Method for pre-treating phosphorus rock by mixture of titanium dioxide waste acid and fluorine-containing waste water
A titanium dioxide waste acid and pretreatment technology, applied in chemical instruments and methods, phosphorus compounds, phosphoric acid, etc., can solve the problems of low phosphorus loss rate, high production efficiency, low operating cost, etc., and achieve low phosphorus loss and magnesium content. The effect of reducing and high demagnesization rate
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Embodiment 1
[0032] 899.59Kg of fluorine-containing waste water (fluorine content 3.3g / l) and 249.89Kg of titanium dioxide waste acid (20% sulfuric acid concentration, 10% ferrous sulfate content) are quickly mixed with 1000kg of solid content 65% through a tubular mixer Phosphate rock (P 2 O 5 The content is 28.54%, the MgO content is 2.63%, and the ore powder 100-mesh sieve remains 11%.) The slurry is fed into 5m through the pipeline. 3 The pretreatment reaction tank makes the phosphate rock react with the waste acid of titanium dioxide under stirring, the stirring intensity is 100rpm, the pH value of the reaction slurry is controlled to be 2.5, the temperature is 44℃, and the residence time of the materials in the pretreatment tank is 2h. The slurry out of the pretreatment tank is separated and washed by the filter press to filter P in the biscuit base 2 O 5 The content is 29.08%, and the MgO content is 0.15%. The pH value of the filtrate is 3.0, the MgO content is 0.47%, the P content is...
Embodiment 2
[0035] 2024.39Kg of fluorine-containing wastewater (4.2g / l fluorine content) and 303.66Kg of waste titanium dioxide acid (30% sulfuric acid concentration and 14% ferrous sulfate content) are quickly mixed with 1000kg of solid content 65% through a tubular mixer Phosphate rock (P 2 O 5 The content is 28.54%, the MgO content is 2.63%, and the ore powder 100-mesh sieve remains 11%.) The slurry is fed into 5m through the pipeline. 3 The pretreatment reaction tank makes the phosphate rock react with the waste acid of titanium dioxide under stirring, the stirring intensity is 100rpm, the pH value of the reaction slurry is controlled to be 3.0, the temperature is 42°C, and the residence time of the materials in the pretreatment tank is 2h. The slurry out of the pretreatment tank is separated and washed by the filter press to filter P in the biscuit base 2 O 5 The content is 28.76%, and the MgO content is 0.47%. The pH value of the filtrate was 3.5, the MgO content was 0.45%, the P cont...
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