JPS5942676B2 - Perfluoroalkoxypropionic acid fluoride having the composition C↓9F↓1↓6O↓4 - Google Patents
Perfluoroalkoxypropionic acid fluoride having the composition C↓9F↓1↓6O↓4Info
- Publication number
- JPS5942676B2 JPS5942676B2 JP62676A JP62676A JPS5942676B2 JP S5942676 B2 JPS5942676 B2 JP S5942676B2 JP 62676 A JP62676 A JP 62676A JP 62676 A JP62676 A JP 62676A JP S5942676 B2 JPS5942676 B2 JP S5942676B2
- Authority
- JP
- Japan
- Prior art keywords
- reaction
- acid fluoride
- epoxide
- hexafluoropropene
- perfluoroalkoxypropionic
- 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.)
- Expired
Links
- KRHYYFGTRYWZRS-UHFFFAOYSA-M Fluoride anion Chemical compound [F-] KRHYYFGTRYWZRS-UHFFFAOYSA-M 0.000 title claims description 13
- 239000000203 mixture Substances 0.000 title description 13
- 239000002253 acid Substances 0.000 title description 10
- XBDQKXXYIPTUBI-UHFFFAOYSA-N Propionic acid Substances CCC(O)=O XBDQKXXYIPTUBI-UHFFFAOYSA-N 0.000 claims description 2
- 238000006243 chemical reaction Methods 0.000 description 20
- PGFXOWRDDHCDTE-UHFFFAOYSA-N hexafluoropropylene oxide Chemical compound FC(F)(F)C1(F)OC1(F)F PGFXOWRDDHCDTE-UHFFFAOYSA-N 0.000 description 14
- -1 alkene epoxides Chemical class 0.000 description 11
- 239000002904 solvent Substances 0.000 description 10
- WEVYAHXRMPXWCK-UHFFFAOYSA-N Acetonitrile Chemical compound CC#N WEVYAHXRMPXWCK-UHFFFAOYSA-N 0.000 description 9
- 150000001875 compounds Chemical class 0.000 description 7
- FAPWRFPIFSIZLT-UHFFFAOYSA-M Sodium chloride Chemical compound [Na+].[Cl-] FAPWRFPIFSIZLT-UHFFFAOYSA-M 0.000 description 6
- 150000002118 epoxides Chemical class 0.000 description 6
- 238000000034 method Methods 0.000 description 6
- 229910052698 phosphorus Inorganic materials 0.000 description 6
- 239000011574 phosphorus Substances 0.000 description 6
- RTZKZFJDLAIYFH-UHFFFAOYSA-N Diethyl ether Chemical compound CCOCC RTZKZFJDLAIYFH-UHFFFAOYSA-N 0.000 description 5
- HCDGVLDPFQMKDK-UHFFFAOYSA-N hexafluoropropylene Chemical compound FC(F)=C(F)C(F)(F)F HCDGVLDPFQMKDK-UHFFFAOYSA-N 0.000 description 5
- 239000011541 reaction mixture Substances 0.000 description 5
- 238000010521 absorption reaction Methods 0.000 description 4
- SBZXBUIDTXKZTM-UHFFFAOYSA-N diglyme Chemical compound COCCOCCOC SBZXBUIDTXKZTM-UHFFFAOYSA-N 0.000 description 4
- 238000002360 preparation method Methods 0.000 description 4
- ZUHZGEOKBKGPSW-UHFFFAOYSA-N tetraglyme Chemical compound COCCOCCOCCOCCOC ZUHZGEOKBKGPSW-UHFFFAOYSA-N 0.000 description 4
- XEKOWRVHYACXOJ-UHFFFAOYSA-N Ethyl acetate Chemical compound CCOC(C)=O XEKOWRVHYACXOJ-UHFFFAOYSA-N 0.000 description 3
- ZMXDDKWLCZADIW-UHFFFAOYSA-N N,N-Dimethylformamide Chemical compound CN(C)C=O ZMXDDKWLCZADIW-UHFFFAOYSA-N 0.000 description 3
- 239000007795 chemical reaction product Substances 0.000 description 3
- 239000012530 fluid Substances 0.000 description 3
- 239000007788 liquid Substances 0.000 description 3
- 239000000047 product Substances 0.000 description 3
