Method for producing polyaluminum ferric chloride composite water purification agent by using plant slag and coal gangue
A technology of polyaluminum ferric chloride and power plant slag, which is applied in the fields of ferric halide, solid waste removal, flocculation/sedimentation water/sewage treatment, etc. It can solve the problems of long production lines, large floor space and high production costs, and achieve Improve the seepage rate, reduce production costs, and strengthen the effect of market competitiveness
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Embodiment 1
[0020] 5 tons of coal gangue are added to the reaction kettle, while injecting 3 tons of industrial waste hydrochloric acid with a mass percentage of 24%, injecting 2 tons of clear water, adding 0.2 tons of potassium chloride and 0.22 tons of calcium chloride in parts by weight, and Fully stir in the reaction kettle, and seal the reaction kettle to prevent the acid from volatilizing. Inject steam for heating, heat to 100-110°C, and react for 2-3 hours. After the reaction is completed, the material is cooled to 70-80°C for separation of residue and liquid. The separated liquid enters into another reaction tank and adds a basicity adjusting agent to adjust the polymerization. The time of the polymerization reaction is controlled to be 1-2 hours, and the temperature is 90-100°C. After the polymerization reaction is completed, cool to 70°C and separate the slag liquid while it is hot. The separation liquid is a liquid product. In the liquid product, the mass fraction of alumina i...
Embodiment 2
[0022] Add 5 tons of slag to the reactor, inject 3 tons of industrial waste hydrochloric acid with a mass percentage of 24%, inject 2 tons of clear water, add 0.2 tons of sodium chloride by weight, and fully stir in the reactor to react The kettle is sealed to prevent the acid from volatilizing. Inject steam for heating, heat to 110-120°C, and react for 2-3 hours. After the reaction is completed, the material is cooled to 70-80°C for separation of residue and liquid. The separated liquid enters into another reaction kettle and adds a basicity adjusting agent for polymerization adjustment, and the polymerization reaction time is controlled to be 1-2 hours, and the temperature is 95-100°C. After the polymerization reaction is completed, cool to 70°C and separate the slag liquid while it is hot. The separation liquid is a liquid product. In the liquid product, the mass fraction of alumina is 10.18%, the mass fraction of iron oxide is 1.5%, and the mass fraction of water-insolubl...
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