TW593301B - Processes for producing fluorinated cyclic ethers and use thereof - Google Patents

Processes for producing fluorinated cyclic ethers and use thereof Download PDF

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TW593301B
TW593301B TW91103039A TW91103039A TW593301B TW 593301 B TW593301 B TW 593301B TW 91103039 A TW91103039 A TW 91103039A TW 91103039 A TW91103039 A TW 91103039A TW 593301 B TW593301 B TW 593301B
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compound
formula
following formula
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TW91103039A
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Hidekazu Okamoto
Takashi Okazoe
Kunio Watanabe
Masahiro Ito
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Asahi Glass Co Ltd
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    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07DHETEROCYCLIC COMPOUNDS
    • C07D307/00Heterocyclic compounds containing five-membered rings having one oxygen atom as the only ring hetero atom
    • C07D307/02Heterocyclic compounds containing five-membered rings having one oxygen atom as the only ring hetero atom not condensed with other rings
    • C07D307/26Heterocyclic compounds containing five-membered rings having one oxygen atom as the only ring hetero atom not condensed with other rings having one double bond between ring members or between a ring member and a non-ring member
    • C07D307/30Heterocyclic compounds containing five-membered rings having one oxygen atom as the only ring hetero atom not condensed with other rings having one double bond between ring members or between a ring member and a non-ring member with hetero atoms or with carbon atoms having three bonds to hetero atoms with at the most one bond to halogen, e.g. ester or nitrile radicals, directly attached to ring carbon atoms

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

Abstract

This invention provides processes for producing a useful, fluorinated, unsaturated, cyclic ether and a useful fluorinated, saturated, cyclic ether from inexpensive materials; an effective use of the fluorinated, unsaturated, cyclic ether and the fluorinated, saturated, cyclic ether; and a novel compound which is useful as an intermediate for these ethers. A compound (5) shown below is thermally decomposed to obtain at least one fluorinated, unsaturated, cyclic ether selected between the compound (6a) and compound (6b) shown below. Reducing the fluorinated, unsaturated, cyclic ether gives at least one fluorinated, saturated, cyclic ether selected between the compound (7a) and compound (7b) shown below. In the formula (5), AF represents perfluorotetrahydrofuranyl and X represents fluorine or -O<->M<+> (in which M<+> represents a counter ion).

Description

593301 A7 __ B7_ 五、發明説明() 本發明係有關工業上有用之氟化環狀不飽和醚及氟化 飽和環狀醚(以下稱此等爲氟化環狀醚)之製造方法及其 用途,以及做爲該氟化環狀醚之製造中間體有用之新穎化 合物者。 先行技術中,做爲氟化環狀醚之合成法者如以下方法 爲公知者。 (1 )四氫呋喃與c〇F 3進行反應之方法(Journal of chemical Soc· C. 1969,(13),1739 )。惟,該方法中產生 3 0以上之化合物,出現目的物選擇性極低之問題點。 (2 )於K 2 C〇3之存在下,使全氟(四氫呋喃基一 2 -羧酸)之鉀鹽進行熱分解之方法(Zh.〇i*g. Khim., 1 977,13 (12),2573 )。惟,全氟(四氫呋喃基—2 —羧酸 )之鉀鹽不易取得,因此,該方法不易做爲工業製造之適 用者。 亦即,先行之氟化環狀醚製造方法其收率極低, 極爲不易,務必使用高價原料等問題點存在,無工 業上可實施之製造方法者。 本發明係提供一種適於工業上實施之方法,且,有利 於經濟面之方法,製造收率良好之氟化環狀醚方法者。 &lt;發明開示&gt; 本發明係提供一種利用可廉價取得之化合物,製造做 爲功能劑等有用之氟化環狀醚之方法。更提供一種藉由再 循環該製造方法之酯分解反應步驟中取得之氟酸鹽化合物 本紙張尺度適财關家標準(CNS ) A4規格(210X297公釐) ' ' &gt;4- (請先閲讀背面之注意事項再填寫本頁) 訂 經濟部智慧財產局員工消費合作社印製 經濟部智慧財產局員工消費合作社印製 593301 A7 __ B7 五、發明説明(》 後’進行工業上有用之連續流程者。本發明更提供做爲氟 化環狀醚製造中間體有用之新穎化合物者。藉由本發明發 現所製造之氟化環狀醚具有做爲氯氟碳類(C F C )代替 化口物之良好k丨生’其臭氧破壞係數(◦ D p )爲零者, 地球溫暖化係數(G W P )亦爲極小之化合物者,利用此 氟化環狀醚提供有效之用途者。 亦即’本發明係提供由以下構成組成之各發明者。 1 ·將下式(5 )所示化合物進行熱分解後,取得工 種以上下式(6 a )所示化合物及下式(6 b )所示化合 物之氟化不飽和環狀醚者爲特徵之氟化不飽和環狀醚製造 方法者。 惟,A F代表全氟四氫呋喃基。:κ代表氟原子或 —〇—Μ +(惟,Μ +爲離子。)者。 AF COX (5)593301 A7 __ B7_ V. Description of the invention () The present invention relates to the industrially useful methods for the production of fluorinated cyclic unsaturated ethers and fluorinated saturated cyclic ethers (hereinafter referred to as fluorinated cyclic ethers) and uses thereof. And novel compounds useful as intermediates for the production of the fluorinated cyclic ether. In the prior art, a method for synthesizing a fluorinated cyclic ether is known as follows. (1) A method for reacting tetrahydrofuran with coF 3 (Journal of chemical Soc. C. 1969, (13), 1739). However, more than 30 compounds are produced in this method, and there is a problem that the selectivity of the target is extremely low. (2) A method for thermally decomposing a potassium salt of perfluoro (tetrahydrofuranyl 2-carboxylic acid) in the presence of K 2 C03 (Zh.〇i * g. Khim., 1 977, 13 (12 ), 2573). However, the potassium salt of perfluoro (tetrahydrofuran-2-carboxylic acid) is not easy to obtain, therefore, this method is not easy to be used as an industrially applicable one. That is, the prior fluorinated cyclic ether production method has extremely low yield and is extremely difficult. There must be problems such as the use of expensive raw materials, and there is no industrially feasible production method. The present invention provides a method suitable for industrial implementation and a method which is economically advantageous and a method for producing a fluorinated cyclic ether with good yield. &lt; Invention of the invention &gt; The present invention provides a method for producing a useful fluorinated cyclic ether, such as a functional agent, using a compound which can be obtained at a low cost. It also provides a fluorate compound obtained by recycling the ester decomposition reaction step of the manufacturing method. This paper is sized to a suitable financial standard (CNS) A4 specification (210X297 mm) '' &gt; 4- (Please read first Note on the back, please fill out this page again) Order printed by the Ministry of Economic Affairs Intellectual Property Bureau employee consumer cooperative printed by the Ministry of Economic Affairs Intellectual Property Bureau employee consumer cooperative printed by 5330301 A7 __ B7 V. Description of the invention ("After the process of industrially useful continuous process The present invention further provides novel compounds useful as intermediates for the production of fluorinated cyclic ethers. The fluorinated cyclic ethers produced by the present invention have good properties as chlorofluorocarbons (CFCs) instead of chemical compounds Those whose ozone destruction coefficient (◦ D p) is zero and those whose global warming coefficient (GWP) is also extremely small, use this fluorinated cyclic ether to provide effective applications. That is, the present invention provides Each inventor consists of the following components: 1 · After thermally decomposing a compound represented by the following formula (5), fluorine of the compound represented by the following formula (6 a) and the compound represented by the following formula (6 b) is obtained. A method for producing a fluorinated unsaturated cyclic ether characterized by converting an unsaturated cyclic ether. However, AF represents a perfluorotetrahydrofuranyl group: κ represents a fluorine atom or -0-M + (However, M + is an ion.) By AF COX (5)

2 ·式(5 )所示之化合物爲下式(5 a )所代表化 合物之該1之製造方法者。 本紙張尺度適用中國國家標準(CMS ) A4規格(210X297公釐) (請先閱讀背面之注意事項再填寫本頁)2. The method for producing a compound represented by the formula (5) is the compound represented by the following formula (5a). This paper size applies Chinese National Standard (CMS) A4 specification (210X297 mm) (Please read the precautions on the back before filling this page)

-5- 593301 A7 B7 五、發明説明()-5- 593301 A7 B7 V. Description of the invention ()

3 ·式(5 )所代表化合物中X爲氟原子之下式(5 f )所示化合物者,而以下式(1 )所示化合物與下式( 2 )所示化合物做爲所反應之下式(3 )所示化合物者, 以該式(3 )所示化合物做爲氟化後之下式(4 )所示化 合物後’該式(4 )所示化合物之醚結合進行分解反應後 取得化合物之該1或2所載之製造方法者。 惟,A F與上述意義相同。r c代表1價有機基。r c F 與R e同- 1價有機基、或R C代表被氟化之1價有機基者 。乂1爲鹵原子。A爲選自下式(la)、下式(lb)、 下式(lc)、及下式(Id)之式所代表之基、或所選 取式中之氫原子1個以上被氟原子取代之式所示之基者。 A C H 9 〇 H ( 1 ; ) R c C 〇 X 1 ( 2 ) A c H 9 〇 C〇R c ( 3 ) A F C F 0 0 C 0 R c F ( 4 ) A F C 〇 F ( 5 f3. In the compound represented by formula (5), X is a compound represented by formula (5 f) below a fluorine atom, and the compound represented by formula (1) below is reacted with the compound represented by formula (2) below. For the compound represented by formula (3), the compound represented by formula (3) is used as the compound represented by formula (4) after fluorination. The compound is produced by the method described in 1 or 2. However, A F has the same meaning as above. r c represents a monovalent organic group. r c F is the same as Re e-monovalent organic group, or R C represents a fluorinated monovalent organic group.乂 1 is a halogen atom. A is selected from the group represented by the following formula (la), (lb), (lc), and (Id), or one or more hydrogen atoms in the selected formula are substituted by fluorine atoms The one shown in the formula. A C H 9 〇 H (1;) R c C 〇 X 1 (2) A c H 9 〇 C〇 R c (3) A F C F 0 0 C 0 R c F (4) A F C 〇 F (5 f

