Please use this identifier to cite or link to this item: https://hdl.handle.net/11499/4889
Title: Sulfate removal from alunitic kaolin by chemical method
Authors: Özdemir, M.
Çetişli, Halil
Keywords: Calcination
Chemical reactors
High temperature effects
Potassium compounds
Solutions
Solvent extraction
Stoichiometry
Sulfur compounds
Alunitic kaolin
Batch reactors
Distilled water
Sulfate removal
Kaolin
chemical engineering
removal
sulfate
Abstract: The removal of sulfate from alunitic kaolin by a chemical method, in which alunitic kaolin + potassium compound (KCl and KOH) was calcined at different temperatures and sulfate was extracted by distilled water, was studied in a batch reactor. The effects of calcination temperature, sample type, potassium compound amount, and sample preparation method on the sulfate removal were investigated. Sulfate removal yield varied with the selected parameters relative to the completion of the solid-phase reaction in which the sulfate in the alunitic kaolin was converted to soluble potassium sulfate. Maximum sulfate removal yield was obtained under the following working conditions: calcination temperature, 700°C; sample type, alunitic kaolin + KCl; potassium compound amount, 17.8% (15% more than the stoichiometric ratio); and solution phase method used for sample preparation. Maximum sulfate removal yield was 97%. By this way, the sulfate content of alunitic kaolin was decreased from 12.97% to below 1%. © 2005 American Chemical Society.
URI: https://hdl.handle.net/11499/4889
https://doi.org/10.1021/ie040177s
ISSN: 0888-5885
Appears in Collections:Fen-Edebiyat Fakültesi Koleksiyonu
Scopus İndeksli Yayınlar Koleksiyonu / Scopus Indexed Publications Collection
WoS İndeksli Yayınlar Koleksiyonu / WoS Indexed Publications Collection

Show full item record



CORE Recommender

SCOPUSTM   
Citations

8
checked on Oct 13, 2024

WEB OF SCIENCETM
Citations

7
checked on Nov 21, 2024

Page view(s)

24
checked on Aug 24, 2024

Google ScholarTM

Check




Altmetric


Items in GCRIS Repository are protected by copyright, with all rights reserved, unless otherwise indicated.