Method for preparing 4A zeolite from red mud solution and bauxite chemical desilication solution
A technology of bauxite and lotion, applied in the direction of crystalline aluminosilicate zeolite, A-type crystalline aluminosilicate zeolite, etc., can solve the problem of high cost of raw materials, achieve simple preparation process, good economic benefits, and promote popularization and application Effect
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Embodiment 1
[0028] 1) Raw material treatment: take the red mud washing liquid and the bauxite chemical desiliconization solution in the alumina production process, and filter the two solutions respectively. After filtering, the components of the two liquid raw materials respectively meet: a. Red mud washing liquid: Na 2 O concentration is 60~90g / L, Al 2 o 3 Concentration is 60~90g / L, solution α K 1.50~1.70; b. Bauxite chemical desiliconization solution: SiO 2 Concentration is 30~50g / L, Na 2 O concentration is 80-100g / L;
[0029] 2) Condition control of hydrothermal synthesis: with n(SiO 2 / Al 2 o 3 )=2.0; n(Na 2 O / SiO 2 )=3.0; n(H 2 O / Na 2 O)=40 ingredients; crystallization temperature 95°C, crystallization time 6h; aging temperature 75°C, aging time 2h;
[0030] 3) Hydrothermal synthesis process: Take the red mud lotion a and the chemical desiliconization solution b according to the ingredients described in 2), and slowly add b to the beaker containing the a solution, and at ...
Embodiment 2
[0034] 1) raw material processing: as described in step 1) in embodiment 1);
[0035] 2) Condition control of hydrothermal synthesis: with n(SiO 2 / Al 2 o 3 )=2.0; n(Na 2 O / SiO 2 )=2.6; n(H 2 O / Na 2 O)=40 ingredients; crystallization temperature 95°C, crystallization time 6h; aging temperature 75°C, aging time 2h;
[0036] 3) Hydrothermal synthesis process: the same as step 3 in Example 1);
[0037] 4) Subsequent processing: the same as step 4) in Example 1.
[0038] The particle size D50 (um) of the obtained 4A zeolite powder was 2.08, and the calcium ion exchange capacity was 312 mg / g.
Embodiment 3
[0040] 1) raw material processing: as described in step 1) in embodiment 1);
[0041] 2) Condition control of hydrothermal synthesis: with n(SiO 2 / Al 2 o 3 )=2.0; n(Na 2 O / SiO 2 )=2.2; n(H 2 O / Na 2 O)=40 ingredients; crystallization temperature 95°C, crystallization time 6h; aging temperature 75°C, aging time 2h;
[0042] 3) Hydrothermal synthesis process: the same as step 3 in Example 1);
[0043] 4) Subsequent processing: the same as step 4) in Example 1.
[0044]The particle size D50 (um) of the obtained 4A zeolite powder was 2.21, and the calcium ion exchange capacity was 329 mg / g.
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