- 238000000926 separation method Methods 0.000 description 3
- 239000011780 sodium chloride Substances 0.000 description 3
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 2
- XTHFKEDIFFGKHM-UHFFFAOYSA-N Dimethoxyethane Chemical compound COCCOC XTHFKEDIFFGKHM-UHFFFAOYSA-N 0.000 description 2
- NBIIXXVUZAFLBC-UHFFFAOYSA-N Phosphoric acid Chemical compound OP(O)(O)=O NBIIXXVUZAFLBC-UHFFFAOYSA-N 0.000 description 2
- WYURNTSHIVDZCO-UHFFFAOYSA-N Tetrahydrofuran Chemical compound C1CCOC1 WYURNTSHIVDZCO-UHFFFAOYSA-N 0.000 description 2
- 125000000217 alkyl group Chemical group 0.000 description 2
- 238000009835 boiling Methods 0.000 description 2
- 125000004432 carbon atom Chemical group C* 0.000 description 2
- 239000003054 catalyst Substances 0.000 description 2
- MVPPADPHJFYWMZ-UHFFFAOYSA-N chlorobenzene Chemical compound ClC1=CC=CC=C1 MVPPADPHJFYWMZ-UHFFFAOYSA-N 0.000 description 2
- 238000006114 decarboxylation reaction Methods 0.000 description 2
- 238000004821 distillation Methods 0.000 description 2
- 150000002170 ethers Chemical class 0.000 description 2
- 238000003682 fluorination reaction Methods 0.000 description 2
- 239000000314 lubricant Substances 0.000 description 2
- 238000004519 manufacturing process Methods 0.000 description 2
- LQNUZADURLCDLV-UHFFFAOYSA-N nitrobenzene Chemical compound [O-][N+](=O)C1=CC=CC=C1 LQNUZADURLCDLV-UHFFFAOYSA-N 0.000 description 2
- 150000003018 phosphorus compounds Chemical class 0.000 description 2
- SQGYOTSLMSWVJD-UHFFFAOYSA-N silver(1+) nitrate Chemical compound [Ag+].[O-]N(=O)=O SQGYOTSLMSWVJD-UHFFFAOYSA-N 0.000 description 2
- RYHBNJHYFVUHQT-UHFFFAOYSA-N 1,4-Dioxane Chemical compound C1COCCO1 RYHBNJHYFVUHQT-UHFFFAOYSA-N 0.000 description 1
- VJGCZWVJDRIHNC-UHFFFAOYSA-N 1-fluoroprop-1-ene Chemical compound CC=CF VJGCZWVJDRIHNC-UHFFFAOYSA-N 0.000 description 1
- NAMDIHYPBYVYAP-UHFFFAOYSA-N 1-methoxy-2-(2-methoxyethoxy)ethane Chemical compound COCCOCCOC.COCCOCCOC NAMDIHYPBYVYAP-UHFFFAOYSA-N 0.000 description 1
- ZAFNJMIOTHYJRJ-UHFFFAOYSA-N Diisopropyl ether Chemical compound CC(C)OC(C)C ZAFNJMIOTHYJRJ-UHFFFAOYSA-N 0.000 description 1
- FXHOOIRPVKKKFG-UHFFFAOYSA-N N,N-Dimethylacetamide Chemical compound CN(C)C(C)=O FXHOOIRPVKKKFG-UHFFFAOYSA-N 0.000 description 1
- 239000003513 alkali Substances 0.000 description 1
- 125000003282 alkyl amino group Chemical group 0.000 description 1
- 229910000147 aluminium phosphate Inorganic materials 0.000 description 1
- 150000001408 amides Chemical class 0.000 description 1
- 239000003831 antifriction material Substances 0.000 description 1
- 239000003849 aromatic solvent Substances 0.000 description 1
- 229910052799 carbon Inorganic materials 0.000 description 1
- 150000001721 carbon Chemical group 0.000 description 1
- 238000006471 dimerization reaction Methods 0.000 description 1
- 150000002148 esters Chemical class 0.000 description 1
- 125000001153 fluoro group Chemical group F* 0.000 description 1
