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JPH0684316B2 - Method for stabilizing perfluoro compound - Google Patents
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JPH0684316B2 - Method for stabilizing perfluoro compound - Google Patents

Method for stabilizing perfluoro compound

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Publication number
JPH0684316B2
JPH0684316B2 JP1328225A JP32822589A JPH0684316B2 JP H0684316 B2 JPH0684316 B2 JP H0684316B2 JP 1328225 A JP1328225 A JP 1328225A JP 32822589 A JP32822589 A JP 32822589A JP H0684316 B2 JPH0684316 B2 JP H0684316B2
Authority
JP
Japan
Prior art keywords
compound
hydrogen fluoride
organic compound
irradiation
perfluoro
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 - Lifetime
Application number
JP1328225A
Other languages
Japanese (ja)
Other versions
JPH03190826A (en
Inventor
尚哉 岡田
雅樹 吉永
孝二 浅田
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Tokuyama Corp
Original Assignee
Tokuyama Corp
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Tokuyama Corp filed Critical Tokuyama Corp
Priority to JP1328225A priority Critical patent/JPH0684316B2/en
Publication of JPH03190826A publication Critical patent/JPH03190826A/en
Publication of JPH0684316B2 publication Critical patent/JPH0684316B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

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  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)

Description

【発明の詳細な説明】 〔産業上の利用分野〕 本発明は、加熱を行なった場合においてもフッ化水素の
発生の少ないパーフルオロ有機化合物を得るためのパー
フルオロ化合物の安定化方法に関する。更に詳しくは、
実質的にパーフルオロ化された炭化水素化合物又はアミ
ノ化合物の安定化方法に関する。
Description: TECHNICAL FIELD The present invention relates to a method for stabilizing a perfluoro compound for obtaining a perfluoro organic compound that generates little hydrogen fluoride even when heated. For more details,
The present invention relates to a method for stabilizing a substantially perfluorinated hydrocarbon compound or amino compound.

〔従来技術および発明が解決しようとする課題〕[Problems to be Solved by Prior Art and Invention]

パーフルオロ有機化合物は化学的に安定であり、熱伝導
性が高く、不燃性であり、また無毒であるため、電子部
品信頼性テスト用媒体、電子部品の直接冷却のための媒
体、気相ハンダ付け用熱媒体等として利用されている。
しかしながら、パーフルオロ有機化合物を熱媒体等とし
て用いるとき、高温特にその沸点まで加熱するとフッ化
水素が発生するという問題があった。フッ化水素は腐食
性が高いために極くわずか発生しても装置材質の腐食や
電子部品の損傷の原因となるため、フッ化水素を発生し
ないパーフルオロ有機化合物が望まれていた。
Perfluoroorganic compounds are chemically stable, have high thermal conductivity, are nonflammable, and are nontoxic, so they are the media for electronic component reliability testing, media for direct cooling of electronic components, and vapor phase solder. It is used as a heat medium for attachment.
However, when a perfluoroorganic compound is used as a heating medium or the like, there is a problem that hydrogen fluoride is generated when heated at a high temperature, especially to its boiling point. Since hydrogen fluoride is highly corrosive, it causes corrosion of the material of the apparatus and damage to electronic parts even if it is generated in a very small amount. Therefore, a perfluoro organic compound that does not generate hydrogen fluoride has been desired.

