An Oxygen Assistant for Oxidation of Sinter Flue Gas Semi-dry Desulfurization Ash
A semi-dry desulfurization and sintering flue gas technology, applied in the direction of calcium/strontium/barium sulfate, etc., can solve the problems of poor desulfurization and oxidation efficiency of semi-dry desulfurization and accelerate the oxidation efficiency of desulfurization ash, so as to speed up the oxidation efficiency and avoid escape , the effect of high purity
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Embodiment 1
[0029] A kind of oxygen auxiliary agent used for the oxidation of sintering flue gas semi-dry method desulfurization ash of the present invention, comprises acidic auxiliary agent, and the acidity of this acidic auxiliary agent is between sulfurous acid and sulfuric acid, namely the pKa of acidic auxiliary agent 1 The acidity coefficient is between the pKa of sulfurous acid and sulfuric acid 1 Between the acidity coefficients, the oxygen promoter is used to oxidize the calcium sulfite in the desulfurization ash, the acid promoter is easily soluble in water, and the pKa of the acid promoter in 25°C water 1 The acidity coefficient is: 1.00-1.89, where the pKa 1 Is the first-order acidity coefficient of the acidic auxiliary agent, and the acidic auxiliary agent of the present embodiment is oxalic acid, and its pKa 1 is 1.27; the oxygen promoter in the present embodiment is oxalic acid, and the oxygen promoter solution is obtained after mixing oxalic acid with water. Among them:...
Embodiment 2
[0042] The basic content of this embodiment is the same as that of Example 1, except that the acidic additive is dichloroacetic acid (CHCl 2 COOH), its pKa in water at 25°C 1 is 1.30, the oxygen promoter in this embodiment is dichloroacetic acid, and the oxygen promoter solution is obtained after dichloroacetic acid is mixed with water. The oxygen promoter of the invention greatly improves the oxidation efficiency of the desulfurization ash, and realizes the oxidation of the desulfurization ash under the condition of low temperature in an open container. After the reaction, the reactant precipitate was heated and dried at a temperature of 100° C. to obtain a dry powder, and the content of calcium sulfate dihydrate in the dry powder reached 95.3%.
Embodiment 3
[0044] The basic content of this embodiment is the same as that of Example 1, except that the acidic auxiliary agent is composed of oxalic acid and dichloroacetic acid, and the mass ratio of oxalic acid and dichloroacetic acid is 2:1. The agent consists of oxalic acid and dichloroacetic acid. The use of the oxygen promoter of the present invention greatly improves the oxidation efficiency of desulfurization ash, and realizes the oxidation of desulfurization ash under low temperature conditions in an open container. Powder, the content of calcium sulfate dihydrate in the dry powder reaches 94.8%.
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