A method for treating rutile titanium dioxide wastewater
A technology for rutile titanium dioxide and waste water, applied in chemical instruments and methods, water/sewage multi-stage treatment, water/sludge/sewage treatment, etc., can solve the problem of high energy consumption, no economic benefits, and unbalanced consumption of titanium dioxide Acid waste water and other problems, to achieve the effect of improving recovery efficiency, major economic benefits and environmental protection benefits
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Embodiment 1
[0024] will be 10m 3 Transfer the acidic wastewater into the mixing tank, start stirring, and slowly add 6m 3 -7m 3 For alkaline wastewater, control the mixing temperature at 50-60°C, stop stirring after 10-15 minutes, the pH of the mixed solution is between 7-8, and after natural settlement for 60 minutes, the supernatant liquid is transferred to a thickener, and the polypropylene with a concentration of 200ppm The amide was added according to the concentration ratio of 5ppm, mixed and stirred for 30min, and settled for 60min to obtain the lower precipitate (mainly containing TiO 2 155kg), the precipitate is returned to the alkali-soluble storage tank in the calcined seed crystal preparation process to continue pressure filtration, and the neutral water in the upper layer contains sulfate ions and sodium ions, which are used for the production of titanium dioxide after the ions are removed by activated carbon adsorption.
[0025] The lower layer of sediment mixed with acidi...
Embodiment 2
[0027] will be 20m 3 Transfer the acidic wastewater into the mixing tank, start stirring, and slowly add 11m 3 -14m 3For alkaline waste water, control the mixing temperature at 50-60°C, stop stirring after 10-15 minutes, the pH of the mixed solution is between 7-8, and after 60 minutes of natural settlement, the supernatant liquid is transferred to a thickener, and the concentration of 200ppm polypropylene The amide was added into it according to the concentration ratio of 10ppm, mixed and stirred for 30min, and settled for 60min to obtain the lower precipitate (mainly containing TiO 2 286kg), the precipitate is returned to the alkali-soluble storage tank in the calcined seed crystal preparation process to continue pressure filtration, and the neutral water in the upper layer contains sulfate ions and sodium ions, which are used for the production of titanium dioxide after the ions are removed by activated carbon adsorption.
[0028] The lower layer of sediment mixed with ac...
Embodiment 3
[0030] will be 25m 3 Transfer the acidic waste water into the mixing tank, turn on the stirring, and slowly add 15m 3 -17m 3 For alkaline waste water, control the mixing temperature at 50-60°C, stop stirring after 10-15 minutes, the pH of the mixed solution is between 7-8, and after 60 minutes of natural settlement, the supernatant liquid is transferred to a thickener, and the concentration of 200ppm polypropylene The amide was added at a concentration ratio of 8ppm, mixed and stirred for 30 minutes, and settled for 60 minutes to obtain the lower layer of precipitate (mainly containing TiO 2 341kg), the precipitate is returned to the alkali-soluble storage tank in the calcined seed crystal preparation process to continue pressure filtration, and the neutral water in the upper layer contains sulfate ions and sodium ions, which are used for titanium dioxide production after being adsorbed by activated carbon to remove ions.
[0031] The lower layer of sediment mixed with acidi...
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