- GNOIPBMMFNIUFM-UHFFFAOYSA-N hexamethylphosphoric triamide Chemical compound CN(C)P(=O)(N(C)C)N(C)C GNOIPBMMFNIUFM-UHFFFAOYSA-N 0.000 description 1
- 230000007062 hydrolysis Effects 0.000 description 1
- 238000006460 hydrolysis reaction Methods 0.000 description 1
- 238000002329 infrared spectrum Methods 0.000 description 1
- 238000009413 insulation Methods 0.000 description 1
- PYLWMHQQBFSUBP-UHFFFAOYSA-N monofluorobenzene Chemical compound FC1=CC=CC=C1 PYLWMHQQBFSUBP-UHFFFAOYSA-N 0.000 description 1
- 150000002826 nitrites Chemical class 0.000 description 1
- 125000004430 oxygen atom Chemical group O* 0.000 description 1
- 239000002244 precipitate Substances 0.000 description 1
- WMFABESKCHGSRC-UHFFFAOYSA-N propanoyl fluoride Chemical compound CCC(F)=O WMFABESKCHGSRC-UHFFFAOYSA-N 0.000 description 1
- 125000001453 quaternary ammonium group Chemical group 0.000 description 1
- 239000002994 raw material Substances 0.000 description 1
- 239000012066 reaction slurry Substances 0.000 description 1
- 230000035484 reaction time Effects 0.000 description 1
- 238000007127 saponification reaction Methods 0.000 description 1
- 238000007789 sealing Methods 0.000 description 1
- 238000007086 side reaction Methods 0.000 description 1
- 229940096017 silver fluoride Drugs 0.000 description 1
- REYHXKZHIMGNSE-UHFFFAOYSA-M silver monofluoride Chemical compound [F-].[Ag+] REYHXKZHIMGNSE-UHFFFAOYSA-M 0.000 description 1
- 229910001961 silver nitrate Inorganic materials 0.000 description 1
- 238000001577 simple distillation Methods 0.000 description 1
- 239000011877 solvent mixture Substances 0.000 description 1
- 238000010183 spectrum analysis Methods 0.000 description 1
- 239000007858 starting material Substances 0.000 description 1
- 238000003756 stirring Methods 0.000 description 1
- HXJUTPCZVOIRIF-UHFFFAOYSA-N sulfolane Chemical compound O=S1(=O)CCCC1 HXJUTPCZVOIRIF-UHFFFAOYSA-N 0.000 description 1
- YLQBMQCUIZJEEH-UHFFFAOYSA-N tetrahydrofuran Natural products C=1C=COC=1 YLQBMQCUIZJEEH-UHFFFAOYSA-N 0.000 description 1
- 239000013638 trimer Substances 0.000 description 1
Landscapes
- Heterocyclic Compounds That Contain Two Or More Ring Oxygen Atoms (AREA)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
Description
【発明の詳細な説明】
テトラフルオルエチレンエポキシド又はヘキサフルオル
プロペンエポキシドのような′ゞ−フルオル化されたア
ルケンエポキシドはフッ化アルカリ、第4級アンモニウ
ムフッ化物、フッ化銀又は活性炭のような触媒の存在下
にパーフルオル化されたカルボン酸フルオリドに付加し
てポリ′ゞ−フルオルアルコキシカルボン酸フルオリド
が形成されるが、この形成された化合物は高能率の減摩
剤の製造のための出発原料として重要である。DETAILED DESCRIPTION OF THE INVENTION '-Fluorinated alkene epoxides, such as tetrafluoroethylene epoxide or hexafluoropropene epoxide, may be prepared from alkali fluoride, quaternary ammonium fluoride, silver fluoride or activated carbon. Addition to the perfluorinated carboxylic acid fluoride in the presence of a catalyst forms a poly'-fluoroalkoxycarboxylic acid fluoride, and the compound formed is a starting material for the production of high efficiency lubricants. Important as a raw material.
