Method for treating vanadium industrial wastewater by aid of semi-dry flue gas desulfurization ash
A technology for industrial wastewater and desulfurization ash, which is applied in multi-stage water treatment, water/sewage treatment, chemical instruments and methods, etc., can solve the problems of incomplete discharge, high treatment cost, and low treatment efficiency, and achieve secondary Pollution and land occupation problems, good treatment effect, and high economic value
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Embodiment 1
[0034] The pH of vanadium industrial wastewater is 1, the concentration of total chromium is 4500 mg / L, the concentration of hexavalent chromium is 3800 mg / L, the concentration of pentavalent vanadium is 200 mg / L, ammonia nitrogen (NH 3 -N) concentration 4000mg / L; introduce the vanadium industrial wastewater into the reduction reaction pool, stir and add semi-dry flue gas desulfurization ash; the amount of semi-dry flue gas desulfurization ash added is 10% of the total mass of vanadium and chromium in the vanadium industrial wastewater times; XRD pattern of semi-dry flue gas desulfurization ash figure 2 shown;
[0035] Adding inorganic acid to adjust the pH of all the materials in the reduction reaction tank to 1.0, and then performing a reduction reaction for 30 minutes under stirring conditions to reduce high-valence vanadium and chromium to low-valence states; the inorganic acid is sulfuric acid;
[0036] After the reduction reaction is completed, let it settle for 2 hour...
Embodiment 2
[0042] Method is with embodiment 1, and difference is:
[0043] (1) The pH of vanadium industrial wastewater is 2, the concentration of total chromium is 4200 mg / L, the concentration of hexavalent chromium is 3600 mg / L, the concentration of pentavalent vanadium is 150 mg / L, ammonia nitrogen (NH 3 -N) concentration 3600mg / L; introduce the vanadium industrial wastewater into the reduction reaction tank, stir and add semi-dry flue gas desulfurization ash; the amount of semi-dry flue gas desulfurization ash added is 8% of the total mass of vanadium and chromium in the vanadium industrial wastewater times;
[0044] (2) Add inorganic acid to adjust the pH of all materials in the reduction reaction tank to 2.0, and then react under stirring conditions for 20 minutes; the inorganic acid is hydrochloric acid;
[0045] (3) After the reduction reaction is completed, let it stand for 1.5 hours to settle;
[0046] (4) Introduce the primary mixed solution into the neutralization sedimenta...
Embodiment 3
[0052] Method is with embodiment 1, and difference is:
[0053] (1) The pH of vanadium industrial wastewater is 2, the concentration of total chromium is 3800 mg / L, the concentration of hexavalent chromium is 3400 mg / L, the concentration of pentavalent vanadium is 100 mg / L, ammonia nitrogen (NH 3 -N) concentration 3200mg / L; introduce the vanadium industrial wastewater into the reduction reaction pool, stir and add semi-dry flue gas desulfurization ash; the amount of semi-dry flue gas desulfurization ash added is 6% of the total mass of vanadium and chromium in the vanadium industrial wastewater times;
[0054] (2) Add mineral acid to adjust the pH of all materials in the reduction reaction tank to 2.0, and then react under stirring conditions for 15 minutes; the mineral acid is nitric acid;
[0055] (3) After the reduction reaction is completed, let it stand for precipitation for 1 hour;
[0056] (4) Introduce the primary mixed solution into the neutralization sedimentation ...
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