Pulp bed reaction technique for producing chlorine gas by chloride hydrogen catalytic oxidation
A technology of catalytic oxidation and hydrogen chloride, which is applied in the direction of chlorine/hydrogen chloride and chloride preparation, can solve the problems of high production cost, complicated preparation process of carbon nanotube materials, unsuitable for industrial application, etc., to eliminate the influence of internal diffusion, The effect of improving the utilization rate and reaction ability of the catalyst and avoiding the phenomenon of sintering deactivation
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Embodiment 1
[0017] In a 60mL three-phase slurry reactor, 50g of inert molten salt composed of zinc chloride, potassium chloride and sodium chloride is loaded, and a cerium-copper-potassium composite oxide catalyst is used, and the atomic ratio of cerium-copper-potassium in the composite oxide is It is 0.5:1:0.9. The particle size of the catalyst is 0.4 μm, the weight fraction of the catalyst in the molten salt is 20%, the reaction temperature is 350°C, the space velocity of hydrogen chloride in the raw material gas is 600L / kg·h, and the molar ratio of oxygen to hydrogen chloride is 1 / 1, The mixture of the two was passed into a three-phase slurry reactor, and the water vapor was separated by a condenser at the outlet of the reactor. After continuous and stable reaction for 4 hours, the conversion rate of hydrogen chloride was 85.2%.
Embodiment 2
[0019] In a 60mL three-phase slurry reactor, 50g of the inert molten salt composed of sodium bisulfate and potassium hydrogensulfate is charged, and the cerium-copper-potassium composite oxide catalyst in Example 1 is adopted, and the particle diameter of the catalyst is 0.4 μm. The weight fraction of the salt is 20%, the reaction temperature is 250°C, the space velocity of hydrogen chloride in the raw material gas is 600L / kg·h, the molar ratio of oxygen to hydrogen chloride is 1 / 1, and the mixture of the two is passed into a three-phase slurry reaction In the reactor, the water vapor was separated by a condenser at the outlet of the reactor. After continuous and stable reaction for 4 hours, the conversion rate of hydrogen chloride was 44.7%.
Embodiment 3
[0021] In a 60mL three-phase slurry reactor, 50g of inert molten salts composed of zinc chloride, potassium chloride and sodium chloride are charged, and the cerium-copper-chromium-potassium composite oxide catalyst in Example 1 is adopted, and the particle diameter of the catalyst is 0.4 μm, the weight fraction of the catalyst in the molten salt is 20%, the reaction temperature is 350°C, the space velocity of hydrogen chloride in the raw material gas is 600L / kg·h, and the molar ratio of oxygen to hydrogen chloride is 1 / 1, the mixture of the two is passed into In the three-phase slurry reactor, the water vapor was separated by a condenser at the outlet of the reactor, and after continuous and stable reaction for 4 hours, the conversion rate of hydrogen chloride was 84.5%.
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