Method for controlling content of silicon tetrachloride in fused salt chlorination process of high titanium slag

A technology of silicon tetrachloride and molten salt chlorination, applied in the direction of titanium halide, etc., can solve the problems of difficulty in the purification of titanium tetrachloride, the inability of the molten salt chlorination furnace to operate stably for a long period of time, and the difficulty in the production of titanium dioxide. The effect of post-processing steps, reduction of production steps, and reduction of energy consumption

Active Publication Date: 2011-05-04
中信钛业股份有限公司
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  • Application Information

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Problems solved by technology

More impurity oxides in high titanium slag, such as calcium and magnesium oxides, are separated from the product titanium tetrachloride during the production process, and silicon chloride enters the product, causing serious damage to the purification of titanium tetrachloride products. It has caused great difficulties, so that the molten salt chlorination furnace cannot run stably for a long period of time during the production process of molten salt chlorination, especially causing difficulties for the subsequent production of titanium dioxide

Method used

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  • Method for controlling content of silicon tetrachloride in fused salt chlorination process of high titanium slag
  • Method for controlling content of silicon tetrachloride in fused salt chlorination process of high titanium slag
  • Method for controlling content of silicon tetrachloride in fused salt chlorination process of high titanium slag

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Embodiment 1

[0011] As shown in the figure, a graphite electrode 2 is connected to the inside of the molten salt chlorination furnace 1, and the graphite electrode 2 is connected to the electric furnace transformer 3, and 45 tons of 700°C-900°C molten sodium, magnesium, Calcium, manganese, iron chloride multi-component molten salt, continuously add 100 parts of high-titanium slag, 10 parts of petroleum coke and 150 parts of chlorine in parts by weight, start the furnace for 1 month, and control the secondary temperature of the electric furnace transformer 3 The voltage is 20V, so that the output current of the molten salt chlorination furnace 1 is 500-800A, and the molten salt current is measured every hour. The change of the resistance of the molten salt is reflected by the change of the measured molten salt current, and then the molten salt chlorination furnace is obtained. The relationship between running time, molten salt current and the mass content of high-titanium slag in molten salt...

Embodiment 2

[0013] As shown in the figure, a graphite electrode 2 is connected to the inside of the molten salt chlorination furnace 1, and the graphite electrode 2 is connected to the electric furnace transformer 3, and 45 tons of 700°C-900°C molten sodium, magnesium, Calcium, manganese, iron chloride multi-component molten salt, add 100 parts of high titanium slag, 30 parts of petroleum coke and 250 parts of chlorine according to the weight ratio, start the furnace for 2 months, and control the secondary voltage of the electric furnace transformer 3 to 50V , so that the output current of the molten salt chlorination furnace 1 is 3200-3500A, and the molten salt current is measured every 2 hours, and the change of the resistance of the molten salt is reflected by the change of the measured molten salt current, and then the operation of the molten salt chlorination furnace is obtained. The relationship between time, molten salt current and the mass content of high-titanium slag in the furna...

Embodiment 3

[0015] As shown in the figure, a graphite electrode 2 is connected to the inside of the molten salt chlorination furnace 1, and the graphite electrode 2 is connected to the electric furnace transformer 3, and 45 tons of 700°C-900°C molten sodium, magnesium, Calcium, manganese, iron chloride multi-component molten salt, add 100 parts of high titanium slag, 20 parts of petroleum coke and 200 parts of chlorine according to the weight ratio, start the furnace for 8 months, and control the secondary voltage of the electric furnace transformer 3 to 30V , so that the output current of the molten salt chlorination furnace 1 is 1700-1900A, and the molten salt current is measured every 90 minutes, and the change of the resistance of the molten salt is reflected by measuring the change of the molten salt current, and then the operating time of the molten salt chlorination furnace, The relationship between the molten salt current and the mass content of high-titanium slag in the molten sal...

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Abstract

The invention provides a method for controlling content of silicon tetrachloride in fused salt chlorination process of high titanium slag, comprising the following steps of: introducing a graphite electrode into a fused salt chlorination furnace, connecting the graphite electrode with an electric furnace transformer, filling multi-component fused salt in the fused salt chlorination furnace, then adding high titanium slag, petroleum coke and chlorine, controlling the secondary voltage of the electric furnace transformer to be 20-50v and the output current to be 500-3500A, measuring the fused salt current for every 1-2h, obtaining the relation among the operating time of the fused salt chlorination furnace, and the fused salt current and the mass content of the high titanium slag in the fused salt; sampling the fused salt in the furnace during the production process, analyzing data and obtaining the mass content of SigmaTi and C, and controlling the mass content of SigmaTi at 1-3% and the mass content of the C at 2-7% by regulating the addition quantity of the high titanium slag and the petroleum coke and observing the current change of the fused salt. The method can ensure the stability of silicon tetrachloride content in titanium tetrachloride products during fused salt chlorination production, ensure that the silicon tetrachloride content in the titanium tetrachloride is below 0.18%, and also ensure the long-term and stable production of the fused salt chlorination furnace.

Description

technical field [0001] The invention relates to the process control of a molten salt chlorination furnace, a main reaction device in a molten salt chlorination production process, in particular to a method for controlling silicon tetrachloride content in a high titanium slag molten salt chlorination process. Background technique [0002] At present, large-scale molten salt chlorination production systems have been industrialized in China. In the molten salt chlorination production, the molten salt chlorination furnace is used as the main reaction generating device, and its function is that the high titanium slag is in the molten salt medium, and under the condition of the presence of the reducing agent (carbon), the chlorine gas converts the titanium in the high titanium slag Oxides and other oxides are chlorinated to chlorides. At present, there are no effective measures for the process control of silicon oxide chlorination, so that the content of silicon tetrachloride in ...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C01G23/02
Inventor 陈志勇马恩泉闫征彬吴琼李俊强槐永忠
Owner 中信钛业股份有限公司
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