Method for preparing zeolite molecular sieve by using oil shale residues
A technology of oil shale waste residue and zeolite molecular sieve, applied in the direction of solid waste removal, crystalline aluminosilicate zeolite, etc., can solve the problems of pollution, land occupation and environment, and achieve the goal of avoiding massive accumulation, reducing environmental pollution and low cost Effect
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Embodiment 1
[0016] ① Take 100g of oil shale waste slag that has been ground to below 100 mesh and roasted and activated at 550°C for 2 hours;
[0017] ② To the calcined waste residue, add H with a mass concentration of 30% in a mass ratio of 1:3 2 SO 4 The solution is heated to 90-95 DEG C and reacted for 5 hours, hot filtered to obtain an aluminum-iron solution and a filter residue, the obtained filter residue is washed 1-2 times, and the obtained washing solution is merged into an aluminum-iron solution;
[0018] 3. the primary aluminum-iron solution obtained in step 2. is evaporated to 2 / 6 of the original volume, crystallized by cooling, and filtered to obtain aluminum sulfate crystals and acid-containing aluminum-iron filtrate;
[0019] 4. According to the mass ratio of 1:3, the acid-containing aluminum-iron filtrate obtained in step 3. is mixed with the newly added oil shale waste residue, heated to 90-95 DEG C to react for 3 hours, crystallized by cooling, and filtered to obtain al...
Embodiment 2
[0025] ① Take 200g of oil shale waste slag after grinding to below 100 mesh and roasting and activating at 550℃ for 2 hours;
[0026] ② To the calcined waste residue, add H with a mass concentration of 30% in a mass ratio of 1:3 2 SO 4 The solution is heated to 90-95 DEG C and reacted for 5 hours, hot filtered to obtain an aluminum-iron solution and a filter residue, the obtained filter residue is washed 1-2 times, and the obtained washing solution is merged into an aluminum-iron solution;
[0027] 3. the primary aluminum-iron solution obtained in step 2. is evaporated to 4 / 6 of the original volume, crystallized by cooling, and filtered to obtain aluminum sulfate crystals and acid-containing aluminum-iron filtrate;
[0028] 4. According to the mass ratio of 1:3, the acid-containing aluminum-iron filtrate obtained in the previous step 3. is mixed with the newly added oil shale waste residue, heated to 90-95 ° C for reaction for 3 hours, crystallized by cooling, and filtered to...
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