Low-alkali α-alumina powder excellent in viscosity characteristics and production method thereof
A technology of α-alumina and viscosity characteristics, applied in chemical instruments and methods, inorganic chemistry, aluminum compounds, etc., can solve problems such as complexity, increased manufacturing costs, and increased manufacturing processes
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Embodiment 1
[0047] Aluminum hydroxide obtained by the Bayer process (the average secondary particle size is 55 μm and sodium oxide (Na 2 O) 0.2% by mass of the component) is added and mixed with aluminum fluoride as a halogen mineralizer in a ratio of 0.4% by mass in terms of alumina, and the resulting mixture is added to a firing furnace made of alumina ceramics containing silica. In the container, firing was carried out at 1500° C.±10° C. for about 15 hours using a tunnel kiln.
[0048] Sodium oxide (Na 2 O) Composition, molding density, and BET specific surface area. The results are shown in Table 1.
[0049] Next, using a vibrating ball mill (manufactured by Chuo Kakiki Co., Ltd. (Chuo Kakki Co., Ltd.)) containing 7.6 kg of 15 mmΦ alumina balls in a 6 liter (L) tank, 1.5 kg of the alumina balls obtained by the above-mentioned firing were fired. The fired product is pulverized so that the average particle size after pulverization (D av : Dp50) is 3.0 μm, the average particle size a...
Embodiment 2
[0052] Using a rotary ball mill (manufactured by Chuo Kakiki Co., Ltd.) containing 255 kg of 20 mmΦ alumina balls in a 300 liter (L) mill, 50 kg of the burnt product obtained in Example 1 was pulverized so that after pulverization The average particle size (D av : Dp50) is 3.1 μm, the average particle size after the pulverization (D av ) and BET equivalent diameter before crushing (D BET ) particle size ratio (D av / D BET ) was 1.27, and α-alumina was obtained.
[0053] For the obtained α-alumina, in the same manner as in Example 1, the 45 μm sieve weight (+45 μm) was measured and the width value was obtained as a particle size distribution, and the viscosity at the time of resin filling was measured. The results are shown in Table 1.
Embodiment 3
[0055] Using the same rotary ball mill as in Example 2 (manufactured by Chuo Chemical Equipment Co., Ltd.), 50 kg of the burnt product obtained in Example 1 was pulverized so that the average particle diameter (D av : Dp50) is 2.9 μm, the average particle size after the pulverization (D av ) and BET equivalent diameter before crushing (D BET ) particle size ratio (D av / D BET ) was 1.19, and α-alumina was obtained.
[0056] For the obtained α-alumina, in the same manner as in Example 1, the 45 μm sieve weight (+45 μm) was measured and the width value was obtained as a particle size distribution, and the viscosity at the time of resin filling was measured. The results are shown in Table 1.
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