A method and equipment for producing titanium dioxide by sulfuric acid method
A sulfuric acid method and titanium dioxide technology, applied in the direction of titanium dioxide, titanium oxide/hydroxide, etc., can solve the problems of increasing the concentration cost and increasing the burden of titanium liquid concentration, so as to avoid the increase of concentration cost, improve the blockage of pipeline valves and Delivery pump, avoiding the effect of burden
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Embodiment 1-4
[0059] The device and method for producing titanium dioxide by the sulfuric acid method provided by the present invention are described.
[0060] The equipment adopted in embodiment 1-4 is specified as follows:
[0061] like figure 1 As shown, the equipment for producing titanium dioxide by the sulfuric acid method provided by the present invention includes an acid hydrolysis / leaching device 10, a crystallization device (not shown in the figure), a crystal separation device (not shown in the figure), a dilution tank 30, a process The circulating water pipeline 40, the crystalline titanium liquid tank 50, the small water tank 60, and the calcining device (not shown in the figure). in,
[0062]The crystal separation device is arranged downstream of the acid hydrolysis / leaching device 10 and the crystallization device, and includes multiple sets of centrifuges 20. The centrifugal liquid outlet ends of the multiple sets of centrifuges 20 pass through the centrifugal mother liquo...
Embodiment 1
[0069] With reference to the method for producing titanium dioxide by the sulfuric acid method in Comparative Example 2, the difference is: the centrifugal mother liquor and the sewage circulating water (the filtered calcined tail gas spraying waste water, the temperature is 40 ° C) in the dilution tank 30 at a weight ratio of 1:2.5 Mixing to form a centrifugal mother liquor dilution, the centrifugal mother liquor dilution is used as a part of the leaching water, and is added to the acidolysis maturation system in the acidolysis / leaching device 10 through a small water tank 60 (i.e. is added to the leaching step), and The amount of the centrifugal mother liquor diluent is 15wt%-20wt% of the amount of the leaching water, and the amount of the centrifugal mother liquor diluent is controlled so that the TiO2 in the titanium sulfate solution after the leaching step 2 The concentration is 120~125g / L.
Embodiment 2
[0071] With reference to the method for producing titanium dioxide by the sulfuric acid method in Comparative Example 2, the difference is: the centrifugal mother liquor is mixed with net circulating water (circulating water from the cooling equipment) at a weight ratio of 1:2 to form a centrifugal mother liquor dilution, and the centrifugal mother liquor dilution As a part of the leaching water, it is added to the acidolysis maturation system in the acidolysis / leaching device 10 through a small water tank 60 (that is, added to the leaching step), and the amount of the centrifugal mother liquor diluent is the amount of the leaching solution. 25wt%-30wt% of the amount of water taken, and the amount of the centrifugation mother liquor diluent is controlled so that the TiO2 in the titanium sulfate solution after the leaching step 2 The concentration is 130~140g / L.
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