CN111138275B - Perfluoroalkyl diacyl fluoride and preparation method thereof - Google Patents
Perfluoroalkyl diacyl fluoride and preparation method thereof Download PDFInfo
- Publication number
- CN111138275B CN111138275B CN201911404655.4A CN201911404655A CN111138275B CN 111138275 B CN111138275 B CN 111138275B CN 201911404655 A CN201911404655 A CN 201911404655A CN 111138275 B CN111138275 B CN 111138275B
- Authority
- CN
- China
- Prior art keywords
- cyclic olefin
- perfluoroalkyl
- activation
- fluoride
- catalyst
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Active
Links
Classifications
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C51/00—Preparation of carboxylic acids or their salts, halides or anhydrides
- C07C51/58—Preparation of carboxylic acid halides
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C55/00—Saturated compounds having more than one carboxyl group bound to acyclic carbon atoms
- C07C55/36—Acyl halides
- C07C55/40—Acyl halides containing halogen outside the carboxyl halide group
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Engineering & Computer Science (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
Abstract
The present invention belongs to the field of fluorine chemical industryCyclic olefin is pre-activated in an activation chamber and then enters a cracking chamber to react with oxygen under the condition of a catalyst to generate the perfluoro diacyl fluoride through catalytic cracking, wherein n is an integer from 1 to 5, and Rf is an integer from 1 to 51Rf2, Rf3, Rf4, Rf5 and Rf6 are respectively one of fluoro, perfluoroalkyl and perfluoroalkyl ether. In the method, cyclic olefin is used as a raw material, and catalytic cracking is carried out under oxygen atmosphere after catalytic pre-activation by ozone, so that the cyclic olefin can almost completely react without loss, the yield is high, and the controllability is strong.
Description
Technical Field
The invention belongs to the field of fluorine chemical industry, and particularly relates to perfluoroalkyl diacyl fluoride and a preparation method thereof.
Background
The diacyl fluorine hexafluoropropylene oxide polymer is a fluorine-containing organic intermediate with wide application, can be hydrolyzed, aminolyzed and alcoholyzed by utilizing the reactivity of a terminal-COF group to further synthesize fluorine-containing polyester, polyamide, polyepoxy resin, fluorosilicone resin and various compounds with polymerizable vinyl fluoride, and therefore has important development value in the fluorine-containing fine chemical engineering field.
Disclosure of Invention
The invention aims to provide perfluoroalkyl diacyl fluoride and a preparation method thereof.
In order to realize the purpose, the invention adopts the following technical scheme:
a preparation method of perfluoroalkyl diacyl fluoride comprises the steps of pre-activating cyclic olefin in an activation chamber, then allowing the cyclic olefin to enter a cracking chamber to react with oxygen under the condition of a catalyst, and catalytically cracking the cyclic olefin to generate the perfluoroalkyl diacyl fluoride, wherein the reaction formula (I) is as shown in the specification:
wherein n is an integer of 1 to 5, Rf1Rf2 and Rf3 are respectively one of fluoro, perfluoroalkyl and perfluoroalkyl ether.
Preferably, n is 1, Rf1Rf2 and Rf3 are all fluorine groups.
The pre-activation method comprises the specific steps of introducing cyclic olefin into an activation chamber, filling metal oxide into the activation chamber, introducing O3, and performing activation under the condition of light irradiation; the light irradiation time was: 10-90min, and the reaction temperature is-10-20 ℃.
The metal oxide is one of TiO2, Fe2O3, Fe3O4, CoO, Co3O4, Ag2O and Pd 2O.
The cracking process takes oxygen and activated cyclic olefin as raw materials, and the cyclic olefin is prepared by reaction under the action of a catalyst; wherein the molar ratio of oxygen to the cyclic olefin is 20:1-1: 10; the contact reaction time is 0.1s to 200 s; the reaction pressure is 0-1 MPa; the reaction temperature is 200-700 ℃.
The catalyst is a supported catalyst, and the active component is one or a mixture of more of AgO, Al2O3, CuO, AgF, NaF, KF, RbF and CsF.
The application also comprises perfluoroalkyl diacyl fluoride obtained by the preparation method.
Compared with the prior art, the invention has the beneficial effects that:
in the method, cyclic olefin is used as a raw material, and catalytic cracking is carried out under oxygen atmosphere after catalytic pre-activation by ozone, so that the cyclic olefin can almost completely react without loss, the yield is high, and the controllability is strong.
Detailed Description
In order to make the technical solutions of the present invention better understood by those skilled in the art, the present invention will be further described in detail with reference to the following preferred embodiments.
