The thermal behaviour of alunite/K2CO3, alunite/CaCO3 and alunite/Ca(OH)(2) mixtures has been established. DTA coupled with XRD analysis has allowed appraisal of the main reactions that occur when the mixtures are roasted up to about 1000 degrees C. The main products of roasting are K2SO4, CaSO4 and other sulphur compounds and aluminates which retain the SO3 deriving from the alunite. The products are formed between 700 and 800 degrees C, The aim of the work was to assess the feasibility of a thermal process for use in the case of certain kaolin deposits whose exploitation is impossible at the present time because they are contaminated with alunite (KAl3(SO4)(2)(OH)(6)) This mineral causes great difficulty when attempting to use these kaolin ores because kilning drives off SO3 which corrodes the furnaces and is environmentally harmful. The K2SO4 and CaSO4 produced by roasting the indicated mixtures can be leached with water and dilute HCl respectively and the former can be used as fertiliser. The leaching residue, with its reduced sulphur content, can then be employed by the ceramics and building industries. (C) 1997 Elsevier Science B.V.
Thermal behaviour of mixtures of an alunite ore with K2CO3, CaCO3 and Ca(OH)2 / P., Cipriani; G., Marruzzo; Piga, Luigi; F., Pochetti. - In: THERMOCHIMICA ACTA. - ISSN 0040-6031. - 294:2(1997), pp. 139-146. [10.1016/s0040-6031(97)00073-7]
Thermal behaviour of mixtures of an alunite ore with K2CO3, CaCO3 and Ca(OH)2
PIGA, LUIGI;
1997
Abstract
The thermal behaviour of alunite/K2CO3, alunite/CaCO3 and alunite/Ca(OH)(2) mixtures has been established. DTA coupled with XRD analysis has allowed appraisal of the main reactions that occur when the mixtures are roasted up to about 1000 degrees C. The main products of roasting are K2SO4, CaSO4 and other sulphur compounds and aluminates which retain the SO3 deriving from the alunite. The products are formed between 700 and 800 degrees C, The aim of the work was to assess the feasibility of a thermal process for use in the case of certain kaolin deposits whose exploitation is impossible at the present time because they are contaminated with alunite (KAl3(SO4)(2)(OH)(6)) This mineral causes great difficulty when attempting to use these kaolin ores because kilning drives off SO3 which corrodes the furnaces and is environmentally harmful. The K2SO4 and CaSO4 produced by roasting the indicated mixtures can be leached with water and dilute HCl respectively and the former can be used as fertiliser. The leaching residue, with its reduced sulphur content, can then be employed by the ceramics and building industries. (C) 1997 Elsevier Science B.V.I documenti in IRIS sono protetti da copyright e tutti i diritti sono riservati, salvo diversa indicazione.