Q C (la) (lb) (ic) ㈤) 4 .式(1 )所代表之化合物爲下式(i )所示化合 物者、式(3 )所代表之化合物爲下式(3 )所示化合物 本紙張尺度適用中國國家標準(CNS ) A4規格(21〇X297公釐) -----------壯衣-- {請先閲讀背面之注意事項再填寫本頁} -訂 經濟部智慧財產局員工消費合作社印製 -6 - 593301 A7 ____B7 ___ 五、發明説明(4 ) 者、式(4 )所代表化合物中a F爲2 -全氟四氫呋喃基者 、式(5 ί )所代表化合物爲下式(5 a )所示化合物之 該3所記載之製造方法。 惟’ R e與上記爲相同意義者。A 1係選自下式(1 a 一 1)、下式(lb — 1)、下式(lc 一 1)、及下式 (1 d - 1 )之式所代表之基、或該選取之式中氫原子1 個以上被氟原子取代之式所示之基者。 A 1 C Η 2 Ο Η ( 1 ) A 1 C Η 2 0 C 0 R c ( 3 ) (請先閱讀背面之注意事項再填寫本頁)QC (la) (lb) (ic) ㈤) 4. The compound represented by formula (1) is a compound represented by the following formula (i), and the compound represented by formula (3) is a compound represented by the following formula (3) This paper size applies the Chinese National Standard (CNS) A4 specification (21〇297mm) ----------- Zhuang Yi-{Please read the precautions on the back before filling this page}-Order economy Printed by the Consumer Cooperatives of the Ministry of Intellectual Property Bureau-6-593301 A7 ____B7 ___ V. Inventor (4), the compound represented by formula (4) where a F is 2-perfluorotetrahydrofuranyl, formula (5 ί) The production method described in the above 3, wherein the representative compound is a compound represented by the following formula (5a). However, 'R e has the same meaning as the above. A 1 is selected from the group represented by the following formula (1 a-1), the following formula (lb-1), the following formula (lc-1), and the following formula (1 d-1), or the selected one In the formula, one or more hydrogen atoms are replaced by a fluorine atom. A 1 C Η 2 Ο Η (1) A 1 C Η 2 0 C 0 R c (3) (Please read the notes on the back before filling this page)

(lc一 1〉(lc-1 1>

、1T, 1T

經濟部智慧財產局員工消費合作社印製 5 .式(3 )所不之化合物係由使式(4 )所示化合 物之酯結合進行分解反應之反應生成物取得式(5 )所示 示化合物與下式(2 a )所示化合物進行反應後取得化合 物之該3或4所載之製造方法。 惟,R e F與上記意義相同者。 R c F C 〇 F (2a) δ .使氟化於液相中與氟反應後進行之該3 ,4或5 所載之製造方法者。 7 ·下式(5 )所示化合物經熱分解後取得丄種以上 本紙張尺度適用中國國家標準(CNS ) A4規格(210X297公釐) 593301 A7 B7 五、發明説明(&amp; 選自下式(6 a )所示化合物及下式(6 b )所示化合物 之化合物後,再進行該1種以上化合物之還原反應後,取 得1種以上選自式(· 6 a )所示化合物爲被還原下式(7 a )所代表之化合物及式(6 b )所示化合物被還原之式 (7 b )所代表化合物之氟化飽和環狀醚者爲特徵之氟化 飽和環狀醚製造方法。 惟,A F及X分別與上述之意義爲相同者。 AFC〇X (5)Printed by the Consumer Cooperatives of the Intellectual Property Bureau of the Ministry of Economic Affairs 5. Compounds not represented by formula (3) are obtained by reacting the reaction product of the compound represented by formula (4) with a decomposition reaction to obtain the compound represented by formula (5) and The method described in 3 or 4 for obtaining the compound after reacting the compound represented by the following formula (2a). However, R e F has the same meaning as the above. R c F C 〇 F (2a) δ. The production method described in 3, 4 or 5 which is performed after reacting fluorination with fluorine in the liquid phase. 7 · The compound represented by the following formula (5) is thermally decomposed to obtain more than one species. The paper size is applicable to the Chinese National Standard (CNS) A4 (210X297 mm) 593301 A7 B7 5. Description of the invention (&amp; selected from the following formula ( After the compound represented by 6 a) and the compound represented by the following formula (6 b) is subjected to a reduction reaction of the one or more compounds, one or more compounds selected from the formula (· 6 a) are obtained. A method for producing a fluorinated saturated cyclic ether characterized by a compound represented by the following formula (7 a) and a compound represented by the formula (6 b) which is reduced by a fluorinated saturated cyclic ether of the compound represented by the formula (7 b). However, AF and X have the same meanings as above. AFC〇X (5)

(6a) F H (7a)(6a) F H (7a)

(6b)(6b)

(Tb) 8 ·式(5 )所示化合物爲下式 之該7之製造方法。 所示化合物 (請先閲讀背面之注意事項再填寫本頁)(Tb) 8 A method for producing a compound represented by the formula (5) in which 7 is represented by the following formula. Compounds shown (Please read the notes on the back before filling out this page)

-、1T 經濟部智慧財產局員工消費合作社印製-、 1T Printed by the Consumer Cooperative of Intellectual Property Bureau of the Ministry of Economic Affairs

(5a) COF •下式所示任一化合物 ΓΛ 、〇/'CH2OCORcl Nv〇/^ch2ocorC1 (3a-2〉 (3b-2)(5a) COFA compound of any one of the formula ΓΛ, 〇 / 'CH2OCORcl Nv〇 / ^ ch2ocorC1 (3a-2> (3b-2)

CFl 本紙張尺度適用中國國家標準(CNS ) A4規格(210Χ297公釐) -8- 593301 A7 B7 五、發明説明($ 惟’ R ° 1及R u F 1代表全氟烷基、全氟(部份氯烷基 )基、全氟(含醚性氧原子之烷基)基、全氟(部份氯( 含醚性氧原t之院基))基、或全集四氫咲喃基者。 1 0 .含有1種以上選自下式(6 a )所示化合物及 下式(6 b )所示化合物之氟化不飽和環狀醚、或1種以 上選自下式(7 a )所示化合物及下式(7 b )所示化合 物之氟化飽和環狀醚之功能劑。CFl This paper size is applicable to Chinese National Standard (CNS) A4 specification (210 × 297 mm) -8- 5933301 A7 B7 V. Description of the invention ($ ', but R ° 1 and R u F 1 represent perfluoroalkyl, perfluoro (part Part of chloroalkyl) group, perfluoro (alkyl group containing etheric oxygen atom) group, perfluoro (part of chlorine (group containing etheric oxygen atom t)) group, or the complete tetrahydrofuranyl group. 10. A fluorinated unsaturated cyclic ether containing one or more compounds selected from the compound represented by the following formula (6 a) and the compound represented by the following formula (6 b), or one or more members selected from the group consisting of the following formula (7 a) A functional agent of a fluorinated saturated cyclic ether of the compound shown and the compound represented by the following formula (7b).

1 1 .含有下式(7 a )所示化合物之功能劑。 (讀先聞讀背面之注意事項再填寫本頁) |嫌|1 1. A functional agent containing a compound represented by the following formula (7a). (Read the notes on the back and then fill out this page) |

、1T, 1T

經濟部智慧財產局員工消費合作社印製 1 2 ·去水乾燥溶劑、乾蝕刻劑、或洗淨劑之該1 〇 或1 1之功能劑。 &lt;發明實施之最佳形態&gt; 以下之本明細書說明中,式(5 )所示化合物記爲化 -合物(5 )。其他式所示化合物亦同法記之。 本:發明中’使下記化合物(5 )進行熱分解後取得1 -9- 593301 A7 B7 五、發明説明(、 種以上選自下記化合物 氟化不飽和環狀醚者。 及下記化合物(6 b )之 (5)Printed by the Consumer Cooperatives of the Intellectual Property Bureau of the Ministry of Economic Affairs 1 2 · The 10 or 11 functional agent in dehydration solvent, dry etchant, or detergent. &lt; Best mode for carrying out the invention &gt; In the following detailed description of the book, the compound represented by the formula (5) is referred to as a compound (5). The compounds represented by other formulas are also recorded by the same method. This: In the invention, 'The following compound (5) is thermally decomposed to obtain 1 -9-593301 A7 B7 5. Description of the invention (, more than one selected from the following compounds fluorinated unsaturated cyclic ethers. And the following compound (6 b ) Of (5)

AFC〇XAFC〇X

㈣ F㈣ F

F 〇 (6b) (請先閱讀背面之注意事項再填寫本頁) -裝- 訂 式(5 )中之A F代表全氟四氫咲喃基。化合物(5 ) 中之一 C〇X基可結合於全氟四氫呋喃基(A F )之2位、 或結合於3位均可,而結合於2位者爲較佳。亦即,做爲 A F者以2 -全氟四氫呋喃基者宜,做爲化合物(5 )者以 下記化合物(5 a )者宜。F 〇 (6b) (Please read the precautions on the back before filling out this page)-Equipment-Order A in Formula (5) represents perfluorotetrahydrosulfanyl. One of the compounds (5) may be bonded to the COX group at the 2-position or the 3-position of the perfluorotetrahydrofuranyl (A F) group, and it is preferable to bind to the 2-position. That is, it is preferable to use 2-perfluorotetrahydrofuranyl as the A F, and it is preferable to use the compound (5 a) below as the compound (5).

