CN108440748A - A kind of high molecular weight carries the synthetic method of acyl fluorides group perfluoropolyether peroxide - Google Patents

A kind of high molecular weight carries the synthetic method of acyl fluorides group perfluoropolyether peroxide Download PDF

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CN108440748A
CN108440748A CN201810308980.XA CN201810308980A CN108440748A CN 108440748 A CN108440748 A CN 108440748A CN 201810308980 A CN201810308980 A CN 201810308980A CN 108440748 A CN108440748 A CN 108440748A
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molecular weight
synthetic method
high molecular
oxygen
peroxide
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CN108440748B (en
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吴庆
耿为利
郑磊
王宗令
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Zhejiang Chuangfu High Tech New Material Co ltd
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Zhejiang Juhua Co Ltd Technology Center
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    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08GMACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
    • C08G65/00Macromolecular compounds obtained by reactions forming an ether link in the main chain of the macromolecule
    • C08G65/002Macromolecular compounds obtained by reactions forming an ether link in the main chain of the macromolecule from unsaturated compounds
    • C08G65/005Macromolecular compounds obtained by reactions forming an ether link in the main chain of the macromolecule from unsaturated compounds containing halogens
    • C08G65/007Macromolecular compounds obtained by reactions forming an ether link in the main chain of the macromolecule from unsaturated compounds containing halogens containing fluorine

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  • Health & Medical Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
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  • Polyethers (AREA)
  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)

Abstract

The invention discloses the synthetic methods that a kind of high molecular weight carries acyl fluorides group perfluoropolyether peroxide, including:1) use element fluorine or Trifluoromethyl hypofluoride as the polymerisation of initiator in one or more of mixing of ozone, oxygen difluoride, the peroxide such as dichloroxide be added be used as auxiliary agent;2) use oxygen or liquid oxygen as raw material;3) for range of reaction temperature from 100 DEG C~30 DEG C, optimal is 100 DEG C~45 DEG C;4) for reaction pressure range from normal pressure~200KPa, optimal is normal pressure~100KPa.The present invention is by addition auxiliary agent, or changes the temperature for the oxygen being added, or changes process conditions and reach the content for improving high molecular weight perfluoropolyether intermediate product, achievees the purpose that reduction low molecular weight perfluoropolyether intermediates content.

