Technology for fluorinating unstable end group of perfluoropolyether

A perfluoropolyether, chemical process technology, applied in the field of fluorine chemical industry, can solve the problems of insufficient gas-liquid contact, increase the amount of exhaust gas, unfavorable environmental protection, etc. The effect of utilization efficiency

Active Publication Date: 2019-08-06
SHANGHAI OULEIFEN BIOLOGICAL TECH
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0004] At present, there are two main methods for fluorinating the unstable terminal groups of perfluoropolyether, one is to use AlF 3 , SbF 5 High-temperature fluorination of solid fluorinating agents such as solid fluorinating agents, but the price of fluorinating agents used in this method is relatively high, and the separation of products is difficult, and the metal ions in it are difficult to remove completely, which will greatly affect product quality; The end group fluorination of fluoropolyether, the product obtained by this method is pure, and the post-treatment is simple, but due to the low solubility of fluorine gas in the reactant, it is difficult to fully react with the active end group of perfluoropolyether, and the currently existing For example, fluorination reaction equipment such as reactors have the disadvantages of insufficient gas-liquid contact and low utilization rate of fluorinating agent. A large excess of fluorine gas is required, and the general dosage needs to be more than ten times the theoretical value, and a longer reaction time is required. , the overall reaction efficiency is low, the reaction cost is high, and the tail gas treatment capacity is increased, which is not conducive to environmental protection

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  • Technology for fluorinating unstable end group of perfluoropolyether

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Effect test

Embodiment 1

[0052] Embodiment 1 provides a fluorination process for unstable terminal groups of perfluoropolyether, wherein the bubble column fluorination reactor used has a diameter of 20 cm and a height of 250 cm, and pumps 50 L of perfluoropolyether with a number average molecular weight of 5200 Da Ether acid fluoride raw material, and then the reactor is heated to 150°C, the circulation pump is turned on to circulate the material in the reactor, and the pressure of the back pressure valve is set to 0.5MPa. Open the fluorine gas valve, feed in a mixed gas of fluorine gas and nitrogen with a mass concentration of 50% fluorine gas, control the flow rate at 1.5g / min, and after ventilating for one hour, adjust the heating device of the bubble tower fluorination reactor to raise the temperature to 230°C and keep it for 24 hours Finally, stop feeding the mixed gas, turn off the heating, and feed nitrogen for purging. After the temperature drops to 40°C, stop nitrogen purging, open the discha...

Embodiment 2

[0054] Embodiment 2 provides a fluorination process for unstable terminal groups of perfluoropolyether, wherein the bubble column fluorination reactor used has a diameter of 20 cm and a height of 250 cm, and 50 L of perfluoropolyether with a number average molecular weight of 5200 Da Ether acid fluoride raw material, and then the reactor is heated to 150°C, the circulation pump is turned on to circulate the material in the reactor, and the pressure of the back pressure valve is set to 0.5MPa. Open the fluorine gas valve, feed in a mixed gas of fluorine gas and nitrogen with a mass concentration of 50% fluorine gas, control the flow rate at 1.5g / min, and after ventilating for one hour, adjust the heating device of the bubble tower fluorination reactor to raise the temperature to 230°C and keep it for 24 hours Finally, stop feeding the mixed gas, turn off the heating, and feed nitrogen for purging. After the temperature drops to 40°C, stop nitrogen purging, open the discharge va...

Embodiment 3

[0056] Embodiment 3 provides a kind of fluorination process of perfluoropolyether unstable end group, wherein the bubble column fluorination reaction equipment adopted is the same as that of embodiment 1, and the specific process includes pumping 50L of fluoride with a number average molecular weight of 3300Da after vacuuming. Perfluoropolyether acid raw material, and then the reactor is heated to 150°C, the circulation pump is turned on to circulate the material in the reactor, and the pressure of the back pressure valve is set to 0.5MPa. Open the fluorine gas valve, feed in a mixed gas of fluorine gas and nitrogen with a mass concentration of 50% fluorine gas, control the flow rate at 2.5g / min, and after ventilating for one hour, adjust the heating device of the bubble column fluorination reactor to raise the temperature to 255°C and keep it for 24 hours Afterwards, stop feeding fluorine gas, turn off the heating, and feed nitrogen gas for purging. After the temperature drop...

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Abstract

The invention relates to the technical field of fluorine chemical, and concretely relates to a technology for fluorinating the unstable end group of perfluoropolyether. The technology comprises the following steps: 1, vacuumizing a bubble tower fluorination reactor, adding an HFPO oligomer acid fluoride and / or perfluoropolyether carboxylic acid into the reactor from the upper end of the bubble tower fluorination reactor, and heating the bubble tower fluorination reactor to 130-170 DEG C; 2, adjusting the pressure in the bubble tower fluorination reactor; 3, introducing a fluorinating agent gas, carrying out a reaction for 45-90 min, and heating the reactor to a preset reaction temperature; and 4, carrying out a reaction for 4-48 h, stopping the introduction of the raw material when the reaction is finished, carrying out nitrogen purging, cooling the obtained material to 40 DEG C or below, and discharging the cooled material. The end group of the HFPO oligomer acid fluoride and / or perfluoropolyether carboxylic acid is treated with fluorine gas by using the bubble tower fluorination reactor, so the utilization efficiency of the fluorine gas is greatly improved, and an ideal effect isachieved.

Description

technical field [0001] The invention relates to the technical field of fluorine chemical industry, in particular to a fluorination process for unstable terminal groups of perfluoropolyether. Background technique [0002] Perfluoropolyether has excellent high and low temperature stability, low surface tension, chemical inertness, non-flammability, low volatility, good lubricity, water and solvent resistance, excellent radiation stability, compatibility with metal plastic elastomers, With high dielectric properties, non-toxicity and excellent viscosity-temperature characteristics, it is widely used as high-vacuum pump oil, lubricant, insulating fluid, heat transfer fluid and cooling fluid in the fields of electronics, military industry, nuclear energy, and high-end equipment. [0003] The currently marketed perfluoropolyethers mainly include K-type prepared by ring-opening polymerization of hexafluoropropylene oxide, Y-type prepared by oxygen oxidation of hexafluoropropylene, ...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C08G65/323
CPCC08G65/3236
Inventor 栾英豪李福清杜文朝刘晨斌戴力
Owner SHANGHAI OULEIFEN BIOLOGICAL TECH
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