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Titania recovery from low-grade titaniferrous minerals

Thesis (PhD)--University of Pretoria, 2012.

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Other Authors: Focke, Walter Wilhelm
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Published: University of Pretoria 2013
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access_status_str Open Access
author2 Focke, Walter Wilhelm
author_browse Focke, Walter Wilhelm
author_facet Focke, Walter Wilhelm
collection Thesis
dc_rights_str_mv © 2012 University of Pretoria. All rights reserved. The copyright in this work vests in the University of Pretoria. No part of this work may be reproduced or transmitted in any form or by any means, without the prior written permission of the University of Pretoria.
description Thesis (PhD)--University of Pretoria, 2012.
format Thesis
id oai:repository.up.ac.za:2263/24305
institution University of Pretoria (South Africa)
last_indexed 2026-06-10T12:36:55.449Z
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provenance_str_mv Harvested via OAI-PMH from UPSpace — University of Pretoria Institutional Repository
publishDate 2013
publishDateRange 2013
publishDateSort 2013
publisher University of Pretoria
publisherStr University of Pretoria
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source_str UPSpace — University of Pretoria Institutional Repository
spelling oai:repository.up.ac.za:2263/24305 Titania recovery from low-grade titaniferrous minerals Focke, Walter Wilhelm araomanhique@uem.mz Manhique, A.J. (Arao Joao) Low-grade titaniferrous minerals Titanium dioxide Humidity and high-temperature oxygen sensor UCTD Thesis (PhD)--University of Pretoria, 2012. Titanium dioxide or titania is applied in paints, in the paper industry, fibbers, cosmetics, sunscreen products, toothpaste, foodstuffs, optical coatings, beam splitters and anti-reflection coatings. It is also used as support catalyst and its use as humidity and high-temperature oxygen sensor is under consideration. These applications are related to its high refractive index, oil absorption, tinting strength and inert chemical properties. Commonly, titania is recovered either by leaching ilmenite with sulphuric acid and subsequently hydrolysing the resulting sulfate solution by boiling. In another process, titanium feedstock is converted into titanium tetrachloride and further oxidised to titanium dioxide. These methods are reportedly time-consuming and environmentally unfriendly. They are also unable to use all existing types of titanium minerals. In this study, a novel process for the extraction of titanium valuables from its minerals is presented. The process entails the roasting of titanium ore with alkaline metal salt. The roasted product is hydrolysed with water and acid, and subsequently reacted with sulphuric acid. Alternatively, the hydrolysed product can be used as feedstock in the chloride process. Roasting at 900°C and using a 2:1 (NaOH:ilmenite) mole ratio proved to be the most efficient in releasing titanium units from its ore. Ternary phases dominate under these conditions. Na0.75Fe0.75Ti0.25O2 was the dominant titanium-bearing phase. NaFeTiO4a ndNa2Fe2Ti3O10 were also present. Whenever the Ti:Fe atom ratio was different from one, the surplus titanium was accommodated in single titanates, mainly Na2TiO3, while iron was accommodated in NaFeO2. In many cases Na8Ti5O14 was also present as a result of Na2TiO3 polymerisation. This is consistent with a fusion period of one hour or more. Shorter fusion periods tended to produce binary phases. Similar results were obtained when lower fusion temperatures were employed, i.e. below 550°C. When anatase reactant was used to resemble an anatase ore, Na2Ti6O3,Na2TiO3, Na8Ti5O14 and Na16Ti10O28 were identified in the products. Optimum recoveries were obtained using a 1:1 NaOH:TiO2 mole ratio, and fusing at 800°C for 2 h. Close to 100% of the titanium was recovered. A one-step leaching process was found to be effective compared with multi-step leaching. The leaching step was found to be dependent on time, solid:liquid ratio and temperature. The optimum conditions for solid:liquid ratio, time and temperature were found to be 0.20, and 15 min at 75°C, respectively. Acidic hydrolysis was controlled by the relative amount of iron and titanium in solution. It was found that less than 1% was dissolved between 3 and 7 in pH units. Higher pH values are recommended, since less acid will be used. Any excess of sulphuric acid in the sulfation step proved to be unnecessary. No significant changes were observed in the amount of dissolved iron and titanium. Therefore the stoichiometric amount can be used in the sulfation process. Chemistry unrestricted 2013-09-06T17:07:26Z 2013-05-20 2013-09-06T17:07:26Z 2013-04-17 2012 2013-05-03 Thesis Manhique, AJ 2012, Titania recovery from low-grade titaniferrous minerals, PhD thesis, University of Pretoria, Pretoria, viewed yymmdd < http://hdl.handle.net/2263/24305 > D13/4/523/ag http://hdl.handle.net/2263/24305 http://upetd.up.ac.za/thesis/available/etd-05032013-143155/ © 2012 University of Pretoria. All rights reserved. The copyright in this work vests in the University of Pretoria. No part of this work may be reproduced or transmitted in any form or by any means, without the prior written permission of the University of Pretoria. application/pdf application/pdf application/pdf application/pdf application/pdf application/pdf University of Pretoria
spellingShingle Low-grade titaniferrous minerals
Titanium dioxide
Humidity and high-temperature oxygen sensor
UCTD
Titania recovery from low-grade titaniferrous minerals
title Titania recovery from low-grade titaniferrous minerals
title_full Titania recovery from low-grade titaniferrous minerals
title_fullStr Titania recovery from low-grade titaniferrous minerals
title_full_unstemmed Titania recovery from low-grade titaniferrous minerals
title_short Titania recovery from low-grade titaniferrous minerals
title_sort titania recovery from low grade titaniferrous minerals
topic Low-grade titaniferrous minerals
Titanium dioxide
Humidity and high-temperature oxygen sensor
UCTD
url http://hdl.handle.net/2263/24305
http://upetd.up.ac.za/thesis/available/etd-05032013-143155/