そこで、フッ素化して得られたパーフルオロ有機化合物
の純度を高め、より安定なものにするために精製するこ
とが行なわれてきた。例えば、高濃度の水酸化ナトリウ
ム水溶液とジイソブチルアミンの混合物中でパーフルオ
ロ有機化合物を長時間還流させるアルカリアミン処理、
ナトリウムメトキシドあるいはナトリウムエトシキドと
ジイソブチルアミンの混合物中でパーフルオロ有機化合
物を長時間還流させるアルコラート−アミン処理、なら
びに蒸留、ガスクロマトグラフィーによる精製等が行な
われてきた。しかしながら上記精製法によってもフッ化
水素がほとんど発生しないパーフルオロ有機化合物を得
ることが難しく、パーフルオロ有機化合物を処理する効
率のよい方法が望まれていた。
Therefore, the perfluorinated organic compound obtained by fluorination has been purified in order to increase its purity and make it more stable. For example, an alkaline amine treatment in which a perfluoroorganic compound is refluxed for a long time in a mixture of a high-concentration aqueous sodium hydroxide solution and diisobutylamine,
Alcolate-amine treatment of refluxing a perfluoroorganic compound for a long time in a mixture of sodium methoxide or sodium ethoxide and diisobutylamine, distillation, purification by gas chromatography and the like have been carried out. However, it is difficult to obtain a perfluoro organic compound that hardly generates hydrogen fluoride even by the above-mentioned purification method, and an efficient method for treating the perfluoro organic compound has been desired.

〔課題を解決するための手段〕[Means for Solving the Problems]

そこで本発明者らは、加熱してもフッ化水素が発生する
ことなく、熱媒体等として好適に使用できるパーフルオ
ロ有機化合物を得ることを目的して鋭意研究を続けてき
た。その結果、有機化合物のフッ素化により得られたパ
ーフルオロ有機化合物を含むフッ素化生成物を紫外線照
射することによって上記の目的を達成し得ることを見出
し本発明を完成させるに至った。
Therefore, the present inventors have continued earnest research for the purpose of obtaining a perfluoroorganic compound which does not generate hydrogen fluoride even when heated and can be suitably used as a heat medium and the like. As a result, they have found that the above object can be achieved by irradiating a fluorinated product containing a perfluoroorganic compound obtained by fluorinating an organic compound with ultraviolet rays, and completed the present invention.

すなわち、本発明は、炭化水素化合物又はアミノ化合物
のフッ素化によって得た、実質的にパーフルオロ化合物
よりなる反応生成物に、フッ素化剤を加えることなく、
紫外線を照射することを特徴とするパーフルオロ化合物
の安定化方法である。
That is, the present invention, obtained by fluorination of a hydrocarbon compound or an amino compound, to the reaction product consisting essentially of a perfluoro compound, without adding a fluorinating agent,
It is a method for stabilizing a perfluoro compound, which comprises irradiating with ultraviolet rays.

本発明で使用し得るパーフルオロ有機化合物は、紫外線
照射によって解裂する結合を有さないものであれば、何
ら制限なく採用できる。ここで、紫外線照射によって解
裂する結合としては、例えば、エーテル結合、チオケー
テル結合、フッ素以外のハロゲンと炭素との結合、並び
にカルボニル基および−SO2F基を構成する結合等が挙げ
られる。これらの結合を有するパーフルオロ有機化合物
は、後述する紫外線照射によって一部分解するために、
本発明では好ましくない。
The perfluoroorganic compound that can be used in the present invention can be adopted without any limitation as long as it does not have a bond that is cleaved by ultraviolet irradiation. Here, examples of the bond that is cleaved by irradiation with ultraviolet rays include an ether bond, a thioketel bond, a bond between a halogen other than fluorine and carbon, and a bond forming a carbonyl group and a —SO 2 F group. Perfluoro organic compound having these bonds, because it is partially decomposed by ultraviolet irradiation described later,
Not preferred in the present invention.

