Method for preparing low-ferrum crystalline aluminium chloride from coal ash
A technology of fly ash and aluminum chloride, applied in the direction of aluminum chloride, aluminum halide, recycling technology, etc., can solve the problems of adverse effects on physical and chemical properties of crystalline aluminum chloride products, high iron content, etc., and achieve iron removal Good effect, high raw material utilization rate and low production cost
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Embodiment 1
[0039] (1) Get the fluidized bed fly ash and pulverize to 120 orders, add water to make a slurry with a solid content of 33wt%, use the vertical ring magnetic separator for fly ash iron removal disclosed in the Chinese invention application 201010112520.3 Magnetic separation under 17,500 GS for 3 times, obtain a filter cake with a solid content of 37.5wt% after press filtration with a plate basket filter press (Henan Yuzhou filter press factory, model: BAS320);
[0040] (2) Put the filter cake into an acid-resistant reaction kettle, add industrial hydrochloric acid with a concentration of 28wt% to carry out acid-dissolution reaction, the mol ratio of HCl in hydrochloric acid and aluminum oxide in fly ash is 5: 1, and the stripping temperature is 150° C., stripping pressure 1.0MPa, stripping time 2h, after the reaction product is press-filtered and washed by the above-mentioned plate basket filter press, an acid dipping solution with a pH value of 1.5 is obtained;
[0041](3) A...
Embodiment 2
[0046] (1) Get the fluidized bed fly ash and pulverize to 200 orders, add water to make a slurry with a solid content of 30wt%, use the vertical ring magnetic separator disclosed in the Chinese invention application No. 201010112520.3 for fly ash iron removal Magnetic separation under 10,000 GS for 4 times, after pressing with a BAS320 plate basket filter press, a filter cake with a solid content of 35wt% was obtained;
[0047] Step (2) is with embodiment 1;
[0048] (3) After cooling the pickling solution to 90°C by heat exchange, use a corrosion-resistant pump to press into a resin column equipped with JK008 macroporous cationic resin (manufacturer: Anhui Wandong Chemical Factory) to remove iron. The immersion liquid flow rate is 2 times of resin volume / hour, obtains aluminum chloride refining liquid;
[0049] When the macroporous cationic resin is adsorbed and saturated, the resin can recover its adsorption capacity through elution and regeneration. The elution conditions ...
Embodiment 3
[0053] (1) Get the fluidized bed fly ash and pulverize to 300 orders, add water and make the slurry that the solid content is 35wt%, use the vertical ring magnetic separator disclosed in No. 201010112520.3 for fly ash iron removal in China Magnetic separation under 20,000 GS for 3 times, and a filter cake with a solid content of 40wt% was obtained after pressing with a BAS320 plate basket filter press;
[0054] Step (2) is with embodiment 1;
[0055] (3) After cooling the pickling solution to 70°C by heat exchange, use a corrosion-resistant pump to press into a resin column equipped with SPC-1 macroporous cationic resin (manufacturer: Shanghai Resin Factory) to remove iron. The immersion liquid flow rate is 3 times of resin volume / hour, obtains aluminum chloride refining liquid;
[0056] When the macroporous cationic resin is adsorbed and saturated, the resin is eluted and regenerated to restore its adsorption capacity. The elution conditions are: water is used as the eluent,...
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