この減摩剤はカルボン酸フルオリドを加水分解して相当
する酸に導びき、次いでフッ素化脱炭酸を行ない、炭素
原子の1個少ない飽和エーテルに導びくことによつて得
られる。このものは化学的に及び熱に対して非常に安定
であり、従つて非常に高度の負担に耐えることが出来る
。勿論上記反応では常に極めて種々の分子量を有する生
成物の混合物が得られる。ペルキー特許第751076
号の発明に従つて、触媒として硝酸銀を使用すると、ヘ
キサフルオフプロペンエポキシドの選択的二量体化が行
なわれて′ゞ−フルオルーα−プロポキシプロピオン酸
フルオリドを形成せしめることが出来る。This lubricant is obtained by hydrolysis of a carboxylic acid fluoride to the corresponding acid followed by fluorination decarboxylation to form a saturated ether with one less carbon atom. It is very chemically and thermally stable and can therefore withstand very high stresses. Of course, the reactions described always give mixtures of products with very different molecular weights. Pelkey Patent No. 751076
According to this invention, the use of silver nitrate as a catalyst allows selective dimerization of hexafluofpropene epoxide to form '-fluoro-alpha-propoxypropionic acid fluoride.
本発明により今回、C_9F、604なる組成を有する
新規パーフルオルアルコキシプロピオン酸フルオリドを
得ることが出来、なおこの際同時にジフルオルフオスフ
オランが殆んど定量的収率で得られる。Thanks to the present invention, it is now possible to obtain a new perfluoroalkoxypropionic acid fluoride having the composition C_9F,604, and at the same time difluorophosfluoran is obtained in an almost quantitative yield.
本発明は、下記式
C_F3−OF−C_F2
、/ (I)
なるへキサフルオルペロペンエポキシドを下記一般式R
、−P−R3(■)
〔式中R4、R2及びR3は、同一でも異なつていても
よく、ジー(C_1〜R4)アルキルアミノ基を示す〕
で表わされる燐化合物と−50ないし+10℃の淵度に
於て反応させることによつて製造される、C_9F16
O4なる組成を有する′々−フルオルアルコキシプロピ
オン酸フルオリドに関する。The present invention provides hexafluoroperopene epoxide of the following formula C_F3-OF-C_F2, / (I) with the following general formula R
, -P-R3(■) [In the formula, R4, R2 and R3 may be the same or different and represent a di(C_1-R4) alkylamino group]
C_9F16 produced by reacting with a phosphorus compound represented by at a temperature of -50 to +10°C.
The present invention relates to '-fluoroalkoxypropionic acid fluoride having the composition O4.
なおこの製造に当つてジフルオルフオスフオランが同時
に製造される。ある特定のザフルオルフオスフオランの
製造を意図するものでない限り、式の燐化合物としては
、そのアルキル基が同一のものであつて1ないし2個の
炭素原子を有するものを使用するのが特に好都合である
。Note that during this production, difluorophosfluorane is produced at the same time. Unless it is intended to produce a specific fluorophosfluoran, it is preferable to use phosphorus compounds of the formula whose alkyl groups are identical and have 1 or 2 carbon atoms. This is especially convenient.
殊に燐酸トリスジメチルアミドを使用することができる
。各アルキル基に2ないし4個の炭素原子を含む燐酸ト
リスジアルキリアミド類を用いた場合の収率はいくらか
低下する。上記化合物の製造に当つては一般に式の燐化
合物をあらかじめ什込み、所望の反応温度に於てこれに
ヘキサフルオルプロペンエポキシドを導入する。しかし
又あらかじめヘキサフルオルプロペンエポキシドを仕込
み、これに燐化合物を導入することもできる。ヘキサフ
ルオルプロペンエポキシドは純粋の形のものが使用され
る。In particular, phosphoric acid trisdimethylamide can be used. Yields are somewhat lower when using phosphoric acid trisdialkylamides containing 2 to 4 carbon atoms in each alkyl group. In the preparation of the above compounds, a phosphorus compound of the formula is generally charged in advance, and hexafluoropropene epoxide is introduced therein at the desired reaction temperature. However, it is also possible to charge hexafluoropropene epoxide in advance and introduce the phosphorus compound therein. Hexafluoropropene epoxide is used in pure form.
