Kinetics of the dissolution of sand into alkaline solutions: application of a modified shrinking core model
The batch dissolution kinetics of sand particles in concentrated alkaline sodium hydroxide solutions was investigated at high temperature and high pressure. The influence of the particle size, the operating temperature (150–220 °C) and the hydroxide ion molality on the kinetic rate were studied. Exp...
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Veröffentlicht in: | Hydrometallurgy 2004, Vol.71 (3), p.435-446 |
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creator | Mgaidi, A Jendoubi, F Oulahna, D El Maaoui, M Dodds, J.A |
description | The batch dissolution kinetics of sand particles in concentrated alkaline sodium hydroxide solutions was investigated at high temperature and high pressure. The influence of the particle size, the operating temperature (150–220 °C) and the hydroxide ion molality on the kinetic rate were studied. Experimental data fit well into a developed model based on the shrinking core model approach in which a variable activation energy term was introduced. Kinetic analysis of the experimental results reveals that the associated energy and the rate-controlling mechanism are dependent upon both sample temperature as well as the extent of the reaction. |
doi_str_mv | 10.1016/S0304-386X(03)00117-8 |
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The influence of the particle size, the operating temperature (150–220 °C) and the hydroxide ion molality on the kinetic rate were studied. Experimental data fit well into a developed model based on the shrinking core model approach in which a variable activation energy term was introduced. Kinetic analysis of the experimental results reveals that the associated energy and the rate-controlling mechanism are dependent upon both sample temperature as well as the extent of the reaction.</description><identifier>ISSN: 0304-386X</identifier><identifier>EISSN: 1879-1158</identifier><identifier>DOI: 10.1016/S0304-386X(03)00117-8</identifier><identifier>CODEN: HYDRDA</identifier><language>eng</language><publisher>Amsterdam: Elsevier B.V</publisher><subject>Activation energy ; Applied sciences ; Engineering Sciences ; Exact sciences and technology ; Hydrometallurgy ; Kinetics ; Mechanism ; Metals. Metallurgy ; Production of metals ; Production of non ferrous metals. 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The influence of the particle size, the operating temperature (150–220 °C) and the hydroxide ion molality on the kinetic rate were studied. Experimental data fit well into a developed model based on the shrinking core model approach in which a variable activation energy term was introduced. Kinetic analysis of the experimental results reveals that the associated energy and the rate-controlling mechanism are dependent upon both sample temperature as well as the extent of the reaction.</description><subject>Activation energy</subject><subject>Applied sciences</subject><subject>Engineering Sciences</subject><subject>Exact sciences and technology</subject><subject>Hydrometallurgy</subject><subject>Kinetics</subject><subject>Mechanism</subject><subject>Metals. Metallurgy</subject><subject>Production of metals</subject><subject>Production of non ferrous metals. 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Metallurgy</topic><topic>Production of metals</topic><topic>Production of non ferrous metals. Process materials</topic><topic>Sand dissolution</topic><topic>Shrinking core model</topic><toplevel>peer_reviewed</toplevel><toplevel>online_resources</toplevel><creatorcontrib>Mgaidi, A</creatorcontrib><creatorcontrib>Jendoubi, F</creatorcontrib><creatorcontrib>Oulahna, D</creatorcontrib><creatorcontrib>El Maaoui, M</creatorcontrib><creatorcontrib>Dodds, J.A</creatorcontrib><collection>Pascal-Francis</collection><collection>CrossRef</collection><collection>Hyper Article en Ligne (HAL)</collection><collection>Hyper Article en Ligne (HAL) (Open Access)</collection><jtitle>Hydrometallurgy</jtitle></facets><delivery><delcategory>Remote Search Resource</delcategory><fulltext>fulltext</fulltext></delivery><addata><au>Mgaidi, A</au><au>Jendoubi, F</au><au>Oulahna, D</au><au>El Maaoui, M</au><au>Dodds, J.A</au><format>journal</format><genre>article</genre><ristype>JOUR</ristype><atitle>Kinetics of the dissolution of sand into alkaline solutions: application of a modified shrinking core model</atitle><jtitle>Hydrometallurgy</jtitle><date>2004</date><risdate>2004</risdate><volume>71</volume><issue>3</issue><spage>435</spage><epage>446</epage><pages>435-446</pages><issn>0304-386X</issn><eissn>1879-1158</eissn><coden>HYDRDA</coden><abstract>The batch dissolution kinetics of sand particles in concentrated alkaline sodium hydroxide solutions was investigated at high temperature and high pressure. The influence of the particle size, the operating temperature (150–220 °C) and the hydroxide ion molality on the kinetic rate were studied. Experimental data fit well into a developed model based on the shrinking core model approach in which a variable activation energy term was introduced. Kinetic analysis of the experimental results reveals that the associated energy and the rate-controlling mechanism are dependent upon both sample temperature as well as the extent of the reaction.</abstract><cop>Amsterdam</cop><pub>Elsevier B.V</pub><doi>10.1016/S0304-386X(03)00117-8</doi><tpages>12</tpages><orcidid>https://orcid.org/0000-0003-3470-1086</orcidid><oa>free_for_read</oa></addata></record> |
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subjects | Activation energy Applied sciences Engineering Sciences Exact sciences and technology Hydrometallurgy Kinetics Mechanism Metals. Metallurgy Production of metals Production of non ferrous metals. Process materials Sand dissolution Shrinking core model |
title | Kinetics of the dissolution of sand into alkaline solutions: application of a modified shrinking core model |
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