Separation method and device of zirconium tetrachloride synthesis gas

A technology of zirconium tetrachloride and separation method, applied in chemical instruments and methods, zirconium halide, zirconium compounds, etc., can solve the problems of energy consumption, complex separation process of zirconium tetrachloride synthesis gas, etc. The effect of reducing separation costs

Active Publication Date: 2018-12-18
XINTE ENERGY +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

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Problems solved by technology

[0003] The technical problem to be solved by the present invention is to provide a separation method and device for zirconium tetrachloride synthesis gas in view of the above-mentioned deficiencies in the prior art, which solves the complicated separation process of zirconium tetrachloride synthesis gas in the prior art. , Technical issues of energy-consuming manuscripts

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  • Separation method and device of zirconium tetrachloride synthesis gas

Examples

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Embodiment 1

[0044]This embodiment provides a method for separating zirconium tetrachloride synthesis gas. The zirconium tetrachloride synthesis gas is obtained by preparing zirconium tetrachloride by a chlorination method, including the following steps:

[0045] 1) cooling the zirconium tetrachloride synthesis gas to 150-180°C, and depositing the first crude zirconium tetrachloride to obtain the first synthesis gas;

[0046] 2) Lowering the temperature of the first synthesis gas to 80-120° C. to precipitate the second crude zirconium tetrachloride to obtain the second synthesis gas.

[0047] The present embodiment provides a kind of device used in the separation method of above-mentioned zirconium tetrachloride synthesis gas, comprising:

[0048] The first cooling separator is used to lower the temperature of the zirconium tetrachloride synthesis gas to 150-180°C, and precipitate the first crude zirconium tetrachloride to obtain the first synthesis gas;

[0049] The second cooling separa...

Embodiment 2

[0052] Such as figure 1 As shown, the present embodiment provides a device for the separation method of zirconium tetrachloride synthesis gas, including:

[0053] The first cooling separator 1 is used to lower the temperature of the zirconium tetrachloride synthesis gas and precipitate the first crude zirconium tetrachloride to obtain the first synthesis gas;

[0054] The second cooling separator 2 is connected with the first cooling separator 1 , and the second cooling separator 2 is used to lower the temperature of the first synthesis gas to precipitate the second crude zirconium tetrachloride to obtain the second synthesis gas.

[0055] The vacuum settler 3 is connected to the second cooling separator 2, and the vacuum settler 3 is used to vacuum settle the second synthesis gas to obtain the separated third synthesis gas and sedimentation precipitate;

[0056] The dryer 4 is connected with the vacuum precipitator 3, and the dryer 4 is used to heat the sediment to obtain th...

Embodiment 3

[0083] This example provides a method for separating zirconium tetrachloride synthesis gas using the device in Example 2. The zirconium tetrachloride synthesis gas is obtained by preparing zirconium tetrachloride through the chlorination method. The difference from the method in Example 2 for:

[0084] 1) In the first cooling separator 1, the temperature of the zirconium tetrachloride synthesis gas from the chlorination reactor is lowered to 180°C.

[0085] 2) In the second cooling separator 2, the temperature of the first syngas is lowered to 100°C.

[0086] 3) The second synthesis gas is settled in vacuum in the vacuum settler 3, the vacuum degree of the vacuum settling is 50000 Pa, and the temperature is 55°C.

[0087] 4) Cool down to 25° C. by eluting with silicon tetrachloride eluent.

[0088] 5) The temperature of the fifth synthesis gas is lowered to -25° C. in the cooler 6 .

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Abstract

The invention discloses a separation method of zirconium tetrachloride synthesis gas. The zirconium tetrachloride synthesis gas is prepared from zirconium tetrachloride by a chlorination method. The method comprises the following steps of (1) lowering the temperature of the zirconium tetrachloride synthesis gas to 150 to 180 DEG C; separating out first coarse zirconium tetrachloride to obtain first synthesis gas; (2) lowering the temperature of the first synthesis gas to 80 to 120 DEG C; separating out second coarse zirconium tetrachloride to obtain second synthesis gas. The separation methodand device of zirconium tetrachloride synthesis gas provided by the method have the advantages that according to the method, the first coarse zirconium tetrachloride and the second coarse zirconium tetrachloride are respectively cooled and separated through stepped temperature reduction; the first coarse zirconium tetrachloride and the second coarse zirconium tetrachloride can be respectively usedas a coarse product to be used; the temperature used for separating out the first coarse zirconium tetrachloride through temperature reduction is lower; most zirconium tetrachloride in the zirconiumtetrachloride synthesis gasis separated out; the cold quantity is greatly saved; the separation cost of the zirconium tetrachloride synthesis gas is reduced.

Description

technical field [0001] The invention belongs to the technical field of zirconium tetrachloride preparation, and in particular relates to a method and a device for separating zirconium tetrachloride synthesis gas. Background technique [0002] The boiling chlorination method is the most potential zirconium tetrachloride production process, which has the advantages of high product quality, low production cost and high utilization rate of raw materials. The boiling chlorination method uses a mixture of zircon sand, reducing agent and chemical heat supplement to react in a fluidized bed reactor to prepare zirconium tetrachloride, and at the same time by-produce silicon tetrachloride. The reducing agent includes charcoal, petroleum coke, Coal powder, etc., chemical heat supplements include silicon powder, ferrosilicon, silicon carbide, etc. The composition of the zirconium tetrachloride synthesis gas produced by the chlorination method is very complex, not only the separation pr...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C01G25/04C01G25/00C01B33/107C01B33/12C01B7/03C01B11/06C01D3/04C01B32/40
CPCC01B7/035C01B11/062C01B33/10721C01B33/10778C01B33/12C01D3/04C01G25/00C01G25/04C01P2006/80C01B32/40
Inventor 武珠峰银波范协诚黄彬张伟刘兴平
Owner XINTE ENERGY
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