Example 1: ozone is led into an activation chamber with an ozone irradiation lamp arranged at the upper part, a temperature-controllable material storage tank is arranged in the activation chamber, a vertical irradiation mode is adopted during irradiation, namely the direction of a particle beam is vertical to the surface of liquid, metal oxide is arranged in the material storage tank, the raw material perfluorocyclopentene is added, the reaction temperature is controlled to be-10-20 ℃, the irradiation time is 10-90min, a liquid discharge valve at the bottom of the material storage tank is opened after irradiation is finished, the activated perfluorocyclopentene is put into a vaporization chamber to be slowly vaporized, and the temperature rise process of the vaporization chamber adopts the programmed temperature rise: keeping the temperature at 20 ℃ for 5-10min, and then increasing the temperature to 30-40 ℃ at the speed of 0.5-1 ℃/min. The gasified raw material enters a cracking chamber to be heated and cracked in the presence of oxygen, and the feeding molar ratio of the gasified raw material to the oxygen is controlled to be 20:1-1:10 by a gas flow meter in the cracking process. The contact reaction time is 0.1s to 200 s; the reaction pressure is 0-1 MPa; the reaction temperature is 200-700 ℃. And (3) the product obtained after cracking firstly enters a cold trap at 30 ℃ for collecting the diacyl fluoride generated by cracking, and the obtained diacyl fluoride is rectified and purified to obtain a high-purity diacyl fluoride product, wherein the parameters and the yield of different embodiments are shown in table 1.
Comparative example 1: the comparative example differs from example 2 only in that perfluorocyclopentene was added directly to the cracking chamber without pre-activation to react with oxygen.
TABLE 1
Example 1 | Example 2 | Example 3 | Example 4 | Comparative example 1 | |
Metal oxides | TiO2 | Ag2O | TiO2 | Ag2O | / |
Catalyst and process for preparing same | NaF | NaF | KF | KF | NaF |
Perfluoro cyclopentene: oxygen gas | 20:1 | 1:1 | 1:1 | 1:10 | 1:1 |
Reaction temperature/. degree.C | 200 | 350 | 350 | 700 | 350 |
Contact time/s | 30 | 60 | 100 | 200 | 100 |
Yield of | 76.2% | 85.1% | 86.9% | 92.3% | 62.3% |
In the method, cyclic olefin is used as a raw material, and catalytic cracking is carried out under oxygen atmosphere after catalytic pre-activation by ozone, so that the cyclic olefin can almost completely react without loss, the yield is high, and the controllability is strong.
The above description is only a preferred embodiment of the present invention, and for those skilled in the art, the present invention should not be limited by the description of the present invention, which should be interpreted as a limitation.
Claims (6)
1. A preparation method of perfluoroalkyl diacyl fluoride is characterized by comprising the following steps: the cyclic olefin is pre-activated by an activation chamber, enters a cracking chamber and reacts with oxygen under the condition of a catalyst, and is catalytically cracked to generate perfluorodiacyl fluoride, wherein the reaction formula is shown as (I):
(I)
wherein n is an integer of 1 to 5, Rf1Rf2, Rf3, Rf4, Rf5 and Rf6 are respectively one of fluoro, perfluoroalkyl and perfluoroalkyl ether.
2. The process for producing a perfluoroalkyldiacyl fluoride according to claim 1, wherein n =1, Rf1All of Rf2, Rf3, Rf4, Rf5 and Rf6 are fluorine groups.
3. The method for preparing perfluoroalkyldiacyl fluoride according to claim 1, wherein the pre-activation comprises the steps of introducing cyclic olefin into an activation chamber, filling metal oxide into the activation chamber, introducing O3, and performing activation under light irradiation; the light irradiation time was: 10-90min, and the reaction temperature is-10-20 ℃.
4. The method of claim 3, wherein the metal oxide is one of TiO2, Fe2O3, Fe3O4, CoO, Co3O4, Ag2O, and Pd 2O.
5. The method for preparing perfluoroalkyldiacyl fluoride according to claim 1, wherein the cracking process is carried out by reacting oxygen with activated cyclic olefin as raw material under the action of catalyst; wherein the molar ratio of oxygen to the cyclic olefin is 20:1-1: 10; the contact reaction time is 0.1s to 200 s; the reaction pressure is 0-1 MPa; the reaction temperature is 200-700 ℃.
