Method for processing alumina process calcium silicone slag
A processing method and technology of calcium-silica slag, which are applied in the purification of aluminate/alumina/aluminum hydroxide, preparation of alkali metal aluminate/alumina/aluminum hydroxide, calcium carbonate/strontium/barium, etc., can solve the problem. The sintering method increases the energy consumption, increases the burden of the clinker kiln, and the large circulation volume of materials, etc., to reduce the energy consumption, improve the equipment capacity and utilization rate, and reduce the dilution effect.
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Embodiment 1
[0013] Add the calcium silicon slag to the carbon mother liquor with a total alkali concentration of 100g / l, the carbon mother liquor and the calcium silicon slag have a liquid-to-solid weight ratio of 3, and a gas with a volume concentration of 30% of carbon dioxide is introduced at a temperature of 60°C. After reacting for 30 minutes, the reaction product is separated; part of the seminal fluid is used as a liquid spray to flush the reaction slag and sent to the deep desiliconization tank; the reacted solution is sent to the adjustment tank of the clinker dissolution process for recovery.
Embodiment 2
[0015] Add the calcium silicon slag to the carbon mother liquor with a total alkali concentration of 120g / l. The carbon mother liquor and the calcium silicon slag have a liquid-to-solid weight ratio of 5, and the volume concentration of carbon dioxide is 35%. After reacting for 80 minutes, the reaction product is separated; part of the seminal fluid is used as a liquid spray to flush the reaction slag and sent to the deep desiliconization tank; the reacted solution is sent to the adjustment tank of the clinker dissolution process for recovery.
Embodiment 3
[0017] The calcium silicon slag is added to the carbon mother liquor whose total alkali concentration is 150g / l, the carbon mother liquor and the calcium silicon slag are 10 according to the liquid-solid weight ratio, and the gas whose volume concentration is 40% is passed into the carbon dioxide, and the feeding amount of the gas is Calculated according to the processing capacity, react at 120°C for 120 minutes, and separate the reaction product; use part of the semen as a liquid spray to flush the reaction slag and send it to the deep desiliconization tank; send the reacted solution to the clinker for dissolution Process adjustment tank for recycling.
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