Recycling using method of aluminum ash at last time
A technology for aluminum ash and ammonia removal, applied in chemical instruments and methods, preparation/separation of ammonium nitrate, ammonia, etc., can solve the problem of recycling ammonia and chloride in aluminum ash, large investment in equipment, and difficulty in refining Large and other problems, to avoid air dust pollution, improve utilization, and achieve the effect of harmlessness
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Embodiment 1
[0023] The recycling method of the last aluminum ash of the present embodiment, its steps are:
[0024] S1, catalytic deamination: add water and catalyst to the last aluminum ash under the condition of stirring and stirring to form a paste, and the weight percentage of water in the paste formed by adding water to the last aluminum ash is 60%; The body is heated and catalytically decomposed to remove ammonia, and the escaped ammonia generated by catalytic decomposition and deamination enters the ammonia absorption tower; the catalyst is one of sodium organic acid, sodium amino acid, sodium carbonate, sodium nitrate, sodium hydroxide, sodium aluminate or Several kinds of mixtures, the amount of catalyst used is 50% of the dry weight of the last aluminum ash; the heating temperature of heating and catalytic decomposition is 130°C, and the time is 1h;
[0025] S2. Use spray water or dilute acid to collect the escaped ammonia gas in the ammonia absorption tower to obtain ammonia wa...
Embodiment 2
[0029] The recycling method of the last aluminum ash of the present embodiment, its steps are:
[0030] S1. Catalytic deamination: Add water and catalyst to the last aluminum ash under the condition of stirring and stirring to form a paste. The weight percentage of water in the paste formed by adding water to the last aluminum ash is 50%; The body is heated and catalytically decomposed to remove ammonia, and the escaped ammonia generated by catalytic decomposition and deamination enters the ammonia absorption tower; the catalyst is one of sodium organic acid, sodium amino acid, sodium carbonate, sodium nitrate, sodium hydroxide, sodium aluminate or Several kinds of mixtures, the amount of catalyst used is 10% of the dry weight of the last aluminum ash; the heating temperature for heating and catalytic decomposition is 120°C, and the time is 2h;
[0031] S2. Use spray water or dilute acid to collect the escaped ammonia gas in the ammonia absorption tower to obtain ammonia water...
Embodiment 3
[0035] The recycling method of the last aluminum ash of the present embodiment, its steps are:
[0036] S1. Catalytic deamination: add water and catalyst to the last aluminum ash under the condition of stirring and stirring to form a paste, and the weight percentage of water in the paste formed by adding water to the last aluminum ash is 80%; The body is heated and catalytically decomposed to remove ammonia, and the escaped ammonia generated by catalytic decomposition and deamination enters the ammonia absorption tower; the catalyst is one of sodium organic acid, sodium amino acid, sodium carbonate, sodium nitrate, sodium hydroxide, sodium aluminate or Several kinds of mixtures, the amount of catalyst used is 100% of the dry weight of the last aluminum ash; the heating temperature for heating and catalytic decomposition is 150°C, and the time is 45min;
[0037] S2. Use spray water or dilute acid to collect the escaped ammonia gas in the ammonia absorption tower to obtain ammon...
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