Description

A kind of high molecular weight carries the synthetic method of acyl fluorides group perfluoropolyether peroxide
Technical field
The invention belongs to organic chemistry fileds, and in particular to a kind of high molecular weight carries acyl fluorides group perfluoropolyether peroxidating The synthetic method of object.
Background technology
It is mixed as initiator with Trifluoromethyl hypofluoride using fluorine gas, Trifluoromethyl hypofluoride, fluorine gas, at low temperature will Oxygen and perfluorinated monomers, the directly method of perfluoropolyether peroxide of the reaction synthesis with acyl fluorides group, in patent CN1049670A has been reported with foreign patent US5149842.
Using the synthetic method of above-mentioned patent report, obtained perfluoropolyether intermediate product (carries the peroxide of acyl fluorides group Compound) molecular weight distribution is from hundreds of to hundreds of thousands, and totally presentation low molecular weight (< 1000) and high molecular weight (> 10000) perfluoropolyether intermediates content is relatively low, intermediate molecular weight (3000~4000) perfluoropolyether intermediates content compared with High distribution situation.Since the price difference of the perfluoro polyether oil of different molecular weight is larger, the perfluor of especially high molecular weight is poly- Ether oil final price may be several times as much as the perfluoro polyether oil of low molecular weight.And the perfluoro polyether oil of intermediate molecular weight, especially in Between the perfluoro polyether oil of molecular weight demand is relatively low always in the market.
Although in USP4755330, describing and can be decomposed into the perfluoro polyether oil of higher molecular weight using catalyst The perfluoropolyether intermediate product of low molecular weight, but loss therein is larger, this method is simultaneously uneconomical.It is needed to adapt to market It asks, rate of guaranteeing the profit, it is necessary to find a kind of suitable synthetic method, in the product that can make synthesis, be worth higher high score Son amount product assay rises, and is worth the content of lower low molecular weight product and reduces.
Invention content
Present invention aims at provide a kind of high molecular weight for deficiency of the prior art to carry acyl fluorides group The technical solution of the synthetic method of perfluoropolyether peroxide, by adding auxiliary agent, or the temperature of the oxygen of change addition, or change Process conditions reach the content for improving high molecular weight perfluoropolyether intermediate product, and reaching reduces production among low molecular weight perfluoropolyether The purpose of object content.
In order to solve the above-mentioned technical problem, the technical solution adopted by the present invention is that a kind of high molecular weight is complete with acyl fluorides group The synthetic method of perfluoroalkyl polyether peroxide, it is characterised in that:
The synthetic method is that oxygen is directly synthesized to the perfluor with acyl fluorides group with perfluorinated monomers with auxiliary agent using initiator Polyethers peroxide.
Further, auxiliary agent is the mixing of one or more of ozone, oxygen difluoride, dichloroxide or peroxide Object.
Further, the ratio of the addition of the addition and initiator of auxiliary agent is (0.01~1):1.
Further, oxygen includes cryogenic oxygen or liquid oxygen, be added oxygen temperature be -100 DEG C~-30 DEG C, optimum temperature be - 100 DEG C~-50 DEG C, oxygen is added jointly after being mixed with initiator (fluorine gas, Trifluoromethyl hypofluoride), auxiliary agent, can also Oxygen, initiator, auxiliary agent are separately added into, and the addition of liquid oxygen can not only participate in reacting, and additionally aid controlling reaction temperature, significantly Reduce the demand of refrigerant in reaction process.
Further, the range of reaction temperature of synthetic method is -100 DEG C~-30 DEG C.
After it is preferred that, the range of reaction temperature of synthetic method is -100 DEG C~-45 DEG C.
Further, the reaction pressure of synthetic method ranging from normal pressure~200KPa.
After it is preferred that, reaction pressure ranging from normal pressure~150KPa of synthetic method.
One or more of mixing of the peroxide such as ozone, oxygen difluoride, dichloroxide are included by being added in the reaction Object can effectively improve the content of high molecular weight perfluoropolyether intermediate product as auxiliary agent, while can also reduce low molecule Measure the content of perfluoropolyether intermediate product.In addition, reduce be added oxygen temperature can also effectively be reduced even with liquid oxygen it is low The content of molecular weight perfluoropolyether intermediate product improves the content of high molecular weight perfluoropolyether intermediate product.Reduction reaction temperature, The content of high molecular weight perfluoropolyether intermediate product can be improved by improving reaction pressure, be reduced among low molecular weight perfluoropolyether Product assay.
The present invention is by adopting the above-described technical solution, have the advantages that:
(1) it is not necessarily to the change of original process equipment, you can implement, method is easy, with obvious effects.
(2) use cryogenic oxygen or liquid oxygen can effective controlling reaction temperature, reduce the demand of refrigerant, reduce energy Consumption.
The present invention provides a kind of technologies of synthetic method of high molecular weight with acyl fluorides group perfluoropolyether peroxide Scheme by addition auxiliary agent, or changes the temperature for the oxygen being added, or changes process conditions and reach raising high molecular weight perfluoropolyether The content of intermediate product achievees the purpose that reduce low molecular weight perfluoropolyether intermediates content.
Description of the drawings
The invention will be further described below in conjunction with the accompanying drawings:
Fig. 1 is infrared point in synthetic method of kind of the high molecular weight with acyl fluorides group perfluoropolyether peroxide of the invention Analyse result;
Fig. 2 is GPC measurement results in the present invention;
Fig. 3 is that nuclear-magnetism fluorine is composed in the present invention.
Specific implementation mode
A kind of high molecular weight of the present invention carries the synthetic method of acyl fluorides group perfluoropolyether peroxide:
