Method for preparing flue gas desulfurization powder adsorbent from liquid-solid wastes
A technology for desulfurization powder and waste, applied in separation methods, chemical instruments and methods, alkali metal compounds, etc., can solve problems such as classification and recovery of metal elements, difficulty in purification, damage to acid-base balance of water quality, metal pollution, etc., to achieve improved catalytic performance Effects of reaction rate, micropore integrity, and increased desulfurization rate
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Embodiment 1
[0025] Raw material: copper electrolysis wastewater 1, in which Cu 2+ The concentration is 25.8g / L, Ni 2+ The concentration is 11.4g / L, Fe 3+ The concentration is 8.3g / L, H 2 SO 4 The concentration is 179.6g / L; the main components of depotassiation soot are 30.12wt% manganese, 12.35wt% zinc, 3.90wt% iron, 30.79wt% oxygen, 15.71wt% silicon, and 7.13wt% others; calcium carbide slag slurry, moisture 42.4 wt%, calcium hydroxide 55.84wt%, other 1.76wt%.
[0026](1) Liquid-solid separation of calcium carbide slag slurry was carried out with a centrifuge to obtain milk of lime and calcium carbide slag; (2) Under the condition of continuous stirring at a stirring speed of 300rpm, 1000g of copper electrolysis wastewater was added to the reactor and heated to 60°C, Then slowly add 100g of 120 mesh depotassium soot ash, and after acidolysis reaction for 1.0h, centrifuge and wash to obtain acidolysis residue and sulfate solution; (3) under the condition of continuous stirring at a sti...
Embodiment 2
[0030] Raw materials: the same as the depotassium soot ash and carbide slag slurry described in the above examples; copper electrolysis wastewater 2, wherein Cu 2+ The concentration is 48.7g / L, Ni 2+ The concentration is 18.9g / L, Fe 3+ The concentration is 4.2g / L, H 2 SO 4 The concentration is 247.4g / L.
[0031] (1) Liquid-solid separation of calcium carbide slag slurry was carried out with a centrifuge to obtain milk of lime and calcium carbide slag; (2) Under the condition of continuous stirring at a stirring speed of 500rpm, 1000g of copper electrolysis wastewater was added to the reactor and heated to 70°C, Then slowly add 300g of 120 mesh depotassium soot ash, and after 3.0h of acid hydrolysis reaction, centrifuge and wash to obtain acid hydrolysis residue and sulfate solution; (3) under the condition of continuous stirring at a stirring speed of 1000rpm, add Add the milk of lime separated in step (1) to adjust the pH value of the solution to 11 in the sulfate solutio...
Embodiment 3
[0035] Raw materials: the same as the copper electrolysis wastewater 2, ferromanganese desulfurizer saturated sulfur waste residue, and carbide slag slurry described in the above-mentioned embodiments and comparative examples.
[0036] (1) Liquid-solid separation of calcium carbide slag slurry was carried out with a centrifuge to obtain milk of lime and calcium carbide slag; (2) Under the condition of continuous stirring at a stirring speed of 400rpm, 1000g of copper electrolysis wastewater was added to the reactor and heated to 80°C, Then slowly add 200g of 80 mesh ferromanganese desulfurizer saturated sulfur capacity waste residue, and after acidolysis reaction for 2.0h, centrifuge and wash to obtain acidolysis residue and sulfate solution; (3) under the condition of continuous stirring at a stirring speed of 750rpm, to Add the milk of lime separated in step (2) to the sulfate solution obtained in step (1) to adjust the pH value of the solution to 10, conduct a precipitation ...
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