SYNTHESIS AND KINETICS CRYSTALIZATION ZEOLITE-NA FROM TAILING TAILINGS.

Bauxite tailings is by product derived from bauxite ore beneficiation. The beneficiation process is done by separating waste particles such as clay, roots, grain, bauxite ore <2 mm are discarded or be referred to as a waste product or tailings. High concentration of alumina and silica in bauxi...

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Bibliographic Details
Main Author: Indra Septiansyah, Sy
Format: Theses
Language:Indonesia
Online Access:https://digilib.itb.ac.id/gdl/view/78498
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Institution: Institut Teknologi Bandung
Language: Indonesia
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Summary:Bauxite tailings is by product derived from bauxite ore beneficiation. The beneficiation process is done by separating waste particles such as clay, roots, grain, bauxite ore <2 mm are discarded or be referred to as a waste product or tailings. High concentration of alumina and silica in bauxite tailings considered as one of the reasons why these tailings can be used as base material in the making new products, namely synthetic zeolites. Zeolites synthetic is selected because zeolites are imported, expensive and have uniform properties and >150 types of synthetic zeolites can be made commercially and even in industrial zeolite can be used widely as an adsorbent, ion exchange, membranes, catalysts, etc. Chemical analysis of bauxite tailings showed the composition of alumina (Al2O3) is approximately 49,41%, silica (SiO2) is about 12,58%, hematite (Fe2O3) is approximately 10,06% and some other inorganic oxides are at small amounts. The conversion process bauxite tailings into zeolite is carried out by caustic fusion between bauxite tailings and NaOH at ratios of 1:1,0; 1:1,5; 1:2,0 and 1:2,5 (w/w) with temperature of 5500C for 90 minutes. The result caustic fusion product is called frit which then leached with water. Leaching aims to obtain an extract Si and Al dissolved in the form of sodium silicate and sodium aluminate wherein the content of Si, Al and Na dissolved in solution is measured by AAS (Atomic Adsorption Spectroscopy). Solution has been known content of Si, Al and Na is made gel and set compositions molar ratio of 1,2Na2O.0,5SiO2.0,5Al2O3.10H2O by adding a solution of sodium silicate (Na2SiO3) as the source of Si suitable precursor in the synthesis zeolites. Crsytallization product is done by using the hydrothermal method at low temperatures with variable temperatures of 100, 110 and 1200C and crystallization 2, 4, 6, 8, 10 and 12 hours. Zeolite-Na produced is characterized by using XRD, SEM-EDS and BET. The result showed that caustic fusion can form compounds among NaAlO2 and Na2SiO3 soluble in water with high percent extraction of alumina is 99,78% and silica is 27,03% with mass ratio bauxite tailing and NaOH 1:1,5 (w/w) in temperature is 5500C for 90 minutes. The best crystallization obtained by highest % crystallinity zeolite-Na is 92,3% in temperature 1200C for 12 hours. The transformation kinetics marked a new crystallites that grow along the crystal deformed which can be seen through the approach of kinetic model of the Avrami and Arrhenius equations showing that the rate controlled by diffusion surface crystallization with the type order 0,7688, 0,8988 and 0,9441 temperature range of crystal growth 100-1200C and time 2-12 hours with the activation energy of 55,6 KJ/mol.K. Types of zeolite product is zeolite Na-P1 cell unit GIS (Gismondinea) with the chemical formula Na6Al6Si10O32.12H2O, fine white powders, crystal size 1-2,5?m and the type of mesoporous product with a cubic shape that can be used as adsorbent media and ion exchange.