しかしヘキサフルオルプロペンは本発明による方法の条
件のもとに於ては不活性であるから、ヘキサフルオルプ
ロペンエポキシドの製造に際して得られるヘキサフルオ
ルプロペンとヘキサフルオルプロペンエポキシドとの混
合物の相当量を使用することも出来る。一般に式の燐化
合物1モルにつき1式のヘキサフルオルプロペンエポキ
シドを3モル使用する。However, since hexafluoropropene is inert under the conditions of the process according to the invention, the proportion of the mixture of hexafluoropropene and hexafluoropropene epoxide obtained in the preparation of hexafluoropropene epoxide is You can also use quantity. Generally, 3 moles of hexafluoropropene epoxide of the formula are used per mole of the phosphorus compound of the formula.
完全な反応にまで反応をす\めるためには、エポキシド
を約10%までの少過剰量で使用するのが有利である。
反応しなかつたエポキシドは反応終了後反応混合物から
容易に回収できる。エポキシドの添加速度はあまり厳密
でなくともよい。In order to drive the reaction to completeness, it is advantageous to use a small excess of the epoxide, up to about 10%.
Unreacted epoxide can be easily recovered from the reaction mixture after the reaction is completed. The rate of addition of epoxide does not have to be too critical.
場合によつては必要量を液状で一度に添加することも出
来る。添加速度及び反応淵度の如何により反応時間は0
.5ないし10時間である。反応温度は−50℃ないし
+1『Cを使用し得る。しかし望ましからぬ副反応が起
るために、反応虎度は+1『Cを越えてはならない。又
、反応淵度は0℃以上に上昇せしめない方がよい。40
ないし−25℃の渦度で行なうのが有利であり、この泥
度に於ては加圧することなく操作することができる。Depending on the case, the required amount can be added at once in liquid form. Depending on the addition rate and reaction depth, the reaction time may be 0.
.. 5 to 10 hours. The reaction temperature can range from -50°C to +1°C. However, because undesirable side reactions occur, the reaction intensity must not exceed +1'C. Further, it is better not to allow the reaction temperature to rise above 0°C. 40
It is advantageous to work at a vorticity of between -25 DEG C. and at this turbidity it is possible to operate without pressurization.
−25℃以上の反応淵度に於ては加圧容器を使用するの
が適当であるが、このような淵度は特定の溶剤を使用す
ることなく操作が可能となる場合には有利である。特に
好都合な収率は、−10℃に於てヘキサフルオルプロペ
ンエポキシドを、それが消費される速成で供給する場合
に得られる。上記方法に於て使用しうる溶剤又は溶剤混
合物は極性で非プロトン性のもので且つ反応条件のもと
に不活性で液状のものでなければならない。When the reaction temperature is -25°C or higher, it is appropriate to use a pressurized vessel, but such a depth is advantageous if the operation can be performed without using a specific solvent. . Particularly advantageous yields are obtained when the hexafluoropropene epoxide is fed at -10 DEG C. rapidly as it is consumed. The solvent or solvent mixture that can be used in the above process must be polar, aprotic and inert and liquid under the reaction conditions.
