Method for Continuous Production of Liquid Calcium Chloride Using Fluorine-Containing By-Product Waste Hydrochloric Acid
A technology of waste hydrochloric acid and calcium chloride, applied in the direction of calcium/strontium/barium chloride, calcium/strontium/barium halide, etc., can solve problems that have not been seen in the production of liquid calcium chloride from fluorine-containing waste hydrochloric acid. Achieve the effect of meeting the requirements of mass processing, high production efficiency and environmental protection
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Embodiment 1
[0019] The fluorine-containing by-product waste hydrochloric acid with a content of 800ppm in the process of producing fluorine chemical products such as difluorochloromethane (R22) produced by a fluorine chemical enterprise and a fluorine-containing by-product waste hydrochloric acid with a HCl mass % of hydrochloric acid of a concentration of 30% is used as a raw material. The reaction vessel (reaction kettle) with a stirring device reacts continuously with limestone and limestone with a particle size of 15m to 125mm. The specific working conditions are: the above-mentioned limestone is excessive at the beginning, and then the by-product hydrochloric acid is added continuously In the operating mode of the working condition, the pH value of the reaction completion liquid produced in the continuous reaction process is controlled to be pH1.5 and the reaction liquid is introduced (overflowed) into the liquid storage tank (neutralization stirring tank) in an overflow mode, and is c...
Embodiment 2
[0022] The fluorine-containing by-product waste hydrochloric acid with a content of 2000ppm of fluorine ion produced in the process of producing fluorine chemical products such as tetrafluoromonomer by a fluorine chemical enterprise and a HCl mass% of hydrochloric acid with a concentration of 12% is used as a raw material in a stirring device for reaction React continuously with limestone that tends to be powdery and has a particle size of 40μm to 2mm in the container (reactor). In the working condition, the pH value of the reaction completion liquid produced in the continuous reaction process is controlled to be pH 3.5 and the reaction liquid is introduced into (neutralizing the stirring tank) liquid storage tank in an overflow mode, and is added to the liquid storage tank in a continuous manner at the same time. The milk of lime with a specific concentration of 25% by mass % adjusts the pH value of the reaction solution in the storage tank to pH=8, and after 36 hours of react...
Embodiment 3
[0024] The fluorine-containing by-product waste hydrochloric acid with a content of 20000ppm in the process of producing fluorine chemical products such as R32 (difluoromethane) produced by fluorine chemical enterprises and a HCl mass % of hydrochloric acid with a concentration of 26% is used as a raw material in a stirring tank. In the reaction vessel (reactor) of the device, there is a continuous reaction with limestone that tends to be small in shape and has a particle size of 0.5-2mm. In the working condition of adding limestone, the pH value of the reaction completion liquid produced in the continuous reaction process is controlled to be pH2.5 and the reaction liquid is introduced into (neutralizing the stirring tank) liquid storage tank in an overflow mode, and is continuously supplied to the storage tank in a continuous manner. Add lime milk with a mass % specific concentration of 55% in the liquid tank to adjust the pH value of the reaction liquid in the liquid storage ...
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