本発明におけるパーフルオロ有機化合物は、炭素−水素
結合を有する有機化合物、就中、炭化水素化合物又はア
ミノ化合物のフッ素化によって得られる。該有機化合物
は、上記したパーフルオロ有機化合物と同様に紫外線照
射によって解裂する結合を有さないものが一般に採用さ
れる。しかし、該有機化合物が紫外線照射によって解裂
する結合を有していたとしても、フッ素化によって該結
合が解裂してしまい、得られたパーフルオロ有機化合物
が結果的に該結合を有さない場合もあり、そのようなパ
ーフルオロ有機化合物の製造を目的をする場合には、そ
の原料となる有機化合物は紫外線照射によって解裂する
結合を有していてもよい。
The perfluoro organic compound in the present invention is obtained by fluorinating an organic compound having a carbon-hydrogen bond, especially a hydrocarbon compound or an amino compound. As the organic compound, a compound that does not have a bond that is cleaved by irradiation with ultraviolet rays is generally adopted as in the above-mentioned perfluoro organic compound. However, even if the organic compound has a bond that is cleaved by UV irradiation, the bond is cleaved by fluorination, and the resulting perfluoroorganic compound does not have the bond as a result. In some cases, for the purpose of producing such a perfluoro organic compound, the organic compound as a raw material thereof may have a bond that is cleaved by ultraviolet irradiation.

本発明におけるパーフルオロ有機化合物を得るためにフ
ッ素化の原料として使用される有機化合物を挙げると、
例えば、脂肪族又は芳香族の炭化水素類;脂肪族又は芳
香族の第一アミン、第二アミン、第三アミン等のアミン
類である。これらの中でも特に好適なものは、炭素数が
4〜60個、さらには5〜30個である液体の有機化合物で
ある。これらの有機化合物を具体的に示すと、ペンタ
ン、ヘキサン、ヘプタン、オクタン、シクロヘキサン、
メチルシクロヘキサン、ジメチルシクロヘキサン、デカ
リン、メチルデカリン等の脂肪族炭化水素類;ベンゼ
ン、トルエン、キシレン、ナフタレン、アントラセン、
フェナントレン等の芳香族炭化水素類;トリプロピルア
ミン、トリブチルアミン、トリペンチルアミン、トリヘ
キシルアミン、ブチルジペンチルアミン、ジブチルプロ
ピルアミン等のアミン類である。
Examples of the organic compound used as a raw material for fluorination to obtain the perfluoroorganic compound in the present invention include:
For example, aliphatic or aromatic hydrocarbons; aliphatic or aromatic primary amines, secondary amines, tertiary amines, and other amines. Among these, particularly preferable are liquid organic compounds having 4 to 60 carbon atoms, and further 5 to 30 carbon atoms. Specific examples of these organic compounds are pentane, hexane, heptane, octane, cyclohexane,
Aliphatic hydrocarbons such as methylcyclohexane, dimethylcyclohexane, decalin and methyldecalin; benzene, toluene, xylene, naphthalene, anthracene,
Aromatic hydrocarbons such as phenanthrene; amines such as tripropylamine, tributylamine, tripentylamine, trihexylamine, butyldipentylamine and dibutylpropylamine.

パーフルオロ有機化合物の製造方法としては、上記した
有機化合物を原料とした公知のフッ素化方法が何ら制限
なく採用することができる。例えば、フッ素ガスによる
直接フッ素化方法、電解フッ素化方法および高原子価金
属フッ化物によるフッ素化方法、或いは、これらを適宜
組合せたフッ素化方法等が好適に採用される。こうして
原料の有機化合物に対応したパーフルオロ有機化合物を
含むフッ素化生成物が得られる。
As a method for producing a perfluoro organic compound, a known fluorination method using the above organic compound as a raw material can be adopted without any limitation. For example, a direct fluorination method using a fluorine gas, an electrolytic fluorination method, a fluorination method using a high-valent metal fluoride, or a fluorination method in which these are appropriately combined is suitably adopted. Thus, a fluorinated product containing a perfluoro organic compound corresponding to the raw material organic compound is obtained.

