ray Radiography (DIR) and Particle Tracking Velocimetry (PTV) techniques. This work also make possible the development of three-dimensional (3-D) V<sub>LL</sub> measurements that can be taken in TBRs. Measurements taken through both the combined and the novel technique, once validated, were found to be comparable to another technique (a two-point fiber optical probe) currently being developed at Missouri University of Science and Technology. The results from this study indicate that, for a gas-liquid-solid type bed, the measured V<sub>LL</sub> can have a maximum range that is between 35 and 51 times that of its superficial liquid velocity (V<sub>SL</sub>). Without the existence of gas, the measured V<sub>LL</sub> can have a maximum range that is between 4 and 4.7 times that of its V<sub>SL</sub>. At a higher V<sub>SL</sub>, the particle tracer was greatly distributed and became carried away by a high liquid flow rate. Neither the variance nor the range of measured V<sub>LL</sub> varied for any of the replications, confirming the reproducibility of the experimental measurements used, regardless of the V<sub>SL</sub>. The liquid's movement inside the pore was consistent with findings from previous studies that used various techniques\"--Abstract, page iii.</p>","abstract_html":"&lt;p&gt;&quot;Trickle Bed Reactors (TBRs) are fixed beds of particles in which both liquid and gas flow concurrently downward. They are widely used to produce not only fuels but also lubrication products. The measurement and the knowledge of local liquid velocities (VLL) in TBRs is less which is essential for advancing the understanding of its hydrodynamics and for validation computational fluid dynamics (CFD). Therefore, this work focused on developing a new, non-invasive, statistically reliable technique that can be used to measure local liquid velocity (V&lt;sub&gt;LL&lt;/sub&gt;) in two-dimensions (2-D). This is performed by combining Digital Industrial X-ray Radiography (DIR) and Particle Tracking Velocimetry (PTV) techniques. This work also make possible the development of three-dimensional (3-D) V&lt;sub&gt;LL&lt;/sub&gt; measurements that can be taken in TBRs. Measurements taken through both the combined and the novel technique, once validated, were found to be comparable to another technique (a two-point fiber optical probe) currently being developed at Missouri University of Science and Technology. The results from this study indicate that, for a gas-liquid-solid type bed, the measured V&lt;sub&gt;LL&lt;/sub&gt; can have a maximum range that is between 35 and 51 times that of its superficial liquid velocity (V&lt;sub&gt;SL&lt;/sub&gt;). Without the existence of gas, the measured V&lt;sub&gt;LL&lt;/sub&gt; can have a maximum range that is between 4 and 4.7 times that of its V&lt;sub&gt;SL&lt;/sub&gt;. At a higher V&lt;sub&gt;SL&lt;/sub&gt;, the particle tracer was greatly distributed and became carried away by a high liquid flow rate. Neither the variance nor the range of measured V&lt;sub&gt;LL&lt;/sub&gt; varied for any of the replications, confirming the reproducibility of the experimental measurements used, regardless of the V&lt;sub&gt;SL&lt;/sub&gt;. The liquid&#x27;s movement inside the pore was consistent with findings from previous studies that used various techniques&quot;--Abstract, page iii.&lt;/p&gt;","abstract_has_math":false,"creators":["Mohd Salleh, Khairul Anuar"],"institution":"Missouri University of Science and Technology","degree_name":"Ph. D. in Nuclear Engineering","degree_level":null,"degree_discipline":null,"degree_department":null,"school":null,"contributors":[],"advisors":[],"committee_chairs":[],"committee_members":[],"year":2016,"date_issued":"2016-02-10T08:00:00Z","date_published":"2016-02-10T08:00:00Z","updated_at":"2026-07-24T03:19:21Z","subjects":["Digital Industrial Radiography (DIR)","Local Liquid Velocity (VLL)","Particle Tracking Velocimetry (PTV)","Trickle Bed Reactor (TBR)","Trickle Liquid Hydrodynamic","X-ray radiography","Nuclear Engineering"],"languages":[],"rights":[],"rights_urls":[],"identifier_entries":[]},"links":{"outbound_url":"https://scholarsmine.mst.edu/doctoral_dissertations/2333","outbound_label":"Repository record","outbound_source":"dc:identifier"},"metadata_groups":[{"id":"people","label":"People","entries":[{"key":"dc:creator","label":"Author","values":["Mohd Salleh, Khairul Anuar"]}]},{"id":"academic_context","label":"Academic Context","entries":[{"key":"dc:date.available","label":"Dc Date Available","values":["2016-02-10T08:00:00Z"]},{"key":"dc:type","label":"Dc Type","values":["Dissertation - Open Access"]},{"key":"thesis:degree_name","label":"Degree Name","values":["Ph. D. in Nuclear Engineering"]},{"key":"thesis:institution_name","label":"Thesis Institution Name","values":["Missouri University of Science and Technology"]}]},{"id":"subjects_keywords","label":"Subjects and Keywords","entries":[{"key":"dc:subject","label":"Dc Subject","values":["Digital Industrial Radiography (DIR)","Local Liquid Velocity (VLL)","Particle Tracking Velocimetry (PTV)","Trickle Bed Reactor (TBR)","Trickle Liquid