經濟部智慧財產局員工消費合作社印製 X代表氟原子或一 ◦ _ Μ +者。Μ +係選自可形成羧酸 與鹽之陽離子者,以鹼金屬陽離子者宜,Κ +、Na +爲特 別理想者。化合物(5 )中,X爲一〇_ Μ +之化合物之製 造方法者係其化合物(5 )之X爲氟原子之化合物(5 f )之一 C〇F基變換成一 C〇〇Η後形成鹽之方法、或該 化合物(5 f )中反應2倍莫耳以上之Μ〇Η ( Μ係陽離 子爲該Μ +者,以鹼金屬原子者宜。)之後,減壓下進行加 本紙張尺度適用中國國家標準(CNS ) A4規格(210X297公釐) -10- 593301 A7 _____B7__ 五、發明説明(令 熱乾燥之方法者宜。 (請先閱讀背面之注意事項再填寫本頁) 熱分解反應之基質化合物(5 )中,X爲氟原子之下 記化合物(5 f )係以化合物(1 )與化合物(2 )做爲 所反應化合物(3 )者,以該化合物(3 )做爲氟化化合 物(4 )者,該化合物(4 )之酯結合經分解反應後所取 得之化合物者宜。惟,A F與上記意義爲相同者。R e代表 1價有機基。R e F與R e爲相同之1價有機基、或R e代表 被氟化之1價有機基者。X1爲鹵原子者。A爲選自下式( 1 a )、下式(1 b )、下式(1 c ) '及下式(1 d ) 之式所代表之基、或所選取式中之1個氫原子以上被氟原 子取代之式所代表之基者。 A C Η 2 Ο Η ( 1 ) R c C 〇 X 1 ( 2 ) A C H 2 0 C 0 R c ( 3 ) A F C F 2 0 C 0 R c F ( 4 ) A F C 〇 F ( 5 f ) 經濟部智慧財產局員工消費合作社印製 Θ (la) (lb) (lc) (Id) 又,化合物(5 )之X爲-〇_ M +之化合物可由該化 合物(5 ί )製造該方法者。 化合物(1 )與化合物(2 )之酯化反應、化合物( 3 )之氟化反應以及化合物(4 )之酯結合分解反應可與 藉由本發明者之WO 〇 〇/5 6 6 9 4所載之各反應方 本紙張尺度適用中.國國家標準(CNS ) Α4規格(210 X 297公釐) -11 - 593301 A7 _______B7 --- 五、發明説明($ 法相同手段及條件下進行之。該方法可由廉價化合物 )及化合物(2 )以極佳效率製造工業用化合物(5 ) 該式(1 a )〜式(1 d )中,由環所延伸之線爲結 合手者,(結合手所結合之5員環碳原子位置不被限定之 。),且,此等基爲1價基者。亦即,化合物(1 )係代 表結合於一 C Η 2〇Η基爲式(1 a )〜式(1 c )所示基 之2位或3位之化合物或任意結合於其- C Η 2 〇 Η基爲式 (1 d )所示基之2位〜5位之化合物者。 A係於2位具有與- C Η 2〇Η相互之結合手之基者, 亦即,選自下式(la — 1)、下式(la - 2)、下式 (la — 3)、以及下式(la - 4)之式所示之基、或 該選取之式中1個以上之氫原子爲被氟原子取代之式所禾 之基(A 1 )者宜。 (請先閲讀背面之注意事項再填寫本頁}Printed by the Consumer Cooperative of the Intellectual Property Bureau of the Ministry of Economic Affairs. X stands for fluorine atom or a ◦ Μ +. M + is selected from those which can form carboxylic acid and salt cations, and alkali metal cations are preferred, and K + and Na + are particularly desirable. Among the compounds (5), a method for producing a compound in which X is 10-M + is that a COF group of the compound (5) in which X is a fluorine atom is converted into a COF group. The method of salt, or the reaction of mol more than 2 moles in the compound (5 f) (M type cation is the M +, preferably alkali metal atom.), Then the paper size is added under reduced pressure. Applicable to China National Standard (CNS) A4 specification (210X297 mm) -10- 593301 A7 _____B7__ V. Description of the invention (please make the method of heat drying. (Please read the precautions on the back before filling this page) In the matrix compound (5), X is a fluorine atom, and the compound (5f) is the compound (1) and the compound (2) as the reacted compound (3), and the compound (3) is used as the fluorinated compound. (4), the ester of the compound (4) is preferably obtained after the decomposition reaction of the compound. However, AF has the same meaning as above. Re represents a monovalent organic group. Re F and Re are the same. A monovalent organic group, or R e represents a fluorinated monovalent organic group. X1 is a halogen atom A is selected from the group represented by the following formula (1a), (1b), (1c) 'and (1d), or a hydrogen atom in the selected formula The base represented by the above formula substituted by a fluorine atom: AC Η 2 Ο Η (1) R c C 〇X 1 (2) ACH 2 0 C 0 R c (3) AFCF 2 0 C 0 R c F (4 ) AFC 〇F (5 f) Printed by the Consumer Cooperative of Intellectual Property Bureau of the Ministry of Economic Affairs Θ (la) (lb) (lc) (Id) In addition, the compound (5) where X is -0_M + (5) The method for producing the method. The esterification reaction of the compound (1) and the compound (2), the fluorination reaction of the compound (3), and the ester-combining decomposition reaction of the compound (4) can be combined with WO of the inventor. 〇 / 5 6 6 9 4 The paper size of each respondent is applicable. National National Standard (CNS) A4 Specification (210 X 297 mm) -11-593301 A7 _______B7 --- V. Description of Invention ($ Method It is performed under the same means and conditions. This method can produce industrial compound (5) from cheap compound) and compound (2) with excellent efficiency. In the formula (1 a) to (1 d), the ring extended For hand binding, (the position of the 5-membered ring carbon atom to which the binding hand is bound is not limited), and these groups are monovalent. That is, the compound (1) represents binding to a C Η 2 The 〇Η group is a compound at the 2 or 3 position of the group represented by the formula (1 a) to the formula (1 c) or any combination thereof-C Η 2 〇 Η group is the 2 position of the group shown by the formula (1 d) Compounds up to 5th place. A is at the base of two persons having a combination with-C Η 2〇Η, that is, selected from the following formula (la-1), (la-2), (la-3), And the base represented by the formula (la-4) below, or one or more hydrogen atoms in the selected formula is preferably the base (A 1) of the formula substituted by a fluorine atom. (Please read the notes on the back before filling this page}

Ό ^ Ο u (la-1) (lb -1) (Id〉 經濟部智慧財產局員工消費合作社印製 A代表不具氟原子之基者,亦即,選自式(1 a )、 式(1 b )、式(1 c )、及式(1 d )之式所示基考寬 ,特別以式(1 a )所示之基或式(1 b )所示之基爲胃 佳,更以式(1 a - 1 )所示之基或式(1 a — 2 ).所示 之基爲最佳。 做爲化合物(1 )之具體例者如下記化合物之例者。Ό ^ Ο u (la-1) (lb -1) (Id) printed by the Consumer Cooperative of the Intellectual Property Bureau of the Ministry of Economic Affairs on behalf of those who do not have a fluorine atom, that is, selected from formula (1 a), formula (1 b), the formula (1c), and the formula (1d) are shown in the formula, especially the formula (1a) or the formula (1b) is better for stomach, more preferably The base represented by the formula (1 a-1) or the base represented by the formula (1 a-2) is most preferable. Specific examples of the compound (1) are as follows.

本紙張尺度適用中.國國家標準(CNS ) A4規格(210X297公釐) -12- 經濟部智慧財產局員工消費合作社印製 593301 A7 B7 五、發明説明(10) 與化合物(1 )反應之化合物(2 )中,R e代表1價 有機基者。做爲R e者例,由對於用於氟化反應時之液相溶 解性之觀點視之,其碳數爲1〜2 0之基者宜,特別以碳 數1〜1 0之基爲更佳者。更且,做爲R e者以含有氟原子 之基(亦即,氟1價有機基)者宜,氟烷基、氟(部份氯 烷基)基、氟(含醚性氧原子之烷基)基、氟(部份氯( 含醚性氧原子之烷基)基、或後述之A F者佳。R e更以全 氟1價有機基者爲更佳,特別以全氟烷基、全氟(部份氯 烷基)基、全氟(含醚性氧原子之烷基)基、全氟(部份 氯(含醚性氧原子之烷基)基、全氟(部份氯(含醚性氧 原子之烷基)基、或後述之A F爲特別理想者。惟,被部份 氯化之基係指殘留氫原子之被氯取代之基者謂之。 做爲化合物(2 )之具體例者如下記化合物例者。惟 ,AF代表全氟四氫呋喃基、全氟(2 -四氫呋喃基)者宜 〇 CF3CF2COF ^ CF3CF2CF2〇CF(CF3)COF ^ CF3CF&gt;CF2〇CF(CF3)CF2〇CF(CF3)COF 'The standard of this paper is applicable. National Standard (CNS) A4 (210X297 mm) -12- Printed by the Consumer Cooperatives of the Intellectual Property Bureau of the Ministry of Economy 5933301 A7 B7 V. Description of the invention (10) Compounds that react with compound (1) In (2), R e represents a monovalent organic group. As an example of R e, from the viewpoint of the solubility in the liquid phase when used in a fluorination reaction, it is preferable that the carbon number is 1 to 20, and the carbon number 1 to 10 is more preferred. Best. In addition, it is preferable for Re to use a group containing a fluorine atom (that is, a fluorine monovalent organic group), a fluoroalkyl group, a fluorine (partial chloroalkyl) group, and a fluorine (an alkyl group containing an etheric oxygen atom). A radical is preferred, a fluorine (partially chlorinated (alkyl group containing etheric oxygen atom)) radical, or AF as described below. Re is more preferably a perfluoro monovalent organic radical, especially a perfluoroalkyl radical, Perfluoro (partially chloroalkyl) groups, perfluoro (partially chlorinated alkyl groups containing etheric oxygen atoms) groups, perfluoro (partially chlorinated (alkyl ether groups containing etheric oxygen atoms) groups, perfluoro (partially chlorinated alkyl groups) An alkyl group having an etheric oxygen atom, or AF described later is particularly desirable. However, a partially chlorinated group refers to a group substituted with chlorine for a residual hydrogen atom. As a compound (2) Specific examples are as follows for compound examples. However, AF represents perfluorotetrahydrofuryl and perfluoro (2-tetrahydrofuryl). CF3CF2COF ^ CF3CF2CF2CF (CF3) COF ^ CF3CF> CF2CF (CF3) CF2. CF (CF3) COF ''