6. The method for preparing perfluoroalkyldiacyl fluoride according to claim 5, wherein the catalyst is a supported catalyst, and the active ingredient is one or a mixture of more of AgO, Al2O3, CuO, AgF, NaF, KF, RbF and CsF.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201911404655.4A CN111138275B (en) | 2019-12-30 | 2019-12-30 | Perfluoroalkyl diacyl fluoride and preparation method thereof |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201911404655.4A CN111138275B (en) | 2019-12-30 | 2019-12-30 | Perfluoroalkyl diacyl fluoride and preparation method thereof |
Publications (2)
Publication Number | Publication Date |
---|---|
CN111138275A CN111138275A (en) | 2020-05-12 |
CN111138275B true CN111138275B (en) | 2022-06-10 |
Family
ID=70522309
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN201911404655.4A Active CN111138275B (en) | 2019-12-30 | 2019-12-30 | Perfluoroalkyl diacyl fluoride and preparation method thereof |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN111138275B (en) |
Families Citing this family (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN112811978B (en) * | 2021-04-22 | 2021-07-16 | 泉州宇极新材料科技有限公司 | Preparation method of Z-1,3,3, 3-tetrafluoropropene |
Citations (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN105492418A (en) * | 2013-08-26 | 2016-04-13 | 旭硝子株式会社 | Method for producing fluorinated compound |
CN109503364A (en) * | 2018-11-30 | 2019-03-22 | 天津市长芦化工新材料有限公司 | Hexafluoropropylene dimmer cracking prepares the method and perfluoropentyl ether of perfluoropentyl ether |
WO2019116789A1 (en) * | 2017-12-12 | 2019-06-20 | 昭和電工株式会社 | Method and apparatus for producing fluorine-containing organic compound |
-
2019
- 2019-12-30 CN CN201911404655.4A patent/CN111138275B/en active Active
Patent Citations (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN105492418A (en) * | 2013-08-26 | 2016-04-13 | 旭硝子株式会社 | Method for producing fluorinated compound |
WO2019116789A1 (en) * | 2017-12-12 | 2019-06-20 | 昭和電工株式会社 | Method and apparatus for producing fluorine-containing organic compound |
CN109503364A (en) * | 2018-11-30 | 2019-03-22 | 天津市长芦化工新材料有限公司 | Hexafluoropropylene dimmer cracking prepares the method and perfluoropentyl ether of perfluoropentyl ether |
Also Published As
Publication number | Publication date |
---|---|
CN111138275A (en) | 2020-05-12 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
CN111138275B (en) | Perfluoroalkyl diacyl fluoride and preparation method thereof | |
CN111269080B (en) | Perfluoro 1, 3-butadiene microreactor preparation system and preparation method thereof | |
CN110152650A (en) | A kind of preparing propylene by dehydrogenating propane supported catalyst and preparation method thereof | |
CN211871826U (en) | Preparation system of perfluorobutadiene | |
CN111875502B (en) | Method for producing tert-butylamine by direct amination of isobutene | |
CN115228503A (en) | Preparation method of carbon nitride-based copper material for ozone catalytic oxidation water treatment | |
CN104383949B (en) | A kind of Ketocyclopentane catalyst for synthesizing and preparation method thereof and the application in Ketocyclopentane synthesizes | |
CN111269079B (en) | Preparation system and preparation method of perfluoro 1, 3-butadiene | |
CN112125792A (en) | Method for co-producing hydroxycitronellal and hydroxycitronellal | |
CN115646498B (en) | High-stability copper-based catalyst for ethanol dehydrogenation and preparation method thereof | |
CN211814212U (en) | Preparation facilities of perfluor pentyl diacyl fluorine | |
CN217164356U (en) | Continuous reaction device of chlorinated ethylene carbonate | |
CN111153792A (en) | Preparation device and use method of perfluoropentyl diacyl fluoride | |
CN113354806B (en) | Epoxy-terminated allyl alcohol polyether and preparation method thereof | |
CN102530960B (en) | Trichlorosilane production method used during polycrystalline silicon production | |
CN108586390A (en) | The method that dichlorohydrin prepares epoxychloropropane | |
CN112316977B (en) | Preparation method and application of adsorption type immobilized ionic liquid catalyst | |
CN110721731B (en) | Supported catalyst and preparation method and application thereof | |
CN108409690A (en) | A kind of production technology of 1,2- epoxy butanes | |
CN109370648B (en) | Preparation method of high-boiling-point aromatic hydrocarbon solvent based on catalysis of foamed nickel supported catalyst | |
CN113509965B (en) | Regeneration method of catalyst for process of preparing acetonitrile by acetic acid ammoniation method | |
CN1218917C (en) | Process for preparing ethylene glycol by ethylene oxide catalytic hydration | |
CN112079757B (en) | Preparation and purification method of trifluoromethyl sulfur pentafluoride | |
CN1566049A (en) | Solid acid catalyst for preparing ethylene glycol by ethylene oxide hydration | |
CN1120050C (en) | Supported type heteropolyacid catalyst in synthesis of ethylene lycol series supported monoether and diethylene monoethers |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
PB01 | Publication | ||
PB01 | Publication | ||
SE01 | Entry into force of request for substantive examination | ||
SE01 | Entry into force of request for substantive examination | ||
GR01 | Patent grant | ||
GR01 | Patent grant |