Processing method for resource recycling and zero discharge of steel hydrochloric acid pickling waste liquid
A technology of pickling waste liquid and treatment method, which is applied in the direction of metallurgical wastewater treatment, preparation of iron compounds, chemical instruments and methods, etc., can solve the problems of failure to meet national standards, no multiple cycles, low use value, etc., and achieve treatment Low cost, water saving, no secondary pollution effect
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Embodiment 1
[0028] The pH of the waste hydrochloric acid pickling solution for iron and steel is <0, and the content of iron ions is 12%.
[0029] (1) Neutralize pre-oxidation and adjust pH
[0030] The original iron and steel pickling waste liquid is diluted 1 times by volume, and under the stirring of ventilated air, the prepared calcium carbide slag slurry (15% carbide slag suspension in terms of calcium hydroxide mass fraction) is slowly added to the iron and steel pickling waste. In the solution, adjust the pH at 8.5 and enter the next step of oxidation.
[0031] (2) Air oxidation
[0032] Naturally heat up the suspension obtained in the previous step to 50°C, pass through air for oxidation, and the air velocity is 0.15m 3 / (m 2 ﹒ min), and continuously add the calcium carbide slag slurry used in (1), keep the pH value at 8.5, and form a dark green suspension, nFe 3+ / nFe 2+ Reach 2:1, stop oxidation.
[0033] (3) After stopping the oxidation, use the calcium carbide slag slur...
Embodiment 2
[0036] Iron and steel pickling waste solution pH<0, iron ion content 12%.
[0037] (1) Neutralize pre-oxidation and adjust pH
[0038] Slowly add the prepared calcium carbide slag slurry (15% carbide slag suspension in terms of calcium hydroxide mass fraction) to the steel pickling waste, adjust the pH to 8.5, enter the next step of oxidation, and naturally heat up to 30°C .
[0039] (2) Air oxidation
[0040] Into the 30°C suspension in the previous step, air is introduced at a velocity of 0.15m 3 / (m 2 ﹒ min), and continuously add the calcium carbide slag slurry used in (1), keep the pH 8.0 constant, forming a dark green suspension, nFe 3+ / nFe 2+ Reach 1.2:1, stop oxidation.
[0041] (3) After stopping the oxidation, use the calcium carbide slag slurry in (1) to adjust the pH of the suspension to 9.0, heat the suspension to 90° C. with steam, and stir for 2 hours.
[0042] After the synthesis reaction is completed, it is filtered with a plate and frame filter press,...
Embodiment 3
[0044] The pH value of the waste hydrochloric acid pickling solution for iron and steel is 0-1, and the content of iron ions is 8%.
[0045] (1) Neutralize pre-oxidation and adjust pH
[0046] The filtrate filtered by the plate-and-frame filter press treated as in Example 1 and carbide slag were used to prepare carbide slag suspension (25% carbide slag suspension in terms of calcium hydroxide mass fraction). Under air stirring, the calcium carbide slag slurry is slowly added to the steel pickling waste liquid to react, stir evenly, adjust the pH at 9.0, and enter the next step of oxidation.
[0047] (2) Air oxidation
[0048] Into the 50°C suspension in the previous step, pass air into it for oxidation, and the air velocity is 0.15m 3 / (m 2 ﹒ min), and continuously add the calcium carbide slag slurry used in (1), keep the pH 8.5 constant, forming a dark green suspension, nFe 3+ / nFe 2+ Reach 1.6:1, stop oxidation.
[0049] (3) After stopping the oxidation, heat the susp...
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