The Process of Producing Titanium Tetrachloride Using Artificial Rutile in Fluidized Chlorination Furnace

A technology of artificial rutile and boiling chlorination furnace, applied in the direction of titanium tetrachloride, titanium halide, etc., can solve the problems of high production cost of activation modifier, surging, channeling, etc.

Inactive Publication Date: 2016-01-20
PANZHIHUA IRON & STEEL RES INST OF PANGANG GROUP
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

But this method is owing to adopting phosphorus-containing compound as the high production cost of activation modifier, the artificial rutile of generation, the fine particle that particle diameter is less than<0.1mm accounts for about 75%, wherein the fine particle that particle diameter is less than 0.074mm accounts for about 40% %about
Fine-grained artificial rutile refers to artificial rutile made by hydrochloric acid leaching method. This kind of artificial rutile has many micropores and low packing density. If the existing boiling chlorination method is used to produce titanium tetrachloride, artificial rutile with too fine particle size , it is not easy to establish a good fluidization, and technical problems such as channeling and surging are prone to occur, resulting in poor contact between artificial rutile particles and chlorine gas, and low chlorination efficiency; at the same time, it will also cause a large amount of fine-grained artificial rutile to be carried by the gas out, causing a lot of waste of raw materials
[0009] In summary, the existing artificial rutile method, the artificial rutile produced by the sulfuric acid method, the content of TiO2 is only 70-80%, and the content of CaO+MgO is as high as 7%-11%, which cannot meet the requirements of the boiling chlorination process. TiO2 content > 90%; fine-grained artificial rutile produced by hydrochloric acid leaching method, the fine particles with a particle size of less than <0.1mm account for about 75%, and the fine particles with a particle size of less than 0.074mm account for about 40%. The raw material particle size required by the boiling chlorination process is between 0.1mm and 0.25mm, that is, the existing artificial rutile cannot be produced by the existing boiling chlorination process to produce titanium tetrachloride

Method used

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  • The Process of Producing Titanium Tetrachloride Using Artificial Rutile in Fluidized Chlorination Furnace
  • The Process of Producing Titanium Tetrachloride Using Artificial Rutile in Fluidized Chlorination Furnace
  • The Process of Producing Titanium Tetrachloride Using Artificial Rutile in Fluidized Chlorination Furnace

Examples

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Effect test

Embodiment 1

[0082] The fluidized chlorination furnace 1 adopted in the present embodiment is a regenerated fluidized chlorination furnace 1 through a lining refractory material, and the fuel gas is coal gas.

[0083] Open the air pipe valve and gas pipe valve in turn, light the burner 112, control the temperature of the gas premixing chamber 105 at 100-150°C, control the ratio of air and gas at 4:1, and bake the fluidized chlorination furnace 1.

[0084] According to the requirement of lining refractory material of boiling chlorination furnace 1, adjust the gas flow rate and gradually increase the gas temperature. When the gas temperature exceeds 500°C, increase the opening of the air pipe valve and increase the air flow rate. The total air volume is controlled at 300Nm3 / h. Gradually open the feeding screw of feeding system 2, add petroleum coke to the petroleum coke feeding pipe, open the nitrogen gas supply pipe valve connected with the gas purging pipe 108, inject nitrogen into the gas ...

Embodiment 2

[0092] The fluidized chlorination furnace 1 used in this embodiment was interrupted due to equipment failure. After the failure was quickly eliminated, the temperature in the furnace was relatively high.

[0093] Open the air pipe valve and gas pipe valve in turn, light the burner 112, control the temperature of the gas premixing chamber 105 at 300-450°C, control the ratio of air and gas at 4:1, and quickly bake the fluidized chlorination furnace 1.

[0094] When the gas temperature exceeds 500°C, increase the opening of the air pipe valve, increase the air flow, control the total air volume at 300Nm3 / h, gradually open the feeding screw of the feeding system 2, add petroleum coke to the petroleum coke feeding pipe, open and blow the gas The sweeping pipe 108 is connected to the nitrogen gas supply pipe valve, inject nitrogen gas into the gas purging pipe 108, use nitrogen gas to purge the petroleum coke in the trumpet-shaped structure part of the petroleum coke feeding pipe, an...

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Abstract

The invention discloses a process for producing titanium tetrachloride in fluidizing chlorination furnace by using artificial rutile. The process includes five steps of: furnace baking, control of feeding, control of chlorination, tail gas slagging and cyclone dust collection. According to the process, the preparation of titanium tetrachloride by using the fine-sized artificial rutile is achieved, and meanwhile the collection and recycle of the artificial rutile in dust slag which is not completely reacted are also achieved.

Description

technical field [0001] The invention relates to the technical field of chemical metallurgy, in particular to a process for producing titanium tetrachloride in a fluidized chlorination furnace using artificial rutile. Background technique [0002] Boiling chlorination is the main process for producing titanium tetrachloride. It is to feed the mixture of titanium-containing material and petroleum coke into the reaction section of the boiling chlorination furnace through the feeding port set on the boiling chlorination furnace. It becomes a fluidized state, and at a temperature of 800-1000°C, chlorine gas and titanium raw materials undergo a chlorination reaction. [0003] Boiling chlorination furnace is the key equipment for boiling chlorination. Existing fluidized chlorination furnaces such as Figure 4 As shown, including the furnace body and the furnace chamber A1 surrounded by the furnace body, the furnace chamber A1 is divided into a settlement section A101, an expansio...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): C01G23/02
CPCC01G23/022
Inventor 叶恩东程晓哲缪辉俊张溅波张兴勇吴轩
Owner PANZHIHUA IRON & STEEL RES INST OF PANGANG GROUP
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