本発明においては、こうして得られたパーフルオロ有機
化合物、好ましくはさらに中和、蒸留或いは公知の方法
により精製されたパーフルオロ有機化合物を含むフッ素
化生成物が紫外線照射処理の対象となる。紫外線の照射
はフッ素ガスやフッ化水素等のフッ素化剤を加えること
なく、行われる。特にで行なわれる。フッ素ガスが存在
する場合には加熱時のフッ化水素の発生の抑制されたパ
ーフルオロ有機化合物を得ることができない。紫外線照
射時の雰囲気はフッ素ガスが実質的に存在しければ、N2
ガスやArガスなどを用いた不活性雰囲気、または、空気
等を用いた酸化性雰囲気であってもよい。
In the present invention, the perfluorinated organic compound thus obtained, preferably a fluorinated product containing a perfluoroorganic compound further purified by neutralization, distillation or a known method, is the object of ultraviolet irradiation treatment. Irradiation with ultraviolet rays is performed without adding a fluorinating agent such as fluorine gas or hydrogen fluoride. Especially done in. When fluorine gas is present, it is not possible to obtain a perfluoroorganic compound in which generation of hydrogen fluoride during heating is suppressed. The atmosphere at the time of UV irradiation is N 2 if fluorine gas is substantially present.
It may be an inert atmosphere using gas or Ar gas, or an oxidizing atmosphere using air or the like.

紫外線照射の方法は特に限定されない。一般に水銀ラン
プその他の、波長190nm〜400nmの紫外線又はこれを含む
光を発する公知の紫外線源を用いて行なうことができ
る。光源は処理液内に入れてもよく、或いは紫外線が良
好に通過する材質を通して外から照射してもよい。紫外
線が良好に通過する材質としては、ガラス類;単結晶サ
ファイヤ;フッ化ビニリデン重合体、テトラフルオロエ
チレン−ヘキサフルオロプロピレン共重合体、テトラフ
ルオロエキレン−エチレン共重合体、テトラフルトロエ
チレン−パーフルオロアルキルビニルエーテル共重合
体、クロロトリフルオロエチレン重合体等のフッ素系の
樹脂などが挙げられる。尚、紫外線照射中に微量のフッ
化水素が発生することがあるため、紫外線透過材として
用いられる石英ガラスのようなガラス類は表面を耐フッ
酸性の樹脂で保護することが好ましい。紫外線照射の時
間は対象となるパーフルオロ有機化合物によって異なる
ため、あらかじめ実験を行ない決定することが望まし
い。一般に5分〜200時間さらに1時間〜50時間程度が
適当である。反応様式としては流通式およびバッチ式の
いずれもが採用されうる。
The method of ultraviolet irradiation is not particularly limited. In general, a mercury lamp or other known ultraviolet ray source that emits ultraviolet rays having a wavelength of 190 nm to 400 nm or light containing the same can be used. The light source may be placed in the treatment liquid, or may be irradiated from the outside through a material through which ultraviolet rays pass well. Materials that allow ultraviolet rays to pass satisfactorily include glass; single crystal sapphire; vinylidene fluoride polymer, tetrafluoroethylene-hexafluoropropylene copolymer, tetrafluoroethylene-ethylene copolymer, tetraflutroethylene-perme Examples thereof include fluorocarbon resins such as fluoroalkyl vinyl ether copolymers and chlorotrifluoroethylene polymers. Since a slight amount of hydrogen fluoride may be generated during irradiation of ultraviolet rays, it is preferable to protect the surface of glass such as quartz glass used as an ultraviolet ray transmitting material with a hydrofluoric acid resistant resin. Since the time of UV irradiation varies depending on the target perfluoroorganic compound, it is desirable to determine it by conducting an experiment in advance. Generally, 5 minutes to 200 hours and about 1 hour to 50 hours are suitable. Either a flow system or a batch system can be adopted as the reaction mode.

紫外線照射における温度はパーフルオロ有機化合物の分
解を抑制し、本発明の効果を十分に発揮させるために、
好ましくは10〜200℃、さらに好ましくは50〜150℃の間
から選択される。
The temperature in ultraviolet irradiation suppresses the decomposition of the perfluoroorganic compound, and in order to sufficiently exert the effects of the present invention,
It is preferably selected from 10 to 200 ° C, more preferably 50 to 150 ° C.

