Method and system for removing vanadium impurities in titanium tetrachloride
A technology of titanium tetrachloride and crude titanium tetrachloride, applied in titanium halide and other directions, can solve the problems of easy blockage of pipelines and heat exchangers, fast scaling of heating coils, and large area of production equipment. Achieve the effect of reducing steam consumption, stable product quality and high effective utilization rate
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[0023] Example 1
[0024] As shown in the figure, the system for removing vanadium impurities in titanium tetrachloride has a crude titanium tetrachloride supply tank 1. The crude titanium tetrachloride supply tank 1 passes through a pipeline and a feed port of a forced circulation pump tank 4 a is connected, the pipe between the crude titanium tetrachloride supply tank 1 and the forced circulation pump tank 4 is provided with a feed pump I2, and the discharge port c of the forced circulation pump tank 4 is connected to a heating heat exchanger 5 is connected by a pipeline. The pipeline between the forced circulation pump tank 4 and the heating heat exchanger 5 is provided with a forced circulation pump 3, and the discharge port of the forced circulation pump 3 is also connected with a mud tank 11, the The heating heat exchanger 5 is connected to the feed port e of the flash tank 6, and the discharge port f of the flash tank 6 is connected to the feed port h of the purification ...
Example Embodiment
[0034] Example 2
[0035] The system for removing vanadium impurities in titanium tetrachloride is the same as in Example 1.
[0036] During production, the specific steps are as follows:
[0037] (1) The crude titanium tetrachloride is pumped from crude titanium tetrachloride supply tank 1 into the forced circulation pump tank 4 through the feed pump I2, and the fatty acid is pumped into the forced circulation from the fatty acid supply tank 10 through the feed pump II12. In the pump tank 4, the mass ratio of the crude titanium tetrachloride to the fatty acid is 1400:1, wherein the fatty acid is an unsaturated straight-chain fatty acid with an unsaturation degree of 1 to 3 and a carbon number of 10 to 30;
[0038] (2) The forced circulation pump 3 pumps the crude titanium tetrachloride in the forced circulation pump tank 4 into the heating heat exchanger 5 through the forced circulation pump 3 to be heated to 170°C. When the heating heat exchanger is heated, the heating High-pressur...
Example Embodiment
[0045] Example 3
[0046] The system for removing vanadium impurities in titanium tetrachloride is the same as in Example 1.
[0047] During production, the specific steps are as follows:
[0048] (1) The crude titanium tetrachloride is pumped from crude titanium tetrachloride supply tank 1 into the forced circulation pump tank 4 through the feed pump I2, and the fatty acid is pumped into the forced circulation from the fatty acid supply tank 10 through the feed pump II12. In the pump tank 4, the mass ratio of the crude titanium tetrachloride to the fatty acid is 1200:1, wherein the fatty acid is an unsaturated straight-chain fatty acid with an unsaturation degree of 1 to 3 and a carbon number of 10 to 30;
[0049] (2) The forced circulation pump 3 pumps the crude titanium tetrachloride in the forced circulation pump tank 4 into the heating heat exchanger 5 through the forced circulation pump 3 to be heated to 150°C. When the heating heat exchanger is heated, the heating High-pressur...
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