Method for recycling semi-dry process desulphurization byproduct sodium sulfate
A technology for semi-dry desulfurization and desulfurization by-products, applied in chemical instruments and methods, alkali metal sulfite/sulfite, alkali metal compounds, etc., can solve the problem of consuming large manpower, material and financial resources, secondary pollution, Environmental hazards and other issues, to achieve the effect of realizing circular economy, reducing total emissions, and solving environmental problems
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Embodiment 1
[0011] Embodiment 1: a kind of semi-dry process desulfurization by-product sodium sulfate recycling method, the method comprises the steps:
[0012] (1) Sodium sulfate, a by-product of desulfurization, was dissolved in water to make a solution, the mass concentration of the solution was 20%, the temperature was controlled at 20-30°C, and then bubbling aeration was carried out for oxidation, and the aeration time was 40 minutes;
[0013] (2) Filter the mixed solution after aeration, then send the obtained filtrate to the evaporation device for evaporation and crystallization treatment, stop heating when crystals are precipitated, and then cool down to 18°C to cool and crystallize to obtain a saturated crystal slurry;
[0014] (3) Centrifuge the above-mentioned saturated crystal slurry to obtain centrifuged liquid and sodium sulfate crystals, then dry the sodium sulfate crystals to finally obtain anhydrous sodium sulfate crystals, dry the obtained crystals and carry out composi...
Embodiment 2
[0015] Embodiment 2: a kind of semi-dry process desulfurization by-product sodium sulfate recycling method, the method comprises the steps:
[0016] (1) Sodium sulfate, a by-product of desulfurization, is dissolved in water to make a solution, the mass concentration of the solution is 30%, the temperature is controlled at 20-30°C, and then bubbling aeration oxidation is carried out, and the aeration time is 60 minutes;
[0017] (2) Filter the mixed solution after aeration, then carry out aeration and oxidation treatment on the obtained filtrate for 20~30 minutes, and then send it to the evaporation device for evaporation and crystallization treatment, stop heating when crystals are precipitated, and then cool down to 18°C Cooling crystallization obtains saturated magma;
[0018] (3) Centrifuge the above-mentioned saturated crystal slurry to obtain centrifuged liquid and sodium sulfate crystals, then dry the sodium sulfate crystals to finally obtain anhydrous sodium sulfate cry...
Embodiment 3
[0019] Example 3: The anhydrous sodium sulfate crystals after drying in Example 2 are used as a raw material to replace Glauber's salt in a 10% weight ratio to carry out a glass production test. The roasting temperature is 1480 ° C. After 1 hour of heat preservation, it is poured out and cooled to remove microbes. Except that there are more bubbles, there is no obvious difference compared with the original glass. Therefore, it can be concluded that the recovered anhydrous sodium sulfate crystals can be used as raw materials, thereby reducing production costs.
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