紫外線処理後、必要に応じて、紫外線処理によって遊離
したフッ化水素を中和若しくは吸着等の方法により取り
除いてもよい。
After the ultraviolet ray treatment, hydrogen fluoride liberated by the ultraviolet ray treatment may be removed by a method such as neutralization or adsorption, if necessary.

〔効果〕〔effect〕

炭化水素化合物やアミノ化合物等の有機化合物のフッ素
化により得られたパーフルオロ有機化合物を含むフッ素
化生成物を、そのまま沸点或いは沸点をこえる高温に加
熱するとフッ化水素が発生し、加熱を長時間続けてもフ
ッ化水素は微量ではあるが発生し続ける。ところが、本
発明の方法により紫外線照射処理されたフッ素化生成物
は、加熱によっても実質的にフッ化水素を発生しない。
When a fluorinated product containing a perfluoroorganic compound obtained by fluorinating an organic compound such as a hydrocarbon compound or an amino compound is heated as it is to the boiling point or a high temperature above the boiling point, hydrogen fluoride is generated and the heating is performed for a long time. Even if it continues, a small amount of hydrogen fluoride continues to be generated. However, the fluorinated product that has been subjected to the ultraviolet irradiation treatment by the method of the present invention does not substantially generate hydrogen fluoride even when heated.

本発明の方法により処理されたフッ素化生成物は、フッ
化水素の発生がほとんどないため、気相ハンダ付用熱媒
体、電子部品の試験用媒体、人工血液等として好適に使
用することができる。
Since the fluorinated product treated by the method of the present invention hardly generates hydrogen fluoride, it can be preferably used as a heat medium for vapor phase soldering, a test medium for electronic components, artificial blood, etc. .

〔実施例〕〔Example〕

本発明をさらに具体的に説明するために以下実施例を掲
げるが、本発明はこれらの実施例に限定されるものでは
ない。
The following examples are provided to describe the present invention more specifically, but the present invention is not limited to these examples.

実施例1 無水フッ化水素酸と表1に示す三種のトリアルキルアミ
ンを原料とし、後者の濃度を10重量%として、ニッケル
製電解槽(電極面積10dm2、電流20A容量3.5lを用いて電
解フッ素化を開始した。無水フッ化水素酸とトリアルキ
ルアミンを連続的に供給しながら、生成するフッ素化物
を電解槽の下部より間欠的に抜き出した。これを40重量
%の水酸化ナトリウム水溶液とジイソブチルアミンの等
容量混合物中で120時間還流して、パーフルオロロリア
ルキルアミンを主成分とするフッ素化生成物を得た。
Example 1 Anhydrous hydrofluoric acid and three kinds of trialkylamines shown in Table 1 were used as raw materials, and the concentration of the latter was set to 10% by weight, and electrolysis was performed using a nickel electrolytic cell (electrode area 10 dm 2 , current 20 A capacity 3.5 l). Fluorination was started.While continuously supplying anhydrous hydrofluoric acid and trialkylamine, the resulting fluorinated product was intermittently withdrawn from the lower portion of the electrolytic cell with 40% by weight aqueous sodium hydroxide solution. Refluxing in an equal volume mixture of diisobutylamine for 120 hours gave a fluorinated product based on perfluorolollyalkylamine.

