{"id":{"repo_id":"cape-town","oai_identifier":"oai:open.uct.ac.za:11427/42677"},"canonical_url":"https://search.dev.ndltd.org/etd/cape-town/oai:open.uct.ac.za:11427/42677","repository":{"repo_id":"cape-town","name":"University of Cape Town","base_url":"https://open.uct.ac.za/oai/request"},"display":{"title":"A DEM numerical modelling approach to simulating size segregation of media in a stirred mill and effects on grind characteristics","abstract":"Comminution is an important operation in the minerals processing industry. In both traditional and stirred mills, single-sized grinding beads are used, along with multiple passes through the mills, to achieve a sufficient size-reduction ratio. It is plausible to expand the size reduction capabilities of a mill using multiple-sized grinding beads in the mill. For this study, the discrete element method (DEM) was used to simulate dry size-segregated systems in a vertical stirred mill. These size-segregated systems were evaluated at different impeller speeds and weight distributions. The dry systems were susceptible to the Brazilian nut effect. Furthermore, it was found that excessive impeller speeds did not subsequently increase the overall collision modulus. The overall modal collision intensity for particle collisions was maximised between 350 rpm and 500 rpm where sufficient mixing and impeller speed were facilitated. At excessive speeds past 700 rpm the collision modulus plateaued. Excessive addition of smaller particles reduced the total energy applied to particle-particle collisions which also reduced the overall systems collision modulus. The results presented in this study could be considered as an introduction to dry size-segregated media in a vertical stirred mill.","abstract_html":"Comminution is an important operation in the minerals processing industry. In both traditional and stirred mills, single-sized grinding beads are used, along with multiple passes through the mills, to achieve a sufficient size-reduction ratio. It is plausible to expand the size reduction capabilities of a mill using multiple-sized grinding beads in the mill. For this study, the discrete element method (DEM) was used to simulate dry size-segregated systems in a vertical stirred mill. These size-segregated systems were evaluated at different impeller speeds and weight distributions. The dry systems were susceptible to the Brazilian nut effect. Furthermore, it was found that excessive impeller speeds did not subsequently increase the overall collision modulus. The overall modal collision intensity for particle collisions was maximised between 350 rpm and 500 rpm where sufficient mixing and impeller speed were facilitated. At excessive speeds past 700 rpm the collision modulus plateaued. Excessive addition of smaller particles reduced the total energy applied to particle-particle collisions which also reduced the overall systems collision modulus. The results presented in this study could be considered as an introduction to dry size-segregated media in a vertical stirred mill.","abstract_has_math":false,"creators":["Sievers, Wilco"],"institution":"Department of Chemical Engineering","degree_name":null,"degree_level":null,"degree_discipline":null,"degree_department":null,"school":null,"contributors":[],"advisors":["Mainza, Aubrey"],"committee_chairs":[],"committee_members":[],"year":2025,"date_issued":"2025","date_published":"2025","updated_at":"2026-07-24T01:34:19Z","subjects":["DEM","vertical stirred mill","size-segregated","impeller speeds","weight distribution","grind characteristics"],"languages":["en"],"rights":[],"rights_urls":[],"identifier_entries":[]},"links":{"outbound_url":"http://hdl.handle.net/11427/42677","outbound_label":"Handle","outbound_source":"dc:identifier.uri"},"metadata_groups":[{"id":"people","label":"People","entries":[{"key":"dc:contributor.advisor","label":"Advisor","values":["Mainza, Aubrey"]},{"key":"dc:creator","label":"Author","values":["Sievers, Wilco"]}]},{"id":"academic_context","label":"Academic Context","entries":[{"key":"dc:date.accessioned","label":"Dc Date Accessioned","values":["2026-01-26T07:21:53Z"]},{"key":"dc:date.available","label":"Dc Date Available","values":["2026-01-26T07:21:53Z"]},{"key":"dc:date.issued","label":"Date","values":["2025"]},{"key":"dc:publisher.department","label":"Dc Publisher Department","values":["Department of Chemical Engineering"]},{"key":"dc:publisher.institution","label":"Dc Publisher