Method for producing high-purity magnesium oxide by reduction and pyrolysis of magnesium sulphate by using natural gas
A technology of magnesium sulfate and natural gas, applied in magnesium oxide and other directions, can solve the problems of low purity of magnesium oxide, polluted environment by tail gas, low pyrolysis efficiency, etc., and achieve the effects of easy control of reaction conditions, high pyrolysis efficiency and simple process.
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Embodiment 1
[0018] (1) Dehydrate magnesium sulfate heptahydrate with a purity greater than 99% at 500°C for 4 hours to obtain anhydrous magnesium sulfate, which is then ground and sieved, and -120 mesh accounts for 80%;
[0019] (2) Put 100 g of anhydrous magnesium sulfate prepared in step 1 into the reactor, and raise the temperature to 900°C;
[0020] (3) Pass natural gas (methane content greater than 98%) into a reactor equipped with anhydrous magnesium sulfate for reduction pyrolysis, control the flow rate of natural gas to 160ml / min, and the reaction time to 0.5 h;
[0021] (4) Turn on switch 1, turn off switches 2 and 3 at the same time, pass the sulfur dioxide gas generated by the reduction pyrolysis reaction into the reactor 11, and turn on the switch of the oxygen cylinder at the same time, and convert it into sulfur trioxide under the catalytic oxidation of the vanadium catalyst , sulfur trioxide is passed into the 98.3% concentrated sulfuric acid absorption bottle 12, the conce...
Embodiment 2
[0029] (1) Dehydrate magnesium sulfate heptahydrate with a purity greater than 99% at 550°C for 3 hours to obtain anhydrous magnesium sulfate, which is then ground and sieved, and -150 mesh accounts for 80%;
[0030] (2) Put 300 g of anhydrous magnesium sulfate prepared in step 1 into the reactor, and raise the temperature to 950°C;
[0031] (3) Pass natural gas (methane content greater than 98%) into the reactor equipped with anhydrous magnesium sulfate, control the flow rate of natural gas to 480ml / min, and the reaction time to 0.5 h;
[0032] (4) Turn on the switch 2 and turn off the switches 1 and 3 at the same time, pass the sulfur dioxide produced by the reduction pyrolysis reaction into the absorption bottle 10 filled with pyrolusite slurry, remove impurities, filter, evaporate and crystallize the obtained adsorption liquid, and dry Obtain manganese sulfate, the carbon dioxide gas that produces absorbs with lime water, filters and obtains calcium carbonate, and excessiv...
Embodiment 3
[0038] (1) Dehydrate magnesium sulfate heptahydrate with a purity greater than 99% at 600°C for 2 hours, then grind it finely, sieve it, and -180 mesh accounts for 80%;
[0039] (2) Put 600 g of anhydrous magnesium sulfate prepared in step 1 into the reactor and raise the temperature to 1000°C;
[0040] (3) Pass natural gas (methane content greater than 98%) into the reactor, control the flow of natural gas to 960ml / min, and the reaction time to 0.5 h;
[0041] (4) Turn on the switch 3, turn off the switches 1 and 2 at the same time, pass the sulfur dioxide produced by the reduction pyrolysis reaction into the absorption bottle 7 filled with sodium hydroxide solution to generate a sodium sulfite solution, purify the sodium sulfite solution, evaporate, crystallize, and dry Obtain anhydrous sodium sulfite, the carbon dioxide gas that produces absorbs with lime water, obtains calcium carbonate after filtering, and excessive natural gas is collected in the collecting bottle 9;
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