得られたフッ素化生成物150gを、還流冷却器、外装式温
度調節器、撹拌器、および40mmφの円盤状の石英ガラス
とテトラフルオロエチレン−パーフルオロアルキルビニ
ルエーテル共重合体を重ね合わせた窓を有する150mlス
テンレス製容器に入れ、1cmの距離から超高圧水銀ラン
プ(ウシオ電機製USH-250D、250W)にて表1に示す条件
で撹拌しながら紫外線を照射した。いずれの場合も紫外
線の照射後の回収率は、照射前を基準にしてほぼ100%
で、組成の変化もほとんどみられなかった。
150 g of the obtained fluorinated product was provided with a reflux condenser, an exterior temperature controller, a stirrer, and a window in which 40 mmφ disc-shaped quartz glass and tetrafluoroethylene-perfluoroalkyl vinyl ether copolymer were superposed. It was placed in a 150 ml stainless steel container, and irradiated with ultraviolet rays from a distance of 1 cm while stirring with an ultra-high pressure mercury lamp (USH-250D, 250W manufactured by Ushio Inc.) under the conditions shown in Table 1. In both cases, the recovery rate after UV irradiation is almost 100% based on that before irradiation.
Therefore, almost no change in composition was observed.

紫外線照射処理をしたフッ素化生成物100gを、還流器を
上部分に配した200mlのナス型フラスコに入れて加熱
し、5時間大気圧下で沸騰させた。この間、80ml/min流
量の窒素ガスを液に吹き込み、発生するフッ化水素を50
mlの0.01Nの水酸化カリウム水溶液に吸収させた。この
水酸化カリウム水溶液に含まれるフッ素イオン濃度をイ
オンクロマトアナライザー(横河北辰電機製、モデルIC
100)で測定することによりフッ化水素発生量を求め、
フッ素化生成物単位重量当たりのフッ化水素発生量〔mg
−(HF)/kg−(フッ素化生成物)〕を算出した。な
お、この値を沸騰時フッ化水素発生量と呼ぶことにす
る。
100 g of the fluorinated product which had been subjected to ultraviolet irradiation was placed in a 200 ml eggplant-shaped flask having a reflux condenser in the upper part, heated, and boiled under atmospheric pressure for 5 hours. During this period, nitrogen gas at a flow rate of 80 ml / min was blown into the liquid to generate 50% hydrogen fluoride.
It was absorbed in ml of 0.01 N potassium hydroxide aqueous solution. Ion chromatographic analyzer (Yokogawa Kitatsuden, model IC
100) to determine the amount of hydrogen fluoride generated,
Amount of hydrogen fluoride generated per unit weight of fluorinated product [mg
-(HF) / kg- (fluorinated product)] was calculated. This value will be called the amount of hydrogen fluoride generated during boiling.

表1には比較のために紫外線照射を行なわなかった場合
の、沸騰時フッ化水素発生量も併せて記した。
For comparison, Table 1 also shows the amount of hydrogen fluoride generated during boiling when ultraviolet irradiation was not performed.

実施例2 表2に示す二種の有機化合物のフッ素化を三フッ化コバ
ルトを用いて行なった。1.8kgの三フッ化コバルト粉末
を充填した撹拌機付きのニッケル製反応器(長さ50cm、
内径9cm)を270℃に加熱し、反応器の一端より有機化合
物を気化させて窒素ガスと共に供給した。反応器より流
出するフッ素化生成物を冷却トラップで凝縮し窒素ガス
等を分離した。反応後、フッ素化生成物に含まれる大部
分のフッ化水素を窒素ガスでバブリングすることにより
除いたのちに、残存するフッ化水素を30%水酸化カリウ
ム水溶液で中和、水洗、塩化カルシウムで乾燥を行な
い、蒸留によって表2に示すパーフルオロ有機化合物を
主成分とするフッ素化生成物を得た。
Example 2 Two organic compounds shown in Table 2 were fluorinated with cobalt trifluoride. Nickel reactor with a stirrer filled with 1.8 kg of cobalt trifluoride powder (length 50 cm,
(Inner diameter 9 cm) was heated to 270 ° C., an organic compound was vaporized from one end of the reactor and supplied together with nitrogen gas. The fluorinated product flowing out from the reactor was condensed with a cooling trap to separate nitrogen gas and the like. After the reaction, most of the hydrogen fluoride contained in the fluorinated product was removed by bubbling with nitrogen gas, and the remaining hydrogen fluoride was neutralized with a 30% aqueous potassium hydroxide solution, washed with water, and washed with calcium chloride. After drying and distillation, a fluorinated product containing a perfluoroorganic compound shown in Table 2 as a main component was obtained.