Institution","values":["University of Cape Town"]},{"key":"dc:type","label":"Dc Type","values":["Thesis / Dissertation"]},{"key":"dc:type.qualificationlevel","label":"Dc Type Qualificationlevel","values":["Masters","MSc"]}]},{"id":"subjects_keywords","label":"Subjects and Keywords","entries":[{"key":"dc:subject","label":"Dc Subject","values":["DEM","vertical stirred mill","size-segregated","impeller speeds","weight distribution","grind characteristics"]}]},{"id":"language_rights","label":"Language and Rights","entries":[{"key":"dc:language.iso","label":"Language (ISO)","values":["en"]}]},{"id":"identifiers","label":"Identifiers","entries":[{"key":"dc:identifier.uri","label":"Identifier URI","values":["http://hdl.handle.net/11427/42677"]}]},{"id":"additional","label":"Additional Metadata","entries":[{"key":"dc:description.abstract","label":"Abstract","values":["Comminution is an important operation in the minerals processing industry. In both traditional and stirred mills, single-sized grinding beads are used, along with multiple passes through the mills, to achieve a sufficient size-reduction ratio. It is plausible to expand the size reduction capabilities of a mill using multiple-sized grinding beads in the mill. For this study, the discrete element method (DEM) was used to simulate dry size-segregated systems in a vertical stirred mill. These size-segregated systems were evaluated at different impeller speeds and weight distributions. The dry systems were susceptible to the Brazilian nut effect. Furthermore, it was found that excessive impeller speeds did not subsequently increase the overall collision modulus. The overall modal collision intensity for particle collisions was maximised between 350 rpm and 500 rpm where sufficient mixing and impeller speed were facilitated. At excessive speeds past 700 rpm the collision modulus plateaued. Excessive addition of smaller particles reduced the total energy applied to particle-particle collisions which also reduced the overall systems collision modulus. The results presented in this study could be considered as an introduction to dry size-segregated media in a vertical stirred mill."]},{"key":"dc:title","label":"Title","values":["A DEM numerical modelling approach to simulating size segregation of media in a stirred mill and effects on grind characteristics"]}]}],"canonical_facts":{"dc:contributor.advisor":["Mainza, Aubrey"],"dc:creator":["Sievers, Wilco"],"dc:date.accessioned":["2026-01-26T07:21:53Z"],"dc:date.available":["2026-01-26T07:21:53Z"],"dc:date.issued":["2025"],"dc:description.abstract":["Comminution is an important operation in the minerals processing industry. In both traditional and stirred mills, single-sized grinding beads are used, along with multiple passes through the mills, to achieve a sufficient size-reduction ratio. It is plausible to expand the size reduction capabilities of a mill using multiple-sized grinding beads in the mill. For this study, the discrete element method (DEM) was used to simulate dry size-segregated systems in a vertical stirred mill. These size-segregated systems were evaluated at different impeller speeds and weight distributions. The dry systems were susceptible to the Brazilian nut effect. Furthermore, it was found that excessive impeller speeds did not subsequently increase the overall collision modulus. The overall modal collision intensity for particle collisions was maximised between 350 rpm and 500 rpm where sufficient mixing and impeller speed were facilitated. At excessive speeds past 700 rpm the collision modulus plateaued. Excessive addition of smaller particles reduced the total energy applied to particle-particle collisions which also reduced the overall systems collision modulus. The results presented in this study could be considered as an introduction to dry size-segregated media in a vertical stirred mill."],"dc:identifier.uri":["http://hdl.handle.net/11427/42677"],"dc:language.iso":["en"],"dc:publisher.department":["Department of Chemical Engineering"],"dc:publisher.institution":["University of Cape Town"],"dc:subject":["DEM","vertical stirred mill","size-segregated","impeller speeds","weight distribution","grind characteristics"],"dc:title":["A DEM numerical modelling approach to simulating size segregation of media in a stirred mill and effects on grind characteristics"],"dc:type":["Thesis / Dissertation"],"dc:type.qualificationlevel":["Masters","MSc"]},"updated_at":"2026-07-24T01:34:19Z"}