かかる溶剤としては反応渦度に従つて、例えばアセトニ
トリルのようなニトリル類、ジメチルフオルムアミド又
はジメチルアセトアミドのようなアミド類、エチレング
リコールジメチルエーテル、ジエチレングリコールジメ
チルエーテル〔ジクリメ(Diglyme)〕、テトラ
エチレングリコールジメチルエーテル〔テトラグリメ(
TetragIyme)]、ジエチルエーテル、ジイソ
プロピルエーテル、テトラヒドロフラン、ジオキサンの
ようなエーテル類、更にスルフオラン、更に酢酸エチル
のようなエステル類又はニトロベンゼン、フルオルベン
ゼン又はクロルベンゼンのような芳香族溶剤が適する。
又反応成分、殊に式の燐化合物を適当に過剰量で或は反
応生成物又は反応混合物も同様に溶剤として使用するこ
とが出来る。使用する溶剤の量はあまり厳密でなくとも
よい。Examples of such solvents include nitrites such as acetonitrile, amides such as dimethylformamide or dimethylacetamide, ethylene glycol dimethyl ether, diethylene glycol dimethyl ether (Diglyme), tetraethylene glycol dimethyl ether (Tetraglyme), etc., depending on the reaction vorticity. (
Suitable are ethers such as TetragIyme), diethyl ether, diisopropyl ether, tetrahydrofuran, dioxane, furthermore sulfolane, furthermore esters such as ethyl acetate or aromatic solvents such as nitrobenzene, fluorobenzene or chlorobenzene.
It is also possible to use suitably excess amounts of the reaction components, in particular the phosphorus compounds of the formula, or the reaction products or reaction mixtures as solvents as well. The amount of solvent used does not have to be too critical.
しかし、適用する反応泥度のもとに於て反応混合物が充
分混合されることが出来且つ粘度があまり高くならない
ように配慮しなければならない。例えばH式の燐化合物
1重量部に対して0,25ないし4容量部の溶剤が使用
される。上記方法は非連続的に行うことが出来る。However, care must be taken to ensure that the reaction mixture can be sufficiently mixed under the applied reaction slurry and that the viscosity does not become too high. For example, 0.25 to 4 parts by volume of solvent are used per part by weight of the phosphorus compound of formula H. The above method can be performed discontinuously.
勿論簡単な方法で連続的に行うこともでき、この場合例
えば反応成分1及びを、場合により溶剤の添加のもとに
、反応搗度に保持された反応域中に連続的に供給し、反
応混合物をこの反応域申に適当時間滞留せしめた後他の
場所から反応成分の添加量に応じて収り出し、場合によ
り反応を完結させるために後反応器中に導入するように
して行う。反応生成物の分離は簡単な蒸留により行うこ
とが出来る。該方法により得られたパーフルオルアルコ
キシプロピオン酸フルオリドは同時に得られるジフルオ
ルフオスフオラン並びに場合により使用される溶剤中に
難溶性であるので、一般に重い方の相として析出し、従
つて反応混合物から分離することが出来る。これを精製
するためには、例えばアセトニトリルのような溶剤で洗
滌し、ついで蒸留する。更に軽い方のジフルオルフオス
フオランも同様に、場合により溶剤を分離した後、蒸留
により精製することが出来る。過剰量のヘキサフルオル
プロペンエポキシドを用いて又はヘキサフルオルプロペ
ンを含む混合物を用いて処理した場合には、反応生成物
を分離する前に反応混合物をoないし10’Cに加温す
るのが有利である。Of course, it can also be carried out continuously in a simple manner, in which case, for example, reaction components 1 and 1 are fed continuously, optionally with the addition of a solvent, into a reaction zone maintained at the reaction temperature. After the mixture remains in this reaction zone for a suitable time, it is removed from another location depending on the amount of reaction components added, and optionally introduced into a post-reactor to complete the reaction. Separation of the reaction products can be carried out by simple distillation. Since the perfluoroalkoxypropionic acid fluoride obtained by this process is poorly soluble in the simultaneously obtained difluorophosfluoran as well as in the solvents used, it generally precipitates out as a heavier phase and therefore does not form in the reaction mixture. It can be separated from To purify it, it is washed with a solvent such as acetonitrile and then distilled. The lighter difluorophosfluoran can similarly be purified by distillation, optionally after separation of the solvent. When treated with an excess of hexafluoropropene epoxide or with a mixture containing hexafluoropropene, it is recommended to warm the reaction mixture to 0 to 10'C before separating the reaction products. It's advantageous.