Hydrodynamic","X-ray radiography","Nuclear Engineering"]}]},{"id":"identifiers","label":"Identifiers","entries":[{"key":"dc:identifier","label":"Identifier","values":["https://scholarsmine.mst.edu/doctoral_dissertations/2333"]}]},{"id":"additional","label":"Additional Metadata","entries":[{"key":"dc:description.abstract","label":"Abstract","values":["<p>\"Trickle Bed Reactors (TBRs) are fixed beds of particles in which both liquid and gas flow concurrently downward. They are widely used to produce not only fuels but also lubrication products. The measurement and the knowledge of local liquid velocities (VLL) in TBRs is less which is essential for advancing the understanding of its hydrodynamics and for validation computational fluid dynamics (CFD). Therefore, this work focused on developing a new, non-invasive, statistically reliable technique that can be used to measure local liquid velocity (V<sub>LL</sub>) in two-dimensions (2-D). This is performed by combining Digital Industrial X-ray Radiography (DIR) and Particle Tracking Velocimetry (PTV) techniques. This work also make possible the development of three-dimensional (3-D) V<sub>LL</sub> measurements that can be taken in TBRs. Measurements taken through both the combined and the novel technique, once validated, were found to be comparable to another technique (a two-point fiber optical probe) currently being developed at Missouri University of Science and Technology. The results from this study indicate that, for a gas-liquid-solid type bed, the measured V<sub>LL</sub> can have a maximum range that is between 35 and 51 times that of its superficial liquid velocity (V<sub>SL</sub>). Without the existence of gas, the measured V<sub>LL</sub> can have a maximum range that is between 4 and 4.7 times that of its V<sub>SL</sub>. At a higher V<sub>SL</sub>, the particle tracer was greatly distributed and became carried away by a high liquid flow rate. Neither the variance nor the range of measured V<sub>LL</sub> varied for any of the replications, confirming the reproducibility of the experimental measurements used, regardless of the V<sub>SL</sub>. The liquid's movement inside the pore was consistent with findings from previous studies that used various techniques\"--Abstract, page iii.</p>"]},{"key":"dc:title","label":"Title","values":["Local liquid velocity measurement of trickle bed reactor using digitial industrial X-ray radiography"]}]}],"canonical_facts":{"dc:creator":["Mohd Salleh, Khairul Anuar"],"dc:date.available":["2016-02-10T08:00:00Z"],"dc:description.abstract":["<p>\"Trickle Bed Reactors (TBRs) are fixed beds of particles in which both liquid and gas flow concurrently downward. They are widely used to produce not only fuels but also lubrication products. The measurement and the knowledge of local liquid velocities (VLL) in TBRs is less which is essential for advancing the understanding of its hydrodynamics and for validation computational fluid dynamics (CFD). Therefore, this work focused on developing a new, non-invasive, statistically reliable technique that can be used to measure local liquid velocity (V<sub>LL</sub>) in two-dimensions (2-D). This is performed by combining Digital Industrial X-ray Radiography (DIR) and Particle Tracking Velocimetry (PTV) techniques. This work also make possible the development of three-dimensional (3-D) V<sub>LL</sub> measurements that can be taken in TBRs. Measurements taken through both the combined and the novel technique, once validated, were found to be comparable to another technique (a two-point fiber optical probe) currently being developed at Missouri University of Science and Technology. The results from this study indicate that, for a gas-liquid-solid type bed, the measured V<sub>LL</sub> can have a maximum range that is between 35 and 51 times that of its superficial liquid velocity (V<sub>SL</sub>). Without the existence of gas, the measured V<sub>LL</sub> can have a maximum range that is between 4 and 4.7 times that of its V<sub>SL</sub>. At a higher V<sub>SL</sub>, the particle tracer was greatly distributed and became carried away by a high liquid flow rate. Neither the variance nor the range of measured V<sub>LL</sub> varied for any of the replications, confirming the reproducibility of the experimental measurements used, regardless of the V<sub>SL</sub>. The liquid's movement inside the pore was consistent with findings from previous studies that used various techniques\"--Abstract, page iii.</p>"],"dc:identifier":["https://scholarsmine.mst.edu/doctoral_dissertations/2333"],"dc:subject":["Digital Industrial Radiography (DIR)","Local Liquid Velocity (VLL)","Particle Tracking Velocimetry (PTV)","Trickle Bed Reactor (TBR)","Trickle Liquid Hydrodynamic","X-ray radiography","Nuclear Engineering"],"dc:title":["Local liquid velocity measurement of trickle bed reactor using digitial industrial X-ray radiography"],"dc:type":["Dissertation - Open Access"],"thesis:degree_name":["Ph. D. in Nuclear Engineering"],"thesis:institution_name":["Missouri University of Science and Technology"]},"updated_at":"2026-07-24T03:19:21Z"}