Method for recycling and processing waste liquid produced by combined desulfurization and denitrification technology using steel slag as absorbent
A technology for desulfurization, denitrification, and waste liquid recovery, which is applied in gaseous effluent wastewater treatment, filtration treatment, multi-stage water treatment, etc., can solve problems such as intractability, difficulty in obtaining pure nitrate products, and complex metallurgical slag composition. To achieve the effect of great value
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[0047] The specific embodiment part of the present invention provides a method for recycling and treating waste liquid produced by using steel slag as an absorbent combined with desulfurization and denitrification process. The preparation method includes the following steps:
[0048] (1) Using steel slag as an absorbent in conjunction with the waste liquid produced by the desulfurization and denitrification process for solid-liquid separation;
[0049] (2) adding unslaked lime and / or slaked lime to the liquid obtained after the solid-liquid separation in step (1) to adjust the pH to remove impurities, and filter after the precipitation is complete;
[0050] (3) the pH of the filtrate obtained in step (2) is adjusted to 5-7, and then oxidized by a micro-nano bubble generating device;
[0051] (4) evaporating and concentrating the liquid obtained after oxidation in step (3) to crystallize, filter, and dry to obtain a calcium nitrate product.
[0052] Wherein, the specific opera...
Embodiment 1
[0055] In this embodiment, the steel slag slurry absorbs SO 2 and NO x The content of steel slag in the waste liquid generated later is 15wt%, pH=6, and total salt concentration is 30wt%.
[0056] (1) filter the waste liquid to remove solid impurities;
[0057] (2) The filtrate obtained in step (1) is adjusted to pH 9 with unslaked lime, and precipitation removes NO 3 - , NO 2 - and Ca 2+ other impurity ions, filtered to obtain the filtrate;
[0058] (3) the filtrate obtained by step (2) is added with nitric acid to adjust the pH to be 6, then the filtrate in the filtrate tank is passed into from the water inlet of the micro-nano bubble generating device, and the amount of feed per hour is controlled to be 1 / of the total amount of filtrate 2. At the same time, add hydrogen peroxide with 10% of the total mass of the filtrate from the water inlet, and introduce air (21% oxygen content) from the inlet. After 3 hours of aeration in the generating device, it enters the fil...
Embodiment 2
[0061] In this embodiment, the steel slag slurry absorbs SO 2 and NO x The content of steel slag in the waste liquid generated later is 10wt%, pH=5.5, and total salt concentration is 40wt%.
[0062] (1) filter the waste liquid to remove solid impurities;
[0063] (2) The filtrate obtained in step (1) is adjusted to pH 10.8 with CaO saturated solution, and the precipitation removes NO 3 - , NO 2 - and Ca 2+ other impurity ions, filtered to obtain the filtrate;
[0064] (3) the filtrate obtained by step (2) is added with nitric acid to adjust pH=6.5, then the filtrate in the filtrate tank is passed into from the water inlet of the micro-nano bubble generating device, and the amount of feed per hour is controlled to be 0.8 of the total amount of filtrate, Add the hydrogen peroxide of filtrate gross mass 5% from water inlet simultaneously, pass into air and oxygen mixed gas (oxygen content 30%) from inlet, the volume mass ratio of intake and liquid intake is 30L / t, and filtra...
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