Treatment method for detoxifying and recycling chromium slag
A treatment method and technology of chromium slag, which is applied in the field of environmental pollution control, can solve the problems of complex recycling, incomplete reduction, and high recycling costs, and achieve a large amount of leaching liquid, which is conducive to subsequent recycling and low equipment construction costs. Effect
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Embodiment 1
[0039] The processing method of chromium slag detoxification recycling, it comprises the steps:
[0040] 1) First, take a sample and analyze the main component content (the main component is chromium content), acidity and particle size in the chromium (VI) waste residue:
[0041] After analyzing a waste residue containing chromium (VI), the content of chromium (VI) on a dry basis is 2.6wt%, the content of insoluble silicate and aluminosilicate is 83wt%, and the oxyacids of acid-soluble iron, sodium, magnesium and calcium The contents of salts, oxides and hydroxides are between 0.5 and 5 wt%, and the contents of other elements are all less than 0.1 wt%. The acidity is PH=6.5. The content of large particles above 20 mesh is 8wt%, and the maximum particle diameter is about 1.5cm. The average water content of chrome slag is 19wt%.
[0042] 2) Build four with a volume of 500m 3 A special leaching tank (cement pool), and a movable spray pipe is built above the leaching tank. Eac...
Embodiment 2
[0066] The processing method of chromium slag detoxification recycling, it comprises the steps:
[0067] 1) Sampling and analysis of main component content (main component is chromium content), acidity and particle size in the waste residue containing chromium (VI) at first;
[0068] After analyzing a waste residue containing chromium (VI), the content of chromium (VI) on a dry basis is 3.2wt%, the content of insoluble silicate and aluminosilicate is 83wt%, and the oxyacids of acid-soluble iron, sodium, magnesium, and calcium The contents of salts, oxides and hydroxides are between 0.5 and 5 wt%, and the contents of other elements are all less than 0.1 wt%. The acidity is PH=6.5. The content of large particles above 20 mesh is 8wt%, and the maximum particle diameter is about 1.5cm. The average water content of chrome slag is 19wt%.
[0069] 2) Build 3 leaching tanks (and do anti-seepage treatment), build a movable spray pipe above the leaching tank, and set a leaching liquid...
Embodiment 3
[0077] Embodiment 3 (build 6 leaching ponds):
[0078] The processing method of chromium slag detoxification recycling, it comprises the steps:
[0079] 1) Sampling and analysis of main component content (main component is chromium content), acidity and particle size in the waste residue containing chromium (VI) at first;
[0080] After analyzing a waste residue containing chromium (VI), the content of chromium (VI) on a dry basis is 1.8wt%, the content of insoluble silicate and aluminosilicate is 83wt%, and the oxyacids of acid-soluble iron, sodium, magnesium, and calcium The contents of salts, oxides and hydroxides are between 0.5 and 5 wt%, and the contents of other elements are all less than 0.1 wt%. The acidity is PH=13.0. The content of large particles above 20 mesh is 8wt%, and the maximum particle diameter is about 10cm. The average water content of chrome slag is 19wt%.
[0081] 2) Build 6 leaching tanks (and do anti-seepage treatment), build a movable spray pipe a...
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