This method is that oxygen is directly synthesized to the perfluoropolyether with acyl fluorides group with perfluorinated monomers with auxiliary agent using initiator Peroxide, auxiliary agent are the mixture of one or more of ozone, oxygen difluoride, dichloroxide or peroxide, are helped The ratio of the addition of agent and the addition of initiator is 0.01~1:1, oxygen includes oxygen or liquid oxygen, be added oxygen temperature be- 100 DEG C~-30 DEG C, most preferably -100 DEG C~-50 DEG C, oxygen can be mixed with initiator (fluorine gas, Trifluoromethyl hypofluoride), auxiliary agent Be added jointly after conjunction, can also oxygen, initiator, auxiliary agent be separately added into, the addition of liquid oxygen can not only participate in reacting, and also help In controlling reaction temperature, the demand of refrigerant in reaction process is greatly reduced, the range of reaction temperature of reaction is -100 DEG C~- 30 DEG C, reaction temperature is preferably -100 DEG C~-45 DEG C, and reaction pressure ranging from normal pressure~200KPa, the reaction pressure of reaction are excellent It is selected as normal pressure~150KPa.
The present invention is further explained below by specific embodiment, these embodiments are only used for the purpose of illustration, It is not intended to limit protection scope of the present invention.
Embodiment 1
200g hexafluoropropenes are condensed in the stainless steel cauldron of band stirring jacketed of a 0.5L volume, stainless steel Reaction kettle top connection stainless steel condenser has the air inlet for being inserted into bottom for condensing hexafluoropropene inside stainless steel cauldron Pipe.Refrigerant is passed through in stainless steel cauldron chuck, maintaining reaction temperature is less than -55 DEG C always.Stirring is started, is divided in 2.5h - 80 DEG C of anhydrous oxygen is not passed through with the speed of 2L/h, Trifluoromethyl hypofluoride (CF is added in the speed of 2.5L/h3OF), The fluorine nitrogen mixed gas that concentration of fluorine is 20% (V%) is added in the speed of 0.7L/h, and ozone is added in the speed of 0.28L/h, and control is anti- It is normal pressure to answer pressure.After reaction, unreacted hexafluoropropene and reaction product are distilled, obtains 85 grams of thick production Product, crude product are the sticky oil bodies of water white transparency.
Crude product carries out infrared analysis, and with iodometric analysis, chemistry titration measures number-average molecular weight, molecule is measured by GPC Amount distribution, is composed by nuclear-magnetism fluorine and determines its structure.
Infrared analysis is the results detailed in Figure of description 1.
Characteristic absorption peak position (cm-1) Judge result
1897.70 Acyl fluorides
1780.95 Carboxylic acid
1150-1030 Alkyl peroxide there may be
Chemistry titration determination data:
Iodometric determination active o content is 0.85%;
By chemistry titration, the number-average molecular weight for measuring product is 6500.
GPC measurement results refer to Figure of description 2.
It is calculated by area normalization, average molecular weight is about 6800.
Nuclear-magnetism fluorine spectrum refers to Figure of description 3.
Nuclear-magnetism determines that its structural formula is:CF3O-(CF(CF3)CF2O)m-(CF2O)n-(CFO(CF3))P- COF,19F-NMR In collection of illustrative plates, the signal expression at the places chemical shift -146ppm-is-(CF (CF3)CF2O-CF- the groups in), the places -131ppm That signal indicates is-(CFO (CF3)) in-CF- groups, -55ppm place signal indicate be-(CF2O-CF in)2Group ,- That the signal at 57ppm indicates is CF3CF in O-3Group, the signal expression at the places -81~-82ppm is-(CF (CF3) CF2O CF in)3And CF2Group.
Example 2-10
Change experimental condition in the reaction unit of example 1, is reacted using 200g hexafluoropropenes, reaction time 2.5h, reaction Condition see the table below:
By nuclear-magnetism and infrared detection after reaction, determine that its structure is consistent with the product that example 1 obtains, reaction result is seen below Table:
Peroxide content (%) Number-average molecular weight GPC measures average molecular weight Product quality (g)
Example 1 0.85 6500 6800 85
Example 2 0.91 7300 7500 87
Example 3 1.21 8500 8600 88
Example 4 1.33 8800 8900 87
Example 5 1.41 8800 9000 88
Example 6 1.44 8900 9200 88
Example 7 1.44 9000 9200 88
Example 8 1.52 9500 9500 87
Example 9 1.56 9800 9800 89
Example 10 1.65 10000 10000 88
As can be seen from the results, the average molecular weight of product obviously rises, and GPC, which is measured, finds high molecular weight product content Rise apparent.
Example 11-20
Change experimental condition in the reaction unit of example 1, reacted with 100g tetrafluoroethene using 100g hexafluoropropenes, Reaction time 2.5h, reaction condition see the table below:
Reaction result see the table below:
Peroxide content (%) Number-average molecular weight GPC measures average molecular weight Product quality (g)
Example 11 1.41 8800 9000 88
Example 12 1.44 8900 9200 89
Example 13 1.44 9000 9200 90
Example 14 1.52 9500 9500 90
Example 15 1.56 9800 9800 89
Example 16 1.65 10000 10000 89
Example 17 1.73 12000 12000 89
Example 18 1.72 12000 12000 90
Example 19 1.75 12000 12000 90
Example 20 1.77 12000 12000 90
The average molecular weight of product rises obviously, while GPC measures high molecular weight product content in product and rises obviously.
Example 21-23
Change experimental condition in the reaction unit of example 1, solvent, 100g tetrafluoro second are done using 100g Freon 13s Alkene is reacted, and reaction time 1.5h, reaction condition see the table below:
Reaction result see the table below:
Peroxide content (%) Number-average molecular weight GPC measures average molecular weight Product quality (g)
Example 21 1.81 13000 13000 67
Example 22 1.84 13000 13000 67
Example 23 1.84 14000 14000 69
The present invention provides a kind of technologies of synthetic method of high molecular weight with acyl fluorides group perfluoropolyether peroxide Scheme by addition auxiliary agent, or changes the temperature for the oxygen being added, or changes process conditions and reach raising high molecular weight perfluoropolyether The content of intermediate product achievees the purpose that reduce low molecular weight perfluoropolyether intermediates content.
It these are only specific embodiments of the present invention, but the technical characteristic of the present invention is not limited thereto.It is any with this hair Based on bright, for the technique effect for realizing essentially identical, made ground simple change, equivalent replacement or modification etc. are all covered Among protection scope of the present invention.

