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Continuous production method of phosphorus pentafluoride

A technology of phosphorus pentafluoride and production method, applied in phosphorus halide/oxyhalide and other directions, can solve the problems of uncontrolled reaction, fluctuation of reaction rate, high safety risk, etc., to avoid explosion accidents, stable reaction process, and easy reaction control. Effect

Inactive Publication Date: 2018-12-21
SICHUAN UNIV
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

Since this method uses solid phosphorus as a raw material, and solid yellow phosphorus is particles with different surface areas, the contact area between yellow phosphorus and fluorine gas fed into the reactor at different times cannot be kept consistent, resulting in large fluctuations in the reaction rate, which is not conducive to Stable and accurate control of the reaction rate. Since the reaction between yellow phosphorus and fluorine gas will release a large amount of heat, when the reaction rate fluctuates greatly, it is easy to cause an explosion accident due to a reaction out of control, and the safety risk is greater

Method used

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  • Continuous production method of phosphorus pentafluoride
  • Continuous production method of phosphorus pentafluoride

Examples

Experimental program
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Effect test

Embodiment 1

[0027] like figure 1 and figure 2 As shown, the vertical continuous production equipment for phosphorus pentafluoride is used for continuous production of phosphorus pentafluoride. The gas port 2, the side wall of the vertical reaction vessel 1 below the gas port 2 is provided with an atomizing nozzle 3, and the outlet of the atomizing nozzle 3 faces downward.

[0028] Use heating equipment to heat the solid yellow phosphorus into a liquid state for later use, and use an air pump to transport the inert gas from the inert gas inlet pipe 5 to the inlet nozzle 8, and the inert gas enters the vertical reaction vessel 1 after passing through the inert gas flow channel 7 and the vent hole 11, All the air in the vertical reaction vessel 1 is squeezed out. Then use the delivery pump to transport the liquid yellow phosphorus to the atomizing nozzle 3. The liquid yellow phosphorus is atomized by the atomizing nozzle 3 to form a phosphorus spray and then flow downward. The spray speed...

Embodiment 2

[0030] The equipment described in Example 1 was used to continuously produce phosphorus pentafluoride, and some parameters were changed, wherein, the spraying speed of phosphorus spray was 1 m / s; the temperature was 250°C. Adjust the distance between the nozzle of phosphorus spray and the nozzle of fluorine-containing gas to 15m, and the ejection speed of the mixed gas of fluorine gas and inert gas to 5m / s; through monitoring, it can be seen that the reaction temperature of this process is 250-500°C Fluctuation, the reaction pressure fluctuates within 0.1-0.5MPa, the temperature and pressure fluctuations are small, and the reaction proceeds smoothly.

Embodiment 3

[0032] The equipment described in Example 1 was used to continuously produce phosphorus pentafluoride, and some parameters were changed, wherein, the spraying speed of phosphorus spray was 10 m / s; the temperature was 150°C. Adjust the distance between the nozzle of the phosphorus spray and the nozzle of the fluorine-containing gas to be 10m. During the reaction, no inert gas is passed into but only fluorine gas (that is, the fluorine-containing gas is fluorine gas), and the ejection speed of the fluorine gas is 15m / s; It can be seen from the monitoring that with this process, the reaction temperature fluctuates at 250-500° C., the reaction pressure fluctuates at 0.1-0.5 MPa, the temperature and pressure fluctuations are small, and the reaction proceeds smoothly.

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Abstract

The invention relates to a continuous production method of phosphorus pentafluoride, and belongs to the technical field of preparation of the phosphorus pentafluoride. The invention aims to provide the continuous production method of the phosphorus pentafluoride. According to the continuous production method, under the protection of an inert gas, liquid yellow phosphorus is atomized and sprayed according to a spraying method, and the sprayed phosphorus spray reacts with fluorine-containing gas through reverse contact to obtain the phosphorus pentafluoride, wherein the fluorine-containing gas is gas containing fluorine gas. According to the continuous production method, through continuous spraying of the phosphorus spray and reaction of the phosphorus spray and the fluorine gas, the phosphorus pentafluoride can be continuously prepared; the conventional gas-solid reaction of the fluorine gas and the phosphorus is changed into an gas-gas reaction, and the reaction thereof is easy to control; through control of the gas flow, the speed rate can be controlled to achieve the purpose of controlling reaction heat, so that the whole reaction process is stable, an explosion accident causedby violent reaction is avoided and safety risks are reduced.

Description

technical field [0001] The invention relates to a continuous production method of phosphorus pentafluoride, belonging to the technical field of phosphorus pentafluoride preparation. Background technique [0002] Phosphorus pentafluoride is an important inorganic fluoride, which can be used in the electronics industry, polymer materials and organic synthesis catalysts. In recent years, with the development of lithium batteries, phosphorus pentafluoride is an important raw material for the production of lithium hexafluorophosphate electrolyte materials for lithium batteries, and its demand and quality requirements are also increasing. Therefore, large-scale continuous production of phosphorus pentafluoride is of great significance . [0003] At present, there are two main processes for industrialized production of high-purity phosphorus pentafluoride, one is to use phosphorus pentachloride to react with hydrogen fluoride to generate phosphorus pentafluoride and hydrogen chlor...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C01B25/10
CPCC01B25/10
Inventor 杨林张攀张志业王辛龙孔行健
Owner SICHUAN UNIV
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