Method for preparing superfine alumina silicate
An ultra-fine aluminum silicate and bauxite technology, applied in the direction of aluminum silicate and silicate, can solve the problems of poor product quality, high raw material requirements, waste liquid discharge, etc., to reduce production links and achieve high product purity , the effect of reducing production costs
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Embodiment 1
[0028] The preparation method of superfine aluminum silicate of the present invention, carries out according to following steps successively:
[0029] (1) 500g of bauxite powder with particle size less than or equal to 70μm, Al 2 o 3 The weight content is 62%, its aluminum-silicon molar ratio is 5, and the evaporated carbon mother liquor with sodium carbonate content of 50g / l is divided according to Na 2 O / Al 2 o 3 = 1.3 After batching, add 5g of sintering auxiliary limestone powder with a particle size of 50 μm or less and 10 g of quartz sand powder with a particle size of 80 μm or less at the same time for secondary batching, and put it into the furnace for sintering reaction at a temperature of 1150 ° C. Time 2 hours, obtained clinker.
[0030] (2) The stripping conditions of burning clinker control are: temperature 80°C, time 1.2 hours, liquid-solid ratio control 10, and crude liquid is obtained after stripping.
[0031] (3) Add 25 g of calcined kaolin powder with a p...
Embodiment 2
[0036] The preparation method of superfine aluminum silicate of the present invention, carries out according to following steps successively:
[0037] (1) 500g of bauxite powder with a particle size of less than or equal to 100μm, the molar ratio of aluminum to silicon is 8, and the mother liquor of evaporated carbon is divided according to Na 2 O / Al 2 o 3 After batching at a ratio of =1.3, add 50g of sintering aid limestone powder with a particle size of 30 μm or less and 50 g of quartz sand powder with a particle size of 60 μm or less at the same time for secondary batching, and put it into the furnace for sintering reaction to obtain clinker .
[0038] (2) Same as Example 1, except that the stripping conditions are: temperature 90° C., time 0.8 hour, liquid-solid ratio controlled at 7, and crude liquid is obtained after stripping.
[0039] (3) Same as Example 1, except that 80 g of calcined kaolin powder is added, the synthesis temperature is controlled at 60° C., and th...
Embodiment 3
[0045] As described in Example 1, the difference is:
[0046] (1) Add 500g of bauxite powder with a particle size of less than or equal to 90μm, and its aluminum-silicon molar ratio is 7, add 25g of limestone powder with a particle size of less than or equal to 60μm, and 25g of quartz sand powder with a particle size of less than or equal to 40μm for secondary The ingredients are put into the furnace for firing reaction to obtain clinker.
[0047] (2) Same as Example 1, except that the stripping conditions are: temperature 85° C., time 0.9 hour, liquid-solid ratio controlled at 9, and crude liquid is obtained after stripping.
[0048] (3) Same as Example 1, except that 50 g of calcined kaolin powder is added, the synthesis temperature is controlled at 55° C., the synthesis time is controlled at 0.9 hours, and the aging temperature is controlled at 65° C.
[0049] (4) with embodiment 1.
[0050] (5) With embodiment 1, difference is liquid-solid ratio control 11.
[0051] Oth...
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