Treatment method for abandoned dichlorodifluoromethane
A processing method, Freon technology, applied in chemical instruments and methods, fluorine/hydrogen fluoride, inorganic chemistry, etc., can solve the problems of inability to recover effective substances, waste of resources, dangerous secondary compounds, etc., to achieve resource utilization and reduce environmental protection. hazard, high hydrolysis efficiency
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Embodiment 1
[0026] (1) Mix zirconium sulfate, titanic acid, and tungstic acid according to the molar ratio of zirconium, titanium, and tungsten of 1:0.55:0.15, add water to granulate, and spray-dry at 280°C to prepare catalyst particles with a diameter of 8mm;
[0027] (2) The particles are naturally piled up in the tubular reactor, and the accumulation volume of the catalyst particles accounts for 30% of the total volume of the tubular reactor;
[0028] (3) Simultaneously pass Freon and water vapor into the tubular reactor at a volume ratio of 1:4, while maintaining the temperature in the tubular reactor at 265°C, the pressure at 1atm, and the contact time for 8min.
[0029] (4) The tail gas after catalytic hydrolysis absorbs water vapor with 98% concentrated sulfuric acid, dehydrated alcohol absorbs hydrogen chloride gas, absorbs hydrogen fluoride gas with saturated sodium bicarbonate solution, and absorbs carbon dioxide gas with sodium carbonate solution. The final hydrolysis rate of F...
Embodiment 2
[0031] (1) Mix zirconium sulfate, titanic acid, and tungstic acid according to the molar ratio of zirconium, titanium, and tungsten of 1:0.55:0.15, add water to granulate, and spray-dry at 280°C to prepare catalyst particles with a diameter of 8mm;
[0032] (2) The particles are naturally piled up in the tubular reactor, and the accumulation volume of the catalyst particles accounts for 35% of the total volume of the tubular reactor;
[0033] (3) Simultaneously feed Freon and water vapor into the tubular reactor at a volume ratio of 1:4, while maintaining the temperature in the tubular reactor at 285°C, the pressure at 1atm, and the contact time for 8min.
[0034] (4) The tail gas after catalytic hydrolysis absorbs water vapor with 98% concentrated sulfuric acid, dehydrated alcohol absorbs hydrogen chloride gas, absorbs hydrogen fluoride gas with saturated sodium bicarbonate solution, and absorbs carbon dioxide gas with sodium carbonate solution. The final hydrolysis rate of F...
Embodiment 3
[0036] (1) Mix zirconium sulfate, titanic acid, and tungstic acid according to the molar ratio of zirconium, titanium, and tungsten of 1:0.5:0.15, add water to granulate, and spray-dry at 300°C to prepare catalyst particles with a diameter of 8mm;
[0037] (2) The particles are naturally piled up in the tubular reactor, and the accumulation volume of the catalyst particles accounts for 35% of the total volume of the tubular reactor;
[0038] (3) Simultaneously feed Freon and water vapor into the tubular reactor at a volume ratio of 1:5, while maintaining the temperature in the tubular reactor at 300°C, the pressure at 1.5atm, and the contact time for 8 minutes.
[0039] (4) The tail gas after catalytic hydrolysis absorbs water vapor with 98% concentrated sulfuric acid, dehydrated alcohol absorbs hydrogen chloride gas, absorbs hydrogen fluoride gas with saturated sodium bicarbonate solution, and absorbs carbon dioxide gas with sodium carbonate solution. The final hydrolysis rat...
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