Claims (8)

1. a kind of high molecular weight carries the synthetic method of acyl fluorides group perfluoropolyether peroxide, it is characterised in that:
The synthetic method is that oxygen is directly synthesized to the perfluoropolyether with acyl fluorides group with perfluorinated monomers with auxiliary agent using initiator Peroxide.
2. a kind of high molecular weight according to claim 1 carries the synthetic method of acyl fluorides group perfluoropolyether peroxide, It is characterized in that:The auxiliary agent is the mixing of one or more of ozone, oxygen difluoride, dichloroxide or peroxide Object.
3. a kind of high molecular weight according to claim 1 carries the synthetic method of acyl fluorides group perfluoropolyether peroxide, It is characterized in that:The ratio of the addition of the auxiliary agent and the addition of the initiator is (0.01~1):1.
4. a kind of high molecular weight according to claim 1 carries the synthetic method of acyl fluorides group perfluoropolyether peroxide, It is characterized in that:The oxygen includes oxygen or liquid oxygen.
5. a kind of high molecular weight according to claim 1 carries the synthetic method of acyl fluorides group perfluoropolyether peroxide, It is characterized in that:The range of reaction temperature of the synthetic method is -100 DEG C~-30 DEG C.
6. a kind of high molecular weight according to claim 5 carries the synthetic method of acyl fluorides group perfluoropolyether peroxide, It is characterized in that:The range of reaction temperature of the synthetic method is -100 DEG C~-45 DEG C.
7. a kind of high molecular weight according to claim 1 carries the synthetic method of acyl fluorides group perfluoropolyether peroxide, It is characterized in that:The reaction pressure of the synthetic method ranging from normal pressure~200KPa.
8. a kind of high molecular weight according to claim 7 carries the synthetic method of acyl fluorides group perfluoropolyether peroxide, It is characterized in that:The reaction pressure of the synthetic method ranging from normal pressure~150KPa.
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Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN109384911A (en) * 2018-11-15 2019-02-26 四川科源精诚新材料科技有限公司 A kind of perfluorinated surfactant and preparation method thereof
CN112159506A (en) * 2020-08-19 2021-01-01 浙江巨化技术中心有限公司 Preparation method of multi-anchor brush-shaped perfluoropolyether anti-fingerprint agent
CN114395117A (en) * 2021-12-31 2022-04-26 西安近代化学研究所 Double-end perfluoropolyether and preparation method thereof

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CN1047313A (en) * 1989-04-20 1990-11-28 奥西蒙特公司 The method for preparing peroxide perfluoropolyethers
CN1167124A (en) * 1996-02-14 1997-12-10 奥西蒙特公司 Process for preparing peroxidic perfluoropolyoxyalkylenes
US10029981B2 (en) * 2015-12-10 2018-07-24 Daikin Industries, Ltd. Process for producing perfluoropolyoxyalkylene peroxide compound

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Publication number Priority date Publication date Assignee Title
CN1047313A (en) * 1989-04-20 1990-11-28 奥西蒙特公司 The method for preparing peroxide perfluoropolyethers
CN1049670A (en) * 1989-04-20 1991-03-06 奥西蒙特公司 The method for preparing peroxide perfluoropolyethers
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Cited By (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN109384911A (en) * 2018-11-15 2019-02-26 四川科源精诚新材料科技有限公司 A kind of perfluorinated surfactant and preparation method thereof
CN109384911B (en) * 2018-11-15 2019-08-27 四川科源精诚新材料科技有限公司 A kind of perfluorinated surfactant and preparation method thereof
EP3872115A4 (en) * 2018-11-15 2022-01-05 Inner Mongolia Huansheng Technology Co., Ltd. Perfluoro surfactant and preparation method therefor
CN112159506A (en) * 2020-08-19 2021-01-01 浙江巨化技术中心有限公司 Preparation method of multi-anchor brush-shaped perfluoropolyether anti-fingerprint agent
CN112159506B (en) * 2020-08-19 2023-01-10 浙江巨化技术中心有限公司 Preparation method of multi-anchor brush-shaped perfluoropolyether anti-fingerprint agent
CN114395117A (en) * 2021-12-31 2022-04-26 西安近代化学研究所 Double-end perfluoropolyether and preparation method thereof
CN114395117B (en) * 2021-12-31 2023-10-20 西安近代化学研究所 Double-end perfluoropolyether and preparation method thereof

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