この際解剰量のヘキサフルオルプロペンエポキシド及び
場合によりヘキサフルオルプロペンはガス状で揮発し、
これらは回収することが出来る。得られたノゞ−フルオ
ルアルコキシプロピオン酸フルオリドはC9Fl6O4
の組成を有し、115ないし118はCに於て沸騰する
。At this time, the dissolved amount of hexafluoropropene epoxide and, if necessary, hexafluoropropene evaporates in gaseous form,
These can be recovered. The obtained no-fluoroalkoxypropionic acid fluoride is C9Fl6O4
115 to 118 boil at C.
このものはヘキサフルオルプロペンエポキシドの三量体
に比して酸素原子を1個多く且つフツ素原子を2個少な
く含有する。この赤外線吸収曲線を第1図に示す。その
特徴としては9.7μ〔′々−キンーエルマー(Per
kin−Elmer)457、NaClギアピラー〕に
強いIR吸収を示す。その構造はNMRスペクトル分析
により下記式に相当するが、これには勿論多数の配座異
性体及びジアステレオマ一が存在しうる。This product contains one more oxygen atom and two less fluorine atoms than the trimer of hexafluoropropene epoxide. This infrared absorption curve is shown in FIG. Its characteristics include 9.7 μ ['-Kin-Elmer (Per
Kin-Elmer) 457, NaCl gear pillar] exhibits strong IR absorption. Its structure corresponds to the following formula according to NMR spectral analysis, but it can of course exist in many conformational isomers and diastereoisomers.
上記′ゞ−フルオルアルコキシプロピオン酸フルオリド
の他に使用した式の燐化合物から下記一般式V −P
(式中R,,R2及びR3は式の化合物に対して示した
意味を有する)で示される相応するジフルオルフオスフ
オランの当量が得られる。From the phosphorus compound of the formula used in addition to the above '-fluoroalkoxypropionic acid fluoride, it is represented by the following general formula V-P (wherein R, , R2 and R3 have the meanings indicated for the compound of the formula). An equivalent amount of the corresponding difluorophosfluoran is obtained.
このジフルオルフオスフオランは公知の化合物であるが
、この化合物は従来極めて煩雑な方法によらなければ得
られなかつたものである。新規パーフルオルアルコキシ
プロピオン酸フルオリド式の構造式にもとずく′々−フ
ルオル α−〔3,6−ジメチル−1,4−ジオキサニ
ル一2−オキシ〕−プロピオン酸フルオリドである。全
反応は下記反応式により示すことができる:上記プロピ
オン酸フルオリドから、公知方法により鹸化及びフツ素
化脱炭酸により下記式なる不活性エチルエーテルが得ら
れる。Although this difluorophosfluoran is a known compound, this compound could not be obtained conventionally without using extremely complicated methods. It is a '-fluoro-[alpha]-[3,6-dimethyl-1,4-dioxanyl-2-oxy]-propionic acid fluoride based on the structural formula of a novel perfluoroalkoxypropionic acid fluoride. The overall reaction can be represented by the following reaction formula: From the above propionic acid fluoride, an inert ethyl ether of the following formula is obtained by saponification and fluorination decarboxylation using known methods.
この/々一フルオル一〔3,6−ジメチル−1,4−ジ
オキサニル一2−オキシ〕一エタンは101〜104℃
の沸点を有す。この化合物は例えば減摩剤、シーリング
液、絶縁用液体又は水圧用液体として適する。本発明の
化合物の製造法を下記の例により例解する。This /monofluoro-[3,6-dimethyl-1,4-dioxanyl-2-oxy]monoethane was heated to a temperature of 101 to 104°C.
It has a boiling point of The compounds are suitable, for example, as anti-friction agents, sealing fluids, insulation fluids or hydraulic fluids. The preparation of the compounds of the invention is illustrated by the following examples.
