A study on the preparation of fine and low soda alumina
A simple process to produce fine and low soda α-alumina (α-Al 2O 3) from a commercial grade aluminium trihydroxide (gibbsite, Al(OH) 3) produced by KC Corporation Ltd was developed. There are two options for this process with the first one producing low soda α-alumina (< 0.05% Na 2O) having a mea...
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Published in | International journal of mineral processing Vol. 80; no. 2; pp. 126 - 132 |
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Main Authors | , , , , |
Format | Journal Article |
Language | English |
Published |
Elsevier B.V
01.09.2006
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Subjects | |
Online Access | Get full text |
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Summary: | A simple process to produce fine and low soda α-alumina (α-Al
2O
3) from a commercial grade aluminium trihydroxide (gibbsite, Al(OH)
3) produced by KC Corporation Ltd was developed. There are two options for this process with the first one producing low soda α-alumina (<
0.05% Na
2O) having a mean particle size of 50 μm. The second option yields a fine product with a mean size of less than 10 μm. In the first option, a plant aluminium trihydroxide containing 0.20% Na
2O was first fluidized with nitrogen at 400–600 °C to yield an amorphous activated alumina. This intermediate product was then treated with acetic or oxalic acid, washed with water and heated to 1200 °C to form calcined α-alumina, having a Na
2O content of less than 0.05%. A 20 min leaching using 0.2 M acetic or oxalic acid could yield an alumina product containing 0.04% Na
2O. In the second option, a new technique for the preparation of fine and low soda α-alumina was evaluated using an attrition mill working also as a leaching vessel at 80 °C. Fine (<
10 μm in mean particle size) and low soda (<
0.04% Na
2O) alumina was produced by a 20 min leaching step with 0.2 M acetic acid and concurrent attrition milling. |
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ISSN: | 0301-7516 1879-3525 |
DOI: | 10.1016/j.minpro.2006.03.006 |