得られたフッ素化生成物を実施例1に示す同様な方法で
表2に示す条件のもとに紫外線照射を行なったのち、沸
騰時フッ化水素発生量を測定した。結果を表2に示し
た。尚、いずれの場合も紫外線の照射後の回収率は、照
射前を基準にしてほぼ100%で、組成の変化もほとんど
みられなかった。
The obtained fluorinated product was irradiated with ultraviolet rays in the same manner as in Example 1 under the conditions shown in Table 2, and then the amount of hydrogen fluoride generated during boiling was measured. The results are shown in Table 2. In each case, the recovery rate after irradiation with ultraviolet rays was almost 100% based on that before irradiation, and almost no change in composition was observed.

表2には比較のために紫外線照射を行なわなかった場合
の、沸騰時フッ化水素発生量も併せて記した。
For comparison, Table 2 also shows the amount of hydrogen fluoride generated at the time of boiling when ultraviolet irradiation was not performed.

───────────────────────────────────────────────────── フロントページの続き (51)Int.Cl.5 識別記号 庁内整理番号 FI 技術表示箇所 C07C 209/90 9280−4H 211/15 9280−4H // A61K 9/107 K 7329−4C ─────────────────────────────────────────────────── ─── Continuation of the front page (51) Int.Cl. 5 Identification number Reference number within the agency FI Technical indication C07C 209/90 9280-4H 211/15 9280-4H // A61K 9/107 K 7329-4C

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】炭化水素化合物又はアミノ化合物のフッ素
化によって得た、実質的にパーフルオロ化合物よりなる
反応生成物に、フッ素化剤を加えることなく、紫外線を
照射することを特徴とするパーフルオロ化合物の安定化
方法
1. A perfluoro compound, which is obtained by fluorinating a hydrocarbon compound or an amino compound, and which is irradiated with ultraviolet rays without adding a fluorinating agent to a reaction product consisting essentially of the perfluoro compound. Method of stabilizing compounds
JP1328225A 1989-12-20 1989-12-20 Method for stabilizing perfluoro compound Expired - Lifetime JPH0684316B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP1328225A JPH0684316B2 (en) 1989-12-20 1989-12-20 Method for stabilizing perfluoro compound

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP1328225A JPH0684316B2 (en) 1989-12-20 1989-12-20 Method for stabilizing perfluoro compound

Publications (2)

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JPH03190826A JPH03190826A (en) 1991-08-20
JPH0684316B2 true JPH0684316B2 (en) 1994-10-26

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Country Status (1)

Country Link
JP (1) JPH0684316B2 (en)

Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH07121881B2 (en) * 1991-03-26 1995-12-25 信越化学工業株式会社 Method for removing iodine contained in ethylene compound having fluorinated organic group
DE4116121A1 (en) * 1991-05-17 1992-11-19 Hoechst Ag METHOD FOR THE CLEANING OF MIXTURES THAT SUBSTANTIALLY consist of PERFLUORED ALKYLBROMIDES OR ALKYLENE DIBROMIDS

Family Cites Families (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2502999B2 (en) * 1987-01-31 1996-05-29 三菱化学株式会社 Process for producing aromatic fluorides
JPS6471824A (en) * 1987-09-11 1989-03-16 Mitsubishi Chem Ind Production of aromatic fluoride
JPH01233232A (en) * 1988-03-12 1989-09-19 Mitsubishi Kasei Corp Production of aromatic compound nucleus-substituted with hydroxyl group and fluorine atom

Also Published As

Publication number Publication date
JPH03190826A (en) 1991-08-20

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