Active silicon slag, its preparation method, desiliconization method containing sodium aluminosilicate
A technology containing sodium aluminosilicate and sodium aluminosilicate, which is applied in the purification of aluminate/alumina/aluminum hydroxide, the preparation of alkali metal aluminate/alumina/aluminum hydroxide, and the removal of solid waste, etc. It can solve the problems of poor seed crystal activity, large seed crystal circulation volume, and low desiliconization efficiency, and achieve the effect of simple operation and low seed crystal circulation volume
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[0036] Wherein, the preparation method of active silicon slag comprises the following steps:
[0037] The silicon slag is ground for 1h to 8h to obtain active silicon slag.
[0038] Among them, when grinding the silicon slag, wet grinding is used.
[0039] Wherein, the preparation device of active silicon slag is selected from rod mill, sand mill, ball mill and tube mill.
[0040] Among them, the value range of the total alkali concentration Nt of the sodium aluminosilicate solution is 90g / L~130g / L, the value range of αk is 1.30~1.50, SiO 2 The value range of concentration is 4g / L~6g / L.
[0041] Wherein, the set temperature ranges from 20°C to 60°C.
[0042] Wherein, the desiliconization method containing sodium aluminosilicate solution also includes the step of performing lime milk deep desiliconization on the first desiliconization product containing sodium aluminosilicate solution to obtain the second desilication product containing sodium aluminosilicate solution.
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Embodiment 1~20
[0046]
[0047] According to the embodiment 1~20 listed in the above table, the preparation method of active silicon slag provided by the invention and the preparation device of active silicon slag can be used to prepare active silicon slag, and the active silicon slag can be used to contain sodium aluminosilicate When desiliconization is carried out, the active silicon slag reacts with silicon in sodium aluminate to form a sodalite-type sodium silicate slag solid. After solid-liquid separation, the value range of the silicon mass percentage reduction in the sodium aluminate solution is 90%. ~95%, and the operation is simple and the circulation of seed crystals is small.
[0048] In addition, a small part of the obtained sodalite-type sodium-silicon slag solid can enter the silicon slag activation process, and the rest can be returned to the batching process of the clinker sintering process.
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