Magnesium oxide particle aggregate
A particle aggregation, magnesium oxide technology, applied in magnesium oxide, furnace type, solid-state chemical plating, etc., can solve problems such as insufficient reaction
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Embodiment 1
[0065] The magnesite is roasted at 850°C for 1 hour in a rotary kiln, and crushed into magnesium oxide with a cage crusher. In order to control the particle structure, magnesium oxide is added to water so that the concentration of magnesium hydroxide after the reaction is 3mol / kg, stirred at 400rpm, and reacted at 85-95°C for 2 hours to generate the precursor magnesium hydroxide. After the generated magnesium hydroxide is filtered with a filter press, washed with water and dried, the obtained magnesium hydroxide is roasted in a rotary kiln at 900°C at 22°C with a final reaction rate of 40% citric acid activity in the range of 120-140 For 1 hour, it is baked to form magnesium oxide particle aggregates. Then, it was pulverized with a hammer mill at a hammer rotation speed of 3500 rpm and a classifier rotation speed of 3000 rpm to produce magnesium oxide particle aggregates having a predetermined particle aggregation structure.
Embodiment 2
[0067] The calcium hydroxide slurry was added into the brine so that the concentration of the reacted magnesium hydroxide was 2 mol / kg, stirred at 600 rpm, and reacted at 80° C. for 2 hours. Then, filter, wash, and dry the magnesium hydroxide with a filter press, use a rotary kiln at 890°C for 1 hour at 22°C and a citric acid activity of 40% at a final reaction rate of 120 to 140 for 1 hour. It is an aggregate of magnesium oxide particles. Then, the powder was pulverized by a pulverizer at a hammer rotation speed of 3500 rpm and a classifier rotation speed of 4000 rpm to produce a magnesium oxide particle aggregate having a predetermined particle aggregation structure.
Embodiment 3
[0069] Calcium hydroxide slurry was added to magnesium chloride, so that the concentration of magnesium hydroxide after the reaction was 1mol / kg, and then 10ppm coagulant polyaluminum chloride was added, stirred at 400rpm, and reacted at 60°C for 20 hours. Then, filter, wash, and dry the magnesium hydroxide with a filter press, use a rotary kiln at 900°C for 1 hour at 22°C and a citric acid activity of 40% at a final reaction rate of 120 to 140 for 1 hour. It is an aggregate of magnesium oxide particles. Then, the powder was pulverized with a pulverizer at a hammer rotation speed of 3200 rpm and a classifier rotation speed of 4000 rpm to produce a magnesium oxide particle aggregate having a predetermined particle aggregation structure.
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