例
ジエチレングリコールジメチルエーテル(ジグリメ)3
00m1及びPOCN( CH)2〕33009( 1
.67モル)よりなる溶液中に、強力冷却器、撹拌器及
び低偏溌度計を備えたΞ頚コルベン中に於て定常的撹拌
下−40ないし−30ルCでヘキサフルオルプロペンエ
ポキシド及びヘキサフルオルプロペンよりなる混合物(
重量比65:35)1400f9を導入する。Example diethylene glycol dimethyl ether (diglyme) 3
00m1 and POCN(CH)2]33009(1
.. 67 mol) of hexafluoropropene epoxide and hexafluoropropene epoxide and hexafluoropropene epoxide at -40 to -30 °C under constant stirring in a high-necked Kolben equipped with a strong condenser, a stirrer, and a low eccentricity meter. A mixture consisting of fluoropropene (
Weight ratio 65:35) 1400f9 is introduced.
仕込量は毎時201である。次いで上記謳度に於て更に
5時間撹拌する。ついで徐々に0℃に加漉してヘキサフ
ルオルプロペン及び過剰量のエポキシドを追い出し、得
られる二相混合物を分液ロードにより分離する。下相(
871y)をアセトニトリル600m1で洗滌して生成
物混合物7JモV1を得る。これを蒸留する。第1分画:
52〜115℃=579IRスペクトル:9.7μに於
ける吸収(パーキンーエルマ一457、NaClギアピ
ラー)上相はジグリメ及びジフルオルートリスージメチ
ルアミノフオスオランの混合物よりなる。The amount of preparation is 201 per hour. Then, the mixture was stirred for an additional 5 hours at the above-mentioned temperature. The mixture is then gradually strained to 0° C. to drive off hexafluoropropene and excess epoxide, and the resulting two-phase mixture is separated by liquid separation loading. Lower phase (
871y) with 600 ml of acetonitrile to obtain the product mixture 7JMoV1. Distill this. First fraction:
52 DEG -115 DEG C.=579 IR spectrum: Absorption at 9.7 .mu. (Perkin-Elmer 457, NaCl Gear Pillar) The upper phase consists of a mixture of diglyme and difluoro-tris-dimethylaminofluorane.
これを蒸留により後処理する。ジフルオルートリスージ
メチルアミノフオスフオラン2579(理論値の89%
)が得られる。沸点22℃/0.4m7!LHg上記と
同一条件のもとに、但しジグリメをテトラグリメで置代
えて行つた場合にも同様の結果が得られた。This is worked up by distillation. Difluorotris-dimethylaminofluoran 2579 (89% of theoretical value)
) is obtained. Boiling point 22℃/0.4m7! LHg Similar results were obtained under the same conditions as above, except that diglyme was replaced with tetraglyme.
第1図は本発明により製造されたパーフルオルアルコキ
シプロピオン酸フルオリドのNaClギアピラーに於い
てパーキンーエルマ一457により測定した赤外線吸収
曲線を示す。FIG. 1 shows an infrared absorption curve measured with a Perkin-Elmer 457 in a NaCl gear pillar of perfluoroalkoxypropionic acid fluoride prepared according to the present invention.
Claims (1)
1,4−ジオキサニル−3−オキシ〕−プロピオン酸フ
ルオリド。[Claims] Perfluoro-α-[3,6-dimethyl-
1,4-Dioxanyl-3-oxy]-propionic acid fluoride.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP62676A JPS5942676B2 (en) | 1976-01-01 | 1976-01-01 | Perfluoroalkoxypropionic acid fluoride having the composition C↓9F↓1↓6O↓4 |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP62676A JPS5942676B2 (en) | 1976-01-01 | 1976-01-01 | Perfluoroalkoxypropionic acid fluoride having the composition C↓9F↓1↓6O↓4 |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS5283606A JPS5283606A (en) | 1977-07-12 |
| JPS5942676B2 true JPS5942676B2 (en) | 1984-10-16 |
Family
ID=11478927
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP62676A Expired JPS5942676B2 (en) | 1976-01-01 | 1976-01-01 | Perfluoroalkoxypropionic acid fluoride having the composition C↓9F↓1↓6O↓4 |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS5942676B2 (en) |
-
1976
- 1976-01-01 JP JP62676A patent/JPS5942676B2/en not_active Expired
Also Published As
| Publication number | Publication date |
|---|---|
| JPS5283606A (en) | 1977-07-12 |
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