AfC〇F 化合物(2 )亦可使用市販品者,亦可使用後述化合 物(4 )之酯結合分解反應中與化合物(5 )同時產生化 合物之化合物(2 a ) ( R c F c〇F ( 2 a ))者。使用 做爲化合物(2 )之化合物(2 a )之方法爲可連續性製 本紙張尺度適用中國國家標準(CNS ) A4規格(21〇&gt;&lt;297公^ &quot; ' β--·--,--、玎,----Φ---、 (請先閲讀背面之注意事項再填寫本頁) 593301 A7 ______B7 五、發明説明( (請先閲讀背面之注意事項再填寫本頁) 造方法者,因此特別理想。亦即,化合物(2 )中之R C係 與R e F爲相同之基者宜,特別是R C爲全氟1價有機基者 爲更佳。該全弗I 1價有機基之理想形態如上述。 又,化合物(2 )中,R c爲a F時,亦即,使用做爲 化合物(2 )之化合物(5 )時,其化合物(4 )之酯結 合分解反應生成物呈化合物(5 )者,具有不須分離生成 物步驟之優點爲理想者。 化合物(1 )與化合物(2 )相互之酯化反應可於溶 媒存在下進行之,惟,由容積效率面觀之,以溶媒不存在 下進行者爲較佳。又,化合物(1 )與化合物(2 )之反 應中,產生H F,因此,於反應系中亦可存在做爲η F收 集劑之鹼金屬氟化物(NaF、KF等者宜)、三院胺等 ’又以H F收集劑之存在爲較佳。若未使用η F收集劑時 ’使H F伴隨氮氣流排出反應系外者宜。使用鹼金屬氟化 物時之重爲化合物(2 )之1〜1 〇倍莫耳使用者宜。 經濟部智慧財產局員工消費合作社印製 化合物(1 )與化合物(2 )之反應溫度以一 5 0 °C 〜+ 1 0 0 °C者宜。又,該反應時間可依其原料供給速度 與反應所使用之化合物量進行適當變更。反應壓力(表壓 ’以下相同。)以0〜2MP a者宜。 化合物(1 )與化合物(2 )之量比針對化合物(1 )之化合物(2 )量以0 · 5〜5倍莫耳者宜,特別以1 〜2倍莫耳爲更佳。 化合物(1 )與化合物(2 )相互反應所生成之化合 物(3 )之粗生成物亦可依其目的進行精製之,亦可直接 本紙張尺度適用中國國家標準(CNS ) A4規格(210X297公釐) -14- 593301 A7 _B7___ 五、發明説明(12) 用於下個反應等,由安定以下步驟中氟化反應之觀點視之 ,該粗生成物中之化合物(3 )進行分離精製者宜。 (請先閲讀背面之注意事項再填寫本頁) 做爲該粗生成物之精製方法者如:直接蒸餾粗生成物 之方法,以稀鹼水等處理粗成物後進行分液之方法,以適 當有機溶媒萃取粗生成物後進行蒸餾之方法’矽膠柱體層 析法等例。 做爲化合物(3 )之具體例者如下記化合物之例。惟 ,八1及人「與上記意義相同。 CF3CF2CF2〇CF(CF3)C〇〇CH2A1、 CF3CF2CF2〇CF(CF3)CF3〇CF(CF3)COOCH2A1 ' A^OOCHiA1 經濟部智慧財產局員工消費合作社印製 本發明中,使化合物(3 )進行氟化。做爲贏化反應 之方法者如:利用C 〇 F 3進行之方法,利用E C F法、或 氟氣之方法例,於液相中導入氟氣後進行液相氟化法者宜 。氟化反應時,於化合物(3 )之分子中結合1原子以上 之氟原子。以下,使氟化反應藉由液相氟化反應進行之形 態舉例說明之。 液相氟化反應中氟氣體可直接使用,亦可以氮氣等不 活性氣體所稀釋之氟氣。使用被稀釋氟氣時該氟氣濃度爲 1 0 V ο 1 %以上者,特別以2 0 V ο 1 %以上爲最佳。 做爲液相者以由溶解氟(F 2 )取得之溶媒所形成者宜 。又溶媒以使用化合物(3 )之溶解性高溶媒者宜,又以 可溶解1質量%以上化合物(3 )之溶媒者,特別是可溶 ^氏張尺度適用中國國家標準(CNS ) A4規格(210X297公釐) ' - -15- 經濟部智慧財產局員工消費合作社印製 593301 Μ __Β7_ 五、發明説明()3 解5質量%以上之溶媒使用者最佳。溶媒量爲化合物(3 )之5倍質量以上者宜,特別爲1 0〜1 0 0倍質量者更 佳。 做爲可用於液相氟化之溶媒例者如:全氟鏈烷類、全 氟醚類、全氟聚醚類、氯氟碳類、氯氟聚醚類、全氟烷胺 、不活性流體等例,而,由易於反應後之後處理有利點觀 之特別以使用後述化合物(4 )、化合物(5 )、或化合 物(2 a )爲更佳。 化合物(3 )之氟含量(氟含量係指針對分子量之氟 原子質量比例)以1 0質量%以上者宜,特別以1 0〜 8 6質量%爲最佳者。當氟含量太少則對於液相中之溶解 性極低、氟化反應之反應系呈不均,於連續反應進行時無 法使化合物(3 )有效進料於反應中等問題點存在。又, 氟含量未限定上限,惟,太高則不易取得化合物(3 ), 價格太高,不經濟之問題點出現。 又,化合物(3)之分子量爲20 0〜1 〇〇〇者, 可防止氣相中不理想之氟化反應,可順利進行液相氟化反 應者。當分子量太小則化合物(3 )容易氣化,液相氟化 反應時恐於氣相中出現分解反應。反之,分子量太大則恐 造成化合物(3 )之精製困難。 氟化反應之反應形式可爲間歇式亦可爲連續式者。由 反應收率與選擇率之觀點視之,特別以連續式爲較佳者。 又,氟氣以間歇式進行,或以連續式進行時,均可使用以 氮氣等不活性氣體進行稀釋者。 本紙張尺度適用中國國家標準(CNS ) A4規格(210X297公釐) (請先閲讀背面之注意事項再填寫本頁)The AfC〇F compound (2) can also be used as a commercial product, or the compound (2a) (R c F c〇F ( 2 a)). The method of using the compound (2 a) as the compound (2) is to make the paper continuously. The paper size applies the Chinese National Standard (CNS) A4 specification (21〇 &gt; &lt; 297 公 ^ &quot; 'β-- ·- ,-, 玎, ---- Φ ---, (Please read the notes on the back before filling this page) 593301 A7 ______B7 V. Description of the invention ((Please read the notes on the back before filling this page) The method is particularly desirable. That is, it is preferable that the RC in the compound (2) is the same as that of R e F, and it is particularly preferable that RC is a perfluorinated monovalent organic group. The ideal form of the organic group is as described above. When compound R2 is a F in compound (2), that is, when compound (5) is used as compound (2), the ester-binding decomposition reaction of compound (4) is performed. If the product is a compound (5), it is desirable to have the advantage of not requiring a product separation step. The esterification reaction between the compound (1) and the compound (2) can be performed in the presence of a solvent, but from the volume efficiency side Obviously, it is better to carry out in the absence of a solvent. Also, in the reaction of the compound (1) and the compound (2) HF is generated, so in the reaction system, alkali metal fluorides (NaF, KF, etc.), ternary amines, etc., which are η F collectors, can also be present, and the presence of HF collectors is better. If When η F collector is not used, it is better to let HF out of the reaction system with nitrogen flow. The weight when using alkali metal fluoride is 1 to 10 times mole of compound (2). It is suitable for the user. The reaction temperature of compound (1) and compound (2) printed by employee consumer cooperatives is preferably between 50 ° C and +100 ° C. In addition, the reaction time can be based on the supply rate of the raw materials and the compounds used in the reaction The amount is appropriately changed. The reaction pressure (the gauge pressure is the same below) is preferably 0 to 2 MP a. The amount ratio of the compound (1) to the compound (2) is 0. 5 for the compound (2). It is preferred to be 5 times mole, especially 1 to 2 times mole. The crude product of compound (3) produced by the reaction of compound (1) and compound (2) can also be refined according to its purpose. , Or this paper size can be directly applied to Chinese National Standard (CNS) A4 specification (210X 297 mm) -14- 593301 A7 _B7___ 5. Explanation of the invention (12) Used in the next reaction, etc. From the viewpoint of stabilizing the fluorination reaction in the following steps, the compound (3) in the crude product is separated and purified. (Please read the precautions on the back before filling in this page) As the method for refining the crude product, such as the method of directly distilling the crude product, the crude product is treated with dilute alkali water and then liquid separation Methods: The method of extracting the crude product with an appropriate organic solvent and then performing distillation, such as silica gel column chromatography. Specific examples of the compound (3) are as follows. However, "Bao1 and Renren" has the same meaning as in the above. In the present invention, the compound (3) is fluorinated. As a method for winning the reaction, for example, a method using COF 3, a method using ECF method, or a method of fluorine gas, fluorine gas is introduced into the liquid phase. It is preferable to perform liquid phase fluorination method later. During the fluorination reaction, a fluorine atom of more than 1 atom is bonded to the molecule of the compound (3). Hereinafter, the form in which the fluorination reaction is carried out by liquid phase fluorination The fluorine gas in the liquid phase fluorination reaction can be used directly, or it can be diluted with inert gas such as nitrogen. When using the diluted fluorine gas, the fluorine gas concentration is 10 V ο 1% or more, especially 20 V ο is more than 1%. The liquid phase is preferably formed by a solvent obtained by dissolving fluorine (F 2). The solvent is preferably a solvent with a high solubility of the compound (3). 1% by mass or more of the solvent of the compound (3), especially soluble Applicable to China National Standard (CNS) A4 specification (210X297 mm) '--15- Printed by the Consumer Cooperatives of the Intellectual Property Bureau of the Ministry of Economic Affairs 5933301 Μ__Β7_ V. Description of the invention () 3 Solvent users who have more than 5 mass% The amount of solvent is preferably 5 times or more the mass of compound (3), especially 10 to 100 times the mass is more preferred. Examples of solvents that can be used for liquid phase fluorination are: perfluoroalkanes , Perfluoroethers, perfluoropolyethers, chlorofluorocarbons, chlorofluoropolyethers, perfluoroalkylamines, inactive fluids, etc., and it is easy to react and then deal with the advantages of the following points. The compound (4), the compound (5), or the compound (2a) is more preferable. The fluorine content of the compound (3) (the fluorine content refers to the mass ratio of fluorine atom to the molecular weight) is preferably 10% by mass or more, particularly 10 to 86% by mass is the best. When the content of fluorine is too small, the solubility in the liquid phase is extremely low, and the reaction system of the fluorination reaction becomes uneven, and the compound (3) cannot be made when the continuous reaction proceeds. The problem of effective feeding in the middle of the reaction exists. Moreover, the fluorine content is not The upper limit is set, but if it is too high, it is difficult to obtain the compound (3), the price is too high, and the problem of uneconomical appears. In addition, if the molecular weight of the compound (3) is 200 ~ 1000, it can prevent the Ideal fluorination reaction, can successfully carry out liquid phase fluorination reaction. When the molecular weight is too small, the compound (3) is easily gasified, and liquid phase fluorination reaction may cause decomposition reaction in the gas phase. On the contrary, if the molecular weight is too large, It may cause difficulty in refining the compound (3). The reaction form of the fluorination reaction may be batch or continuous. From the viewpoint of reaction yield and selectivity, continuous type is particularly preferred. In addition, when the fluorine gas is carried out in a batch type or in a continuous type, it is possible to use one diluted with an inert gas such as nitrogen. This paper size applies to China National Standard (CNS) A4 (210X297 mm) (Please read the precautions on the back before filling this page)

-16- 593301 A7 __ B7____ 五、發明説明()4 氟化反應中,針對化合物(3 )中之氫原子其氟量經 常使呈過剩當量置入氟氣體者宜’特別是使用1 . 5倍當 量以上(亦即,1 · 5倍莫耳以上)之氟氣者其選擇率較 爲理想。氟氣由反應開始至結束經常維持過剩當量者宜。 因此,將化合物(3 )導入溶解氟之液相中者宜。 液相氟化反應之反應溫度一般以- 6 0 t以上,且, 化合物(’3 )之沸點以下者宜,由反應收率、選擇率、及 工業上易於實施面觀之,又以一 5 0 t〜+ 1 〇 〇 °C爲較 佳,特別以一 2 0 °C〜+ 5 0 °C爲最佳。氟化反應之反應 壓力以0〜2MP a時其反應收率、選擇率、工業上易於 實施面最爲理想者。 更且,液相氟化反應中,爲有效進行氟化,於反應系 中添加含C - Η結合化合物、或進行紫外線照射者宜。 做爲含C - Η結合化合物者,以芳香族烴基爲者,特 別以苯、甲苯等爲較佳。該含C - Η結合化合物之添加量 爲化合物(3)中氫原子之〇 · 1〜10莫耳%者宜,特 別以0 · 1〜5莫耳%爲更佳。含C - Η結合化合物係於 反應系中於氟氣存在狀態下進行添加者宜。更且,於添加 含C——Η結合化合物時,使反應系進行加壓者宜。加壓時 之壓力以0 · 0 1〜5MPa者宜。 氟化反應中,因出現H F之副產物,爲去除副產物之 H F目的下於反應系中共存H F之收集劑者宜,或於反應 器氣體出口使收集劑與出口氣體接觸者宜。.做爲該H F收 集劑者與上述爲同例者,以N a F爲理想者。 本紙張尺度適财關家標準(CNS ) A4規格(210X 297公釐) -- -17- (請先閱讀背面之注意事項再填寫本頁)-16- 593301 A7 __ B7____ V. Description of the invention (4) In the fluorination reaction, the amount of fluorine in the hydrogen atom in the compound (3) often requires excessive fluorine equivalents to be placed in the fluorine gas, especially 1.5 times. A fluorine gas having an equivalent weight (that is, 1.5 times or more moles) has a better selection rate. It is advisable to maintain an excess of fluorine gas from the beginning to the end of the reaction. Therefore, it is preferable to introduce the compound (3) into a liquid phase in which fluorine is dissolved. The reaction temperature of the liquid phase fluorination reaction is generally higher than -60 t, and the boiling point of the compound ('3) is preferably lower than the boiling point of the compound (' 3). 0 t ~ + 100 ° C is preferred, and especially 20 ° C ~ + 50 ° C is most preferred. The reaction yield of fluorination is 0 to 2 MP a. The reaction yield, selectivity, and industrial ease of implementation are the most desirable. In addition, in the liquid phase fluorination reaction, in order to efficiently perform fluorination, it is preferable to add a C-fluorene-containing binding compound to the reaction system, or to perform ultraviolet irradiation. As the C-fluorene-containing compound, an aromatic hydrocarbon group is preferred, and benzene, toluene, etc. are particularly preferred. The C-fluorene-containing binding compound is preferably added in an amount of 0.1 to 10 mole% of the hydrogen atom in the compound (3), and more preferably 0.1 to 5 mole%. The C- 者 -containing binding compound is preferably added in the reaction system in the presence of fluorine gas. Furthermore, when adding a C-fluorene-binding compound, it is preferable to pressurize the reaction system. The pressure during pressurization is preferably from 0 · 0 1 to 5 MPa. In the fluorination reaction, as a by-product of H F appears, it is preferable to co-exist the collector of H F in the reaction system for the purpose of removing the H F of the by-product, or to contact the collector with the outlet gas at the gas outlet of the reactor. As the H F collector is the same example as above, and Na F is the ideal one. The paper size is suitable for financial and family care standards (CNS) A4 (210X 297 mm)--17- (Please read the precautions on the back before filling this page)

、1T 經濟部智慧財產局員工消費合作社印製 593301 Α7 Β7 五、發明説明()5 共存H F收集劑於反應系中之量爲存在於化合物(3 )中總氫原子量之1〜2 0倍莫耳者宜,1〜5倍莫耳爲 (請先閲讀背面之注意事項再填寫本頁) 更佳。 含氟化反應取得之化合物(4 )粗生物亦可直接用於 以下步驟,亦可精製後做成高純度度。做爲精製方法者如 使粗生成物直接於常壓或於減壓下進行蒸餾之方法等例者 〇 化合物(4 )係其化合物(3 )被氟化之化合物者, 化合物(3 )爲被全氟化之化合物者宜。 經濟部智慧財產局員工消費合作社印製 氟化反應時其C - Η爲變換成C - F之反應,於不飽 和結合中附加氟之反應者。所生成化合物(4 )中之A F係 對應A之基者,R e F爲對應R e之基者,此等基中氟化反 應前後未變更碳原子之排列方式,取得對應化合物(3 ) 之化合物。惟,化合物(3 )中出現碳-碳不飽和結合時 ,不飽和結合1個以上附加氟原子後變化結合狀態亦可。 做爲R e F者與該R ϋ爲相同之基者宜,特別以全氟1價有 機基爲更佳,更以全氟烷基、全氟(部份氯烷基)基、全 氟(含醚性氧原子烷基)基、全氟(部份氯(含醚性氧原 子烷基))基、或全氟四氫呋喃基爲最佳者。做爲化合物 (4 )之具體例者如下記化合物之例者。惟,A F與上述意 義相同者。 CF3CF2CF2OCF(CF3)COOCF2Af、 CF3CF2CF2OCF(CF3)CF2OCF(CF3)COOCF2Af、 AfCOOCF2Af 〇 本紙張尺度適用中.國國家標準(CNS ) Α4規格(210Χ297公釐) -18- 593301 A7 B7 五、發明説明()6 (請先閲讀背面之注意事項再填寫本頁) 化合物(4 )係藉由酯結合之分解反應後,X變換成 氟原子之化合物(5 )。酯結合分解反應可藉由加熱方法 ’或,求核劑之存在下、或與求電子劑反應後,進行者。 以加熱方法進行酯結合之分解反應時,可藉由化合物(:4 )之沸點與安定性選擇反應形式。 化合物(4 )爲易於氣化之化合物時,以於氣相進行 連續分解後使含取得化合物(5 )之出口氣體進行凝縮、 回收之氣相法進行者宜。氣相法之反應溫度爲5 0〜 35〇°C者宜’ 5〇〜300°C爲更佳,150〜250 °C爲最佳。又’氣相法中,亦可於反應系中共存無直接關 係之不活化氣體。做爲不活化氣體者如··氮氣、二氧化碳 氣體等例。不活化氣體之量爲化合物(4 )之0 · 0 1〜 5 0 %者宜。不活化氣體量太多時,則生成物之回收量將 降低。 經濟部智慧財產局員工消費合作社印製 以氣相法進行酯結合之分解反應時,以管型反應器使 用者宜。使用管型反應器時,其滯留時間以空塔基準爲 〇· 1秒〜1 0分鐘者宜。使用管型反應器之氣相反應中 ,爲促進反應之目的下,以塡充玻璃、鹼金屬鹽、或鹼土 類金屬之鹽於反應管中者宜。反應壓力並未特別限定,一 般,化合物C 4 )爲高沸點化合物時,於減壓下進行反應 者宜。另外,化合物(4 )爲低沸點化合物時,其生成物 之分解被抑制,且,反應率變高,因此,於加壓下進行反 應者宜。 本紙張尺度適用中國國家標準(CNS)A4規格(2K)X297公t) -19- 593301 經濟部智慧財產局員工消費合作社印製 A7 B7 五、發明説明()7 又,化合物(4 )爲不易氣化之化合物時,於反應器 內採用直接以液體加熱之液相法者宜。該方法之反應壓力 並未限定。含氟化環狀醚(5 )之生成物亦可於加熱結束 後,由反應器中一倂取出,惟,氟化環狀醚(5 )比化合 物(4 )之沸點較低,因此,氣化後,以連續性取出之方 法者宜。液相法之反應溫度以5 0〜3 0 0 °C者宜,特別 以1 0 0〜2 5 0 °C爲更佳。且,液相法其溶媒存在與否 均可,而由容積效率,控制副產物面觀之又以溶媒不存在 者爲較佳。 使酯結合之分解反應於液相中與求核劑或求電子劑相 互反應之方法下進行時,該反應中溶媒存在與否均可,由 容積效率,副產物抑制之觀點視之,又以溶媒不存在者爲 較佳。做爲求核劑者以氟陰離子(F _ )者宜,特別以源於 鹼金屬氧化物之氟陰離子爲最佳。鹼金屬化物之例如:1.1T printed by the Consumer Cooperative of the Intellectual Property Bureau of the Ministry of Economic Affairs 5933301 Α7 Β7 V. Description of the invention (5) The amount of coexisting HF collector in the reaction system is 1 ~ 20 times the total hydrogen atom amount in compound (3) For ears, 1 to 5 times moles is better (please read the precautions on the back before filling this page). Crude organisms containing compound (4) obtained from the fluorination reaction can also be used directly in the following steps, or they can be purified to high purity. As a purification method, for example, a method in which the crude product is directly distilled at normal pressure or under reduced pressure. The compound (4) is a compound whose compound (3) is fluorinated, and the compound (3) is Perfluorinated compounds are preferred. Printed by the Consumers' Cooperative of the Intellectual Property Bureau of the Ministry of Economic Affairs. The fluorination reaction is a reaction in which C-变换 is converted to C-F, and the responder adds fluorine to the unsaturated bond. In the generated compound (4), AF is the group corresponding to A, and R e F is the group corresponding to Re. In these groups, the arrangement of carbon atoms is not changed before and after the fluorination reaction, and the corresponding compound (3) is obtained. Compounds. However, when a carbon-carbon unsaturated bond occurs in the compound (3), the unsaturated state may be changed by adding one or more fluorine atoms to the unsaturated state. It is preferred that R e F is the same as that of R ϋ. Particularly, a perfluoro monovalent organic group is preferred, and a perfluoroalkyl group, a perfluoro (partial chloroalkyl) group, and a perfluoro ( Ether-containing oxygen atom alkyl) groups, perfluoro (partial chlorine (ether-containing oxygen atom alkyl)) groups, or perfluorotetrahydrofuranyl are the best. Specific examples of the compound (4) are as follows. However, A F has the same meaning as above. CF3CF2CF2OCF (CF3) COOCF2Af, CF3CF2CF2OCF (CF3) CF2OCF (CF3) COOCF2Af, AfCOOCF2Af 〇 This paper is applicable. National standard (CNS) A4 specification (210 × 297 mm) -18- 593301 A7 B7 5. Description of the invention () (Please read the precautions on the back before filling in this page) Compound (4) is a compound (5) where X is converted to a fluorine atom after a decomposition reaction by ester bonding. The ester-binding decomposition reaction can be performed by heating method or in the presence of a nucleating agent or after reacting with an electron-seeking agent. When the ester-binding decomposition reaction is carried out by heating, the reaction form can be selected by the boiling point and stability of the compound (: 4). When the compound (4) is a compound that is easily vaporized, it is preferable to perform a gas phase method in which the outlet gas containing the obtained compound (5) is condensed and recovered after continuous decomposition in the gas phase. The reaction temperature of the gas phase method is 50 ~ 35 ° C, and 50 '~ 300 ° C is more preferable, and 150 ~ 250 ° C is most preferable. In the gas phase method, an inactivated gas having no direct relationship can also coexist in the reaction system. Examples of non-activated gas include nitrogen and carbon dioxide gas. The amount of inactivated gas is preferably 0. 0 1 to 50% of the compound (4). When the amount of inactive gas is too large, the recovery amount of the product will decrease. Printed by the Consumer Cooperatives of the Intellectual Property Bureau of the Ministry of Economic Affairs. For the ester-binding decomposition reaction using the gas phase method, it is advisable to use a tubular reactor. When using a tubular reactor, the residence time is preferably 0.1 seconds to 10 minutes based on the empty tower. In the gas-phase reaction using a tubular reactor, for the purpose of promoting the reaction, it is preferable to fill the reaction tube with glass, an alkali metal salt, or an alkaline earth metal salt. The reaction pressure is not particularly limited. In general, when the compound C 4) is a high-boiling compound, it is preferable to perform the reaction under reduced pressure. In addition, when the compound (4) is a low boiling point compound, decomposition of the product is suppressed and the reaction rate becomes high. Therefore, it is preferable to perform the reaction under pressure. This paper scale applies Chinese National Standard (CNS) A4 (2K) X297g t) -19- 593301 Printed by the Consumer Cooperatives of the Intellectual Property Bureau of the Ministry of Economic Affairs A7 B7 V. Description of the invention () 7 Also, the compound (4) is not easy In the case of gasified compounds, a liquid phase method using liquid heating directly in the reactor is preferred. The reaction pressure of this method is not limited. The product containing the fluorinated cyclic ether (5) can also be taken out of the reactor after heating, but the fluorinated cyclic ether (5) has a lower boiling point than the compound (4). After the conversion, it is advisable to take it out continuously. The reaction temperature of the liquid phase method is preferably 50 to 300 ° C, and more preferably 100 to 250 ° C. In addition, the liquid phase method can be used with or without a solvent, and it is better to control the side products by volumetric efficiency and the presence of a solvent. When the ester-binding decomposition reaction is performed in a method of reacting with a nucleating agent or an electron-seeking agent in the liquid phase, the presence or absence of a solvent in the reaction can be considered from the viewpoint of volume efficiency and suppression of by-products. The absence of a solvent is preferred. As the nucleating agent, a fluoride anion (F_) is preferable, and a fluorine anion derived from an alkali metal oxide is particularly preferable. Examples of alkali metal compounds:

Na F、KF、C s F者宜,又以Na F其經濟面較爲理 想。求核劑可使用觸媒量’或過剩量亦無妨。求核劑量爲 化合物(4)之1〜500莫耳%者宜’ 10〜10〇莫 耳%爲特別理想,5〜5 0莫耳%爲最佳者。反應溫度之 下限以- 3 0 °C者宜,上限爲溶媒之沸點或化合物(4 ) 之沸點者宜。一般反應溫度爲- 2 0 °C〜2 5 0 °C爲特別 理想者。該方法中將所生成化合物(5 )連續性取出之同 時進行反應者宜。 酯分解反應之反應生成物中含有化合物(5 )同時亦 含化合物(2 a )。化合物(2 a )與化合物(5 )爲不 本紙張尺度適用中國國家標準(CNS ) A4規格(210X 297公釐) (請先閱讀背面之注意事項再填寫本頁)Na F, KF, C s F are preferred, and Na F is more economical. It is not necessary to use a catalyst amount 'or an excess amount for the nucleating agent. It is particularly desirable that the nuclear dose is 1 to 500 mole% of the compound (4). 10 to 100 mole% is particularly desirable, and 5 to 50 mole% is the best. The lower limit of the reaction temperature is preferably -30 ° C, and the upper limit is preferably the boiling point of the solvent or the boiling point of the compound (4). The general reaction temperature is-2 0 ° C ~ 2 50 ° C is particularly desirable. In this method, it is preferable to perform the reaction while taking out the produced compound (5) continuously. The reaction product of the ester decomposition reaction contains the compound (5) and also the compound (2a). Compound (2 a) and compound (5) are different. The paper size is applicable to Chinese National Standard (CNS) A4 (210X 297 mm) (Please read the precautions on the back before filling this page)

-20- 593301 A 7 _B7__ 五、發明説明()8 同化合物時,化合物(2 a )由化合物(5 )分離後,可 用於其他用途,化合物(2 a )可變換成其他有用化合物 之有用中間體者。 又,將化合物(2 a )用於與化合物(1 )進行酯化 反應之化合物(2 ),進行酯化反應時,可製造化合物( 3 ),該化合物(3 )藉由前述方法可製造化合物(5 ) ,如:化合物(2 a )於化合物(2 )中,其R e爲R e F 者,X爲氟原子之化合物者。將此化合物(2 a )做爲化 合物(2 )再行利用後,可製造化合物(5 )。 本發明中,使化合物(5 )進行熱分解。熱分解之反 應條件並無特別限定。一般熱分解反應係於氣相之熱分解 反應後進行者宜。 化合物(5 )之X爲氟原子時,氣相熱分解反應之反 應溫度以250〜400 °C者宜,280〜350 °C爲更 佳者。又,X爲一〇—M +時,氣相熱分解反應中之反應溫 度以150〜3〇〇Τ:者宜,20〇〜28〇°C爲較佳。 當氣相熱分解反應中反應溫度太低時,則變換率降低。反 之,氣相熱分解反應中反應溫度太高則增加生產目的化合 物以外之生成量者。 化合物(5 )之熱分解反應中,出現脫C ◦ F X反應 後,於呋喃環中形成雙重結合,產生化合物(6 a )或化 合物(6 b )。更且,此化合物中,由出現雙鍵轉移反應 之化合物(6 a )其化合物(6 b )由化合物(6 b )可 產生化合物C 6 a )。如:2位結合一C〇F之化合物( 本紙張尺度適用中國國家標準(CNS ) Α4規格(210Χ297公釐) (請先閲讀背面之注意事項再填寫本頁) •裝·-20- 593301 A 7 _B7__ V. Description of the invention () 8 When the compound is the same, compound (2 a) can be used for other purposes after being separated from compound (5), and compound (2 a) can be used as a useful intermediate for other useful compounds. Body. In addition, when the compound (2a) is used for the compound (2) which is subjected to an esterification reaction with the compound (1), when the esterification reaction is performed, the compound (3) can be produced, and the compound (3) can be produced by the aforementioned method. (5), for example: Compound (2a) in Compound (2), in which R e is Re e F, and X is a compound of fluorine atom. The compound (2a) can be reused as the compound (2) to produce the compound (5). In the present invention, the compound (5) is thermally decomposed. The reaction conditions for thermal decomposition are not particularly limited. Generally, the thermal decomposition reaction is performed after the thermal decomposition reaction in the gas phase. When X of the compound (5) is a fluorine atom, the reaction temperature of the gas-phase thermal decomposition reaction is preferably 250 to 400 ° C, and more preferably 280 to 350 ° C. In addition, when X is 10-M +, the reaction temperature in the gas-phase thermal decomposition reaction is preferably 150-300 T: preferably, 20-280 ° C. When the reaction temperature is too low in the gas-phase thermal decomposition reaction, the conversion rate decreases. Conversely, if the reaction temperature is too high in the gas-phase thermal decomposition reaction, the amount of compounds other than the production target compound is increased. In the thermal decomposition reaction of the compound (5), a de-C ◦ reaction occurs, and a double bond is formed in the furan ring, resulting in the compound (6a) or the compound (6b). Furthermore, among the compounds, the compound (6a) from the compound undergoing a double bond transfer reaction (6b) and the compound (6b) can produce the compound C6a). For example: 2-position compound with a COF (this paper size applies the Chinese National Standard (CNS) A4 specification (210 × 297 mm) (please read the precautions on the back before filling in this page))

、1T 經濟部智慧財產局員工消費合作社印製 -21 &gt; 593301 A7 B7 五、發明説明()9 (請先閲讀背面之注意事項再填寫本頁) 5 )熱分解反應中產生化合物(6 a ) ’又’ 3位結合 一 C〇F之化合物(5 )熱分解反應中產生化合物(6 b )。更於部份生成物出現雙鍵之轉移反應後,生成物呈&amp; 合物(6 a )與化合物(6 b ) 2種者。且,熱分解反應 中,一般生成2種化合物。特別是X由一〇 K +所不化合 物(5 )爲化合物(6 b )其X由一〇_ N a +所示化合物 (5 )爲化合物(6 a )被優先生成之。 熱分解反應之生成物組成可藉由反應條件等進行變化 之。生成物爲化合物(6 a )與化合物(6 b )兩者時’ 組成並未特別限定。 化合物(6 a )與化合物(6 b )可直接用於目的之 用途者,而通常變更爲其他化合物後使用之。又,生成2 種化合物時,使化合物(6 a )與化合物(6 b )進行分 離精製後變換成其他化合物亦可,化合物(6 a )與化合 物(6 b )其沸點相近,兩者進行分離手段極爲麻煩,因 此,不進行此等之分離,變換成其他化合物者宜。 經濟部智慧財產局員工消賓合作社印製 更且,本發明中,藉由1種以上選自化合物(6 a ) 及化合物(6 b )之化合物進行還原反應後,可取得1種 以上選自化合物(6 a )被還原之下記化合物(7 a )、 及化合物(6 b )被還原之化合物(7 b )之氟化飽和環 狀醚者。、 1T Printed by the Consumer Cooperatives of the Intellectual Property Bureau of the Ministry of Economic Affairs -21 &gt; 593301 A7 B7 V. Invention Description () 9 (Please read the precautions on the back before filling this page) 5) Compounds generated in the thermal decomposition reaction (6 a ) The compound (5) bound to a COF at position 3 again produces a compound (6b). Furthermore, after a double bond transfer reaction occurs in some products, the products are two types: &amp; compound (6 a) and compound (6 b). In the thermal decomposition reaction, two kinds of compounds are generally formed. In particular, the compound (5) in which X is from 10 K + is the compound (6 b), and the compound (5) in which X is from 10 — N a + is the compound (6 a) is preferentially formed. The product composition of the thermal decomposition reaction can be changed by reaction conditions and the like. When the product is both the compound (6a) and the compound (6b), the composition is not particularly limited. Compounds (6a) and (6b) can be directly used for the purpose, and they are usually used after being changed to other compounds. When two kinds of compounds are produced, the compound (6 a) and the compound (6 b) may be separated and purified and then converted into other compounds. The compounds (6 a) and the compound (6 b) have similar boiling points, and the two are separated. The method is extremely cumbersome, so it is advisable not to perform such separation and convert to other compounds. Printed by the Consumers' Cooperative of the Intellectual Property Bureau of the Ministry of Economic Affairs. Furthermore, in the present invention, after one or more compounds selected from the compound (6a) and the compound (6b) are subjected to a reduction reaction, one or more selected from The compound (6 a) is reduced below the compound (7 a), and the compound (6 b) is reduced to the fluorinated saturated cyclic ether of the compound (7 b).

本紙張尺度適用中.國國家標準(CNS ) A4規格(210X297公釐) -22- 593301 A7 ____ B7 五、發明説明($〇 還原反應時,於化合物(6 a )、化合物(6 b )之 碳-碳不飽和雙鍵中附加氫原子。此還原反應以使用氫進 行者宜’於觸媒之存在下使用氫進行者爲特別理想者。做 爲觸媒者以金屬擔載觸媒者宜。金屬擔載觸媒爲擔載金屬 之0 · 5〜5重量%者宜,較佳者爲1〜3重量%被擔載 者。更且’做爲金屬擔載觸媒者於活性碳中擔載金屬之觸 媒者宜’特別以擔載鈀之活性碳觸媒,擔載主成分之鈀與 金巴以外之8屬兀素之活性碳觸媒,或擔載a u之活性碳觸 媒者爲特別理想者。 其中,做爲銷以外之8屬元素者以1種以上選自f e 、C〇、Ni 、Ru、Rh、 Ir、及Pt者宜。鈀以外 之8屬元素量爲IE之0 · 〇1〜5〇質量%者宜。載體爲 活性碳時,以植物質做爲原料之活性碳比以鑛物質做爲原 料之活性碳爲較佳者’特別以椰子殻活性碳最佳。載體之 形狀可採用長約2〜5 m m之成型碳,約4〜5 〇網篩之 碎碳、粒狀碳等形狀者,又以4〜2 0網篩之碎碳、或長 度約2〜5 m m之成型碳爲較佳。 於活性碳擔載金屬之觸媒係於載體金屬成份擔載後, 進行乾燥之後’更以氫還原後,藉由活化方法所調製者宜 。該方法所調製之觸媒其耐久性高,長時間使用亦無需活 化之優點存在。活化時,以1 〇 〇〜3 〇 〇 °C特別是 2〇0〜3 0 0 °C )進行氫還原方法者佳。 氫量係針對由還原反應基質總量之化學.量論量時以2 倍莫耳以上者宜,更以3〜8倍莫耳爲更佳可取得高收率 本纸張尺度適用中國國家標準icNS ) A4規$ ( 210X:297公釐1 · 一 — - 23- (請先閱讀背面之注意事項再填寫本頁)The standard of this paper is applicable. National National Standard (CNS) A4 specification (210X297 mm) -22- 5933301 A7 ____ B7 V. Description of the invention (in the reduction reaction of $ 0, the compound (6a), compound (6b) A hydrogen atom is added to the carbon-carbon unsaturated double bond. This reduction reaction is particularly desirable for those using hydrogen as the catalyst in the presence of the catalyst. Those who support the catalyst with a metal should be the catalyst. The metal-supported catalyst is preferably 0.5 to 5% by weight of the supported metal, and more preferably 1 to 3% by weight of the supported metal. Furthermore, as a metal-supported catalyst in activated carbon Metal-bearing catalysts should especially use activated carbon catalysts that support palladium, active carbon catalysts that contain palladium as the main component and 8-element elements other than Kimba, or activated carbon catalysts that support au Among them, 8 elements other than pins are preferably one or more selected from fe, Co, Ni, Ru, Rh, Ir, and Pt. The amount of 8 elements other than palladium is IE 0 · 〇1 ~ 50% by mass is preferred. When the carrier is activated carbon, the ratio of activated carbon using plant matter as the raw material is based on minerals. The activated carbon is better, especially coconut shell activated carbon. The shape of the carrier can be shaped carbon with a length of about 2 ~ 5 mm, and the shape of crushed carbon, granular carbon, etc. with a mesh screen of about 4 ~ 50 mm. The crushed carbon of 4 ~ 20 mesh sieve or the shaped carbon with a length of about 2 ~ 5 mm is more preferred. After the catalyst of the active carbon-carrying metal is supported by the carrier metal component, it is dried. After hydrogen reduction, it should be prepared by the activation method. The catalyst prepared by this method has the advantages of high durability and long-term use without the need for activation. At the time of activation, it is particularly effective at 1000 ~ 300 ° C. 2000 ~ 300 ° C) is preferred for hydrogen reduction method. The amount of hydrogen is based on the chemistry of the total amount of the reduction reaction substrate. When measuring the quantity, it is better to use more than 2 times moles, and more preferably 3 to 8 times moles to obtain a high yield. This paper scale applies Chinese national standards. icNS) A4 Regulation $ (210X: 297 mm 1 · 1 —-23- (Please read the precautions on the back before filling this page)

、1T 經濟部智慧財產局員工消費合作社印製 593301 A7 B7 五、發明説明(幻 之目的化合物者。 (請先閲讀背面之注意事項再填寫本頁) 還原反應之溫度一般於常壓下1 3 0〜2 5 0 °C者宜 ,特別以1 5 0〜2 0 0 °C爲較佳。反應壓力並無特別限 定。還原反應之反應時間針對觸媒之接觸時間以4〜6 0 秒爲宜,特別以8〜4 0秒爲更佳。更且,還原反應爲控 制過剩之溫度上昇,亦可以氮等不活性氣體稀釋氫之同時 進行之。 該還原反應中產生還原化合物(6 a )時呈化合物( 7a)、還原化合物(6 b )時呈化合物(7 a )與(7 b )所成之生成物。還原反應之生成物組成係藉由還原反 應之基質組成進行變化。 經濟部智慧財產局員工消費合作社印製 還原反應之生成物由化合物(7 a )與化合物(7 b )所成時,此等亦可直接做爲目的用途使用之,或進行分 離亦可。由於化合物(7 a )與化合物(7 b )之沸點不 同,因此,分離時,藉由蒸餾法進行分離者宜。又,熱分 解反應之生成物爲化合物(6 a )與化合物(6 b )時, 還原反應取得化合物爲化合物(7 a )時,以於還原反應 後進行蒸餾分離取得化合物(7 a )者宜。 藉由本發明製造方法取得之化合物(6 a )、化合物 (6b)、化合物(7 a )、及化合物(7 b )具有做爲 氯氟碳類代替化合物之良好特性、臭氧破壞係數爲零者、 地球溫暖化係數亦極小之化合物者。由此等化合物或此等 1種以上化合物所成混合物爲做爲功能劑有用之化合物者 本紙張尺度適用中.國國家標準(CNS ) A4規格(210X297公釐) -24- 593301 A7 -_______B7__五、發明説明( 功能劑之例如:冷媒、洗淨劑、去水乾燥溶劑、溶劑 、聚合溶劑、乾蝕刻劑、樹脂之發泡劑等例。其中含1種 或2種選自化合物(6 a )及化合物(6 b )之氟化不飽 和環狀醚之功能劑做爲去水乾燥溶劑、乾蝕刻劑、或洗淨 劑使用者宜。又,含有1種或2種選自化合物(7 a )及 化合物(7 b )之氟化飽和環狀醚之功能劑,特別定含化 合物(_ 7 a )之功能劑爲做爲乾蝕刻劑使用者佳。 本發明氟化環狀醚之結構中由於存在氧原子,因此, 此做爲乾蝕刻劑使用時,可省略乾蝕刻中之添加氧操作之 優點。 本發明更提供一種做爲該功能劑中間體有用之下記化 合物者。1.1T printed by the Consumer Cooperative of the Intellectual Property Bureau of the Ministry of Economic Affairs 5933301 A7 B7 V. Description of the invention (for those who want to be the target compounds. (Please read the precautions on the back before filling this page) The temperature of the reduction reaction is usually under normal pressure 1 3 0 ~ 2 50 ° C is preferred, especially 150 ~ 2 0 ° C is preferred. The reaction pressure is not particularly limited. The reaction time of the reduction reaction is 4 ~ 60 seconds for the contact time of the catalyst. It is particularly preferable that it is 8 to 40 seconds. Furthermore, the reduction reaction is to control the excessive temperature rise, and it can also be performed while diluting hydrogen with an inert gas such as nitrogen. This reduction reaction produces a reducing compound (6a) When the compound (7a) and the reduced compound (6b) are present, the product formed by the compounds (7a) and (7b) is present. The composition of the product of the reduction reaction is changed by the matrix composition of the reduction reaction. Ministry of Economic Affairs When the product of the reduction reaction printed by the Intellectual Property Bureau's consumer cooperative is made of compound (7a) and compound (7b), these can also be used directly for the purpose, or can be separated. Since the compound ( 7 a) and The boiling point of the compound (7b) is different. Therefore, it is suitable to perform the separation by distillation during the separation. When the product of the thermal decomposition reaction is the compound (6a) and the compound (6b), the compound obtained by the reduction reaction is In the case of the compound (7a), it is preferable to obtain the compound (7a) by distillation and separation after the reduction reaction. The compound (6a), the compound (6b), the compound (7a), and the compound obtained by the production method of the present invention (7 b) Those who have good characteristics as chlorofluorocarbon replacement compounds, those with zero ozone destruction coefficient, and extremely low global warming coefficient. These compounds or mixtures of these compounds For functional compounds that are useful, the paper size is applicable. National National Standard (CNS) A4 specification (210X297 mm) -24-593301 A7 -_______ B7__ V. Description of the invention (Examples of functional agents: refrigerant, detergent, Examples of solvents, solvents, polymerization solvents, dry etchants, resin foaming agents, etc., containing one or two fluorinated unsaturated cyclic ethers selected from compound (6a) and compound (6b) Of It is suitable for users to use water as a drying solvent, a dry etchant, or a detergent. In addition, it contains one or two fluorinated saturated cyclic ethers selected from compound (7a) and compound (7b). The functional agent, especially the functional agent containing the compound (_ 7 a) is preferably used as a dry etchant. The fluorinated cyclic ether structure of the present invention has oxygen atoms, so when it is used as a dry etchant The advantages of the operation of adding oxygen in dry etching can be omitted. The present invention further provides a compound described below which is useful as the functional agent intermediate.

(3b-2) 經濟部智慧財產局員工消費合作社印製 (請先閲讀背面之注意事項再填寫本頁)(3b-2) Printed by the Consumer Cooperatives of the Intellectual Property Bureau of the Ministry of Economic Affairs (Please read the precautions on the back before filling this page)

ClCl

CFl (4b-2) 〇 ch2ocorC1 (3a-2) 惟,R e 1及R e F 1分別代表全氟烷基、全氟(部份氯 烷基)基、全氟(含醚性氧原子烷基)基、全氟(部份氯 (含醚性氧原子烷基)基、或全氟四氫呋喃基。R e 1及 R e F 1之例如:碳數1〜2 0之基者宜,特別以碳數1〜 ◦之基爲更佳。又,做爲R e 1及R e F 1者更以全氟烷基、 全氟(醚性氧原子烷基)爲最佳。 〔實施例〕 ch2〇cor 本紙張尺度適用中國國家標準(CNS ) A4規格(210X297公釐) -25-CFl (4b-2) 〇ch2ocorC1 (3a-2) However, Re 1 and Re F 1 represent perfluoroalkyl, perfluoro (partially chloroalkyl), and perfluoro (ether ether-containing alkane) Group), perfluoro (partially chlorinated (alkyl group containing etheric oxygen atom)), or perfluorotetrahydrofuranyl. Examples of Re 1 and Re F 1 are: a group having 1 to 20 carbon atoms, particularly A radical having a carbon number of 1 to ◦ is more preferred. In addition, as for Re 1 and Re F 1, a perfluoroalkyl group or a perfluoro (ether oxygen atom alkyl group) is more preferred. [Example] ch2〇cor This paper size is applicable to Chinese National Standard (CNS) A4 (210X297 mm) -25-

爲 T M S 、C CFor T M S, C C

593301 A7 B7 ____ 五、發明説明( 以下,依實施例進行本發明具體說明,惟,本發明不 限於此。又,以下,氣體層析法記爲G C、氣體層析法質 量分析記爲G C - M S。另外,由G C.頂點面積比所求出 之純度記爲G C純度、收率記爲G C收率。由N M R光譜 頂點面積比求出收率記爲N M R收率。又,四甲基矽烷記 FCC1F2記爲R—113。又 N M R光譜數據以外觀化學移動範圍代表之 〔例1〕 藉由酯化步驟之化合物(3 b - 1 )之製造例 ch2oh + fc〇cf(cf3)ocf2cf2cf3 (請先閲讀背面之注意事項再填寫本頁}593301 A7 B7 ____ V. Description of the Invention (Hereinafter, the present invention will be specifically described according to the examples, but the present invention is not limited thereto. In the following, the gas chromatography method is referred to as GC and the gas chromatography mass analysis is referred to as GC- MS. The purity obtained from the G C. vertex area ratio is described as GC purity, and the yield is described as GC yield. The yield obtained from the NMR spectrum vertex area ratio is described as NMR yield. Also, tetramethyl Silane is recorded as FCC1F2 as R-113. The NMR spectrum data is represented by the range of appearance chemical shift. [Example 1] Production example of compound (3 b-1) through esterification step ch2oh + fcocf (cf3) ocf2cf2cf3 ( Please read the notes on the back before filling out this page}

ch2oc〇cf(cf3)ocf2cf2cf3 (3b-l) g 將2 —四氫糠醇(2 0 g )與三乙胺(2 1 . 8 經濟部智慧財產局員工消費合作社印製 置入燒瓶後,冰浴下進行攪拌。維持內溫1 0 °c以下胃日寺 以1小時滴入F C〇C F ( C F 3 )〇C F 2 C F 2 c P , 7 1 · 5 g )。滴畢後,室溫下攪拌2小時,於內溫丄5 °C以下加入水(5 0 m L )。 將取得粗液進行分液後,以水(5 0 m L )進f于2 之下層洗淨後,以硫酸鎂進行乾燥後,過濾後取得粗液。 減壓下取得做成8 8〜8 9 °C / 2 . 7 K P a (絕對_ 餾份之目的酯化合物(6 6 , 3 g ) 。G C純度爲9 8 % 者。N M R分析後確定化合物(3 b — 1 )之生成。 -26 - 593301 A7 B7 五、發明説明(&gt;4 'H NMR(300.4MHz,CDCl35TMS)5(ppm): 1 · 6 〇〜1 · 7 3 ( m,1 Η ), 1·86 〜2.10(m,3H), 3. 76 〜3. 91 (m,2H), 4 . 1 4 〜4 · 2 2 ( m,1 Η ), 4·28 〜4.47(m,2H)〇 19F-NMR(282.7MHz,CDCl3,CFCl3)5(ppm): -7 9 . 9 ( 1 F ),- 81.3(3F), 一 8 2 · 1 ( 3 F ) ,一 8 6 · 4 ( 1 F ), (請先閲讀背面之注意事項再填寫本頁) 12 9 2 F ) ,一 1ch2oc〇cf (cf3) ocf2cf2cf3 (3b-l) g Printed and placed 2-tetrahydrofurfuryl alcohol (20 g) and triethylamine (2 1.8 in the Consumer Cooperative of the Intellectual Property Bureau of the Ministry of Economic Affairs into the flask, then placed in an ice bath Stirring was carried out. At an internal temperature of 10 ° C or lower, FC Ri (CF 3 (CF 3) CF 2 CF 2 c P (7 1 · 5 g)) was dripped into Wei Ri Temple for 1 hour. After dripping, stir at room temperature for 2 hours, and add water (50 ml) at an internal temperature below 5 ° C. The obtained crude liquid was separated, and then washed with water (50 ml) into the lower layer of 2, and then dried with magnesium sulfate, and then filtered to obtain a crude liquid. Obtained under reduced pressure to make 8 8 ~ 8 9 ° C / 2.7 KP a (absolute _ fraction of the target ester compound (66, 3 g). The GC purity is 98%. The compound was determined after NMR analysis ( 3 b — 1). -26-593301 A7 B7 V. Description of the invention (&gt; 4 'H NMR (300.4 MHz, CDCl35TMS) 5 (ppm): 1 · 6 〇 ~ 1 · 7 3 (m, 1 Η ), 1.86 to 2.10 (m, 3H), 3. 76 to 3.91 (m, 2H), 4. 1 4 to 4 · 2 2 (m, 1 Η), 4.28 to 4.47 (m, 2H) 〇19F-NMR (282.7MHz, CDCl3, CFCl3) 5 (ppm): -79.9 (1F), -81.3 (3F), -8 2 · 1 (3F), -8 6 · 4 (1 F), (Please read the notes on the back before filling out this page) 12 9 2 F), 1 1

F 〔例2〕 藉由氟化步驟之化合物(4 b - 1 )製造例 (3b-1)F [Example 2] Production Example (3b-1) of Compound (4b-1) by the fluorination step

(4b-l)(4b-l)

\ 'CP2OCOCF(CF3)OCF2CF2CF3 F 經濟部智慧財產局員工消費合作社印製 5 0 0 m 1鎳製高壓鍋中加入R — 1 1 3 ( 3 1 3 g\ 'CP2OCOCF (CF3) OCF2CF2CF3 F Printed by the Consumer Cooperative of the Intellectual Property Bureau of the Ministry of Economy 5 0 0 m 1 Add R — 1 1 3 (3 1 3 g

)進行攪拌後,保持2 5 °C。於高壓鍋氣體出口直列設置 保持2 0 t之冷却器,N a F顆粒塡充層、及保持1 0 °C 之冷却器。又,使保持- 1 0 °C之冷却器所凝聚之液體設 置爲回送高壓鍋之液體回送線。以1小時吹入氮氣後,以 流速8 · 〇 8 L / h,1小時內吹入以氮氣稀釋成2 0 % 之氟氣。再以相同流速吹入氟氣之同時,將例1取得化合 物(3 b — 1 ) ( 5 .〇 1 g )溶於 R — 1 1 3 ( 1 〇 〇 本紙張尺度適用中周國家標準(CNS ) A4規格(210X297公釐) -27 - 593301 A7 ___ _B7_ 五、發明説明(知 g )之溶液以4 · 7小時進行注入。 (請先閲讀背面之注意事項再填寫本頁) 再以相同流速吹入氟氣之同時,使苯濃度爲〇 . 〇 1 g /m 1之R - 1 1 3溶液(9 m 1 )由2 5 t昇溫至 4 0 °C同時進行注入後,關閉高壓鍋之苯注入口,更關閉 高壓鍋之出口活門持續攪拌0 · 4小時。再使壓力做成常 壓,保持反應器內溫爲4 0 °C同時,注入該苯溶液(6 ml),關閉高壓鍋注入口,更關閉高壓鍋之出口閥,壓 力爲0 · 2 0 Μ P a後,關閉高壓鍋氟氣體入口活門,持 續攪拌0 · 4小時。更重覆同樣操作進行3次。苯之注入 總量爲〇_ 3 3 g ,R - 1 1 3之注入總量爲3 3 m 1 。 更以1小時吹入氮氣。目的物以1 9 F - N M R進行定量後 ,確定化合物(4 b - 1 )之生成,其收率爲6 4 %者。 19F-NMR(3 76.0MHz,CDCh,CFCl3)6(ppm): -8 0 . 3 ( 1 F ) ,- 8 1 · 9 ( 3 F ), 經濟部智慧財產局員工消費合作社印製 -82.1 C3F),- 83.5 〜- 84.8( 2F) ,-85.5 〜-88.0(3F) ,一 126.5(1 F),- 127.4(1F),- 128.1(1F), -1 3 0 . 2 ( 2 F ) ,13〇.4(1F), -1 3 2 . 2 ( 1 F ) ,- 1 3 5 . 8 ( 1 F )。 〔例3〕 藉由酯分解步驟之化合物(5 a - 1 )製造例 本紙張尺度適用中國國家標準(CNS ) A4規格(210X297公釐) - 28- 593301 A7 B7 五、發明説明(釦 (4b-l)) After stirring, keep at 25 ° C. A cooler maintained at a temperature of 20 t, a filling layer of Na F particles, and a cooler maintained at 10 ° C were arranged in line at the gas outlet of the autoclave. In addition, the liquid condensed by the cooler maintained at -10 ° C was set as a liquid return line for returning the autoclave. After nitrogen was blown in for 1 hour, a fluorine gas diluted with nitrogen to 20% was blown in at a flow rate of 8.08 L / h for 1 hour. While blowing in fluorine gas at the same flow rate, the compound (3 b — 1) (5.01 g) obtained in Example 1 was dissolved in R — 1 1 3 (100). ) A4 size (210X297mm) -27-593301 A7 ___ _B7_ V. The solution of invention description (knowledge g) is injected in 4 · 7 hours. (Please read the precautions on the back before filling this page) and then use the same flow rate While blowing in the fluorine gas, the R-1 1 3 solution (9 m 1) with a benzene concentration of 0.01 g / m 1 was heated from 2 5 t to 40 ° C, and the benzene was closed after the autoclave was injected. Note the inlet and close the outlet valve of the autoclave and continue to stir for 0.4 hours. Then make the pressure normal pressure and keep the internal temperature of the reactor at 40 ° C. At the same time, inject the benzene solution (6 ml) and close the autoclave inlet. Close the outlet valve of the pressure cooker again. After the pressure is 0 · 20 MPa, close the fluorine gas inlet valve of the pressure cooker and continue stirring for 0.4 hours. Repeat the same operation 3 times. The total amount of benzene injected is 0_ 3 3 g, the total injection of R-1 1 3 is 3 3 m 1. Nitrogen is blown in for 1 hour. The target is 19 F -After quantification by NMR, it was confirmed that the compound (4 b-1) was produced, and the yield was 64%. 19F-NMR (3 76.0 MHz, CDCh, CFCl3) 6 (ppm): -8 0.3. (1 F),-8 1 · 9 (3 F), printed by the Consumer Cooperatives of the Intellectual Property