A method for removing low-concentration sulfur dioxide in flue gas and preparing sodium metabisulfite
A sodium pyrosulfite and sulfur dioxide technology, applied in the chemical industry, can solve the problems of large steam consumption, high operating cost, and long system process of desulfurization by-products, and achieve the effects of wide application range, low operating cost, and high desulfurization efficiency
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Embodiment 1
[0051] This example is the first specific embodiment of the method for preparing sodium metabisulfite product from low-concentration sulfur dioxide in flue gas according to the present invention:
[0052] The method for preparing sodium metabisulfite product, its process is as follows:
[0053] (1), flue gas purification: the temperature is 280 ℃, SO 2 Content 0.1% (ie 2860mg / Nm 3 ) of zinc smelting rotary kiln flue gas 50000Nm 3 / h, sent to the water washing tower for washing to remove dust and SO in the flue gas 3 , the dust content of flue gas after water washing is 30mg / Nm 3 , the flue gas temperature drops to 60°C;
[0054] (2), SO 2 Absorption: SO after purification and cooling 2 Flue gas with 0.1% content 50000Nm 3 / h, enter the secondary series rotary tangential flow scrubber, in the secondary series rotary tangential flow scrubber, and the Na-containing 2 CO 3 30wt%-Na 2 SO 3 15wt%-NaHSO 3 10wt% of the absorbing liquid (pH value is 6.5) is in reverse conta...
Embodiment 2
[0058] This example is the second specific embodiment of the method for preparing sodium metabisulfite product from low-concentration sulfur dioxide in flue gas according to the present invention:
[0059] The method for preparing sodium metabisulfite product, its process is as follows:
[0060] (1), flue gas purification: the temperature is 250 ℃, SO 2 Content 1.0% (ie 28600mg / Nm 3 ) of zinc smelting rotary kiln flue gas 60000Nm 3 / h, sent to the water washing tower for washing to remove dust and SO in the flue gas 3 , the dust content of flue gas after water washing is 28mg / Nm 3 , the flue gas temperature drops to 65°C;
[0061] (2), SO2 absorption: SO after purification and cooling 2 Flue gas with 1.0% content 60000Nm 3 / h, enter the secondary series spray scrubber, in the secondary series series spray scrubber, and the Na containing 2 CO 3 35wt%-Na 2 SO 3 18wt%-NaHSO 3 7wt% of the absorption liquid (pH value is 6.8) is in reverse contact, an absorption reaction ...
Embodiment 3
[0065] The present embodiment is the third specific embodiment of the method for preparing sodium metabisulfite product from low-concentration sulfur dioxide in flue gas according to the present invention:
[0066] The method for preparing sodium metabisulfite product, its process is as follows:
[0067] (1), flue gas purification: the temperature is 250 ℃, SO 2 Content 2.0% (ie 57200mg / Nm 3 ) of zinc smelting rotary kiln flue gas 50000Nm 3 / h, sent to the water washing tower for washing to remove dust and SO in the flue gas 3 , the dust content of flue gas after water washing is 29mg / Nm 3 , the flue gas temperature drops to 70°C;
[0068] (2), SO2 absorption: SO after purification and cooling 2 Flue gas with 2.0% content 50000Nm 3 / h, enter the secondary scrubber connected in series with the rotary tangential flow scrubber and the spray scrubbing tower. 2 CO 3 40wt%-Na 2 SO 3 20wt%-NaHSO3 5wt% of the absorption liquid (pH value is 7.0) is in reverse contact, and the...
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