A method for purifying desulfurization by-product ammonium sulfate
A technology of ammonium sulfate and by-products, applied in the direction of ammonium sulfate and other directions, can solve the problem of ammonium sulfate purification, etc., to overcome the high content of water insolubles and metal impurity ions, obvious impurity removal effect, and overcome the problem of coloration. Effect
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Embodiment 1
[0031] A method for purifying ammonium sulfate by-product of desulfurization. The desulfurization by-product ammonium sulfate described in this embodiment is the wet ammonia desulfurization by-product ammonium sulfate of a sintering plant of a steel company, and the appearance of the desulfurization by-product ammonium sulfate is as follows figure 1 Shown is a reddish-brown crystal; the main impurity content of the desulfurization by-product ammonium sulfate: tar content > 10mg / L, TFe content 0.057-0.095wt%, Pb, Cr and As total content 0.043-0.048wt%.
[0032] The concrete steps of the technical solution adopted in this embodiment are:
[0033] Step 1. Removal of water insoluble matter
[0034] Mix the desulfurization by-product ammonium sulfate and water according to the solubility of ammonium sulfate, stir the ingredients under normal pressure and 50-60°C for 0.5-1h, and filter to obtain filtrate I.
[0035] Step 2. Tar removal
[0036] The filtrate I is pumped into the e...
Embodiment 2
[0049] A method for purifying ammonium sulfate by-product of desulfurization. The desulfurization by-product ammonium sulfate described in this example is the wet-type ammonia desulfurization by-product ammonium sulfate of a sintering plant of a steel company. The appearance of the desulfurization by-product ammonium sulfate is reddish-brown crystal; 20mg / L, the content of TFe is 0.095-0.15wt%, and the total content of Pb, Cr and As is 0.048-0.053wt%.
[0050] The concrete steps of the technical solution adopted in this embodiment are:
[0051] Step one and step two are the same as step one and step two of embodiment 1.
[0052] Step 3, removal of Fe ions
[0053] At 20-40°C, add sodium carbonate to filtrate II, the amount of sodium carbonate added per cubic meter of filtrate II is 1.5-2.0 kg, stir for 3-4 hours, and filter to obtain filtrate III.
[0054] Step 4, removal of Pb, Cr and As ions
[0055] At 20-40°C, add sodium sulfide to filtrate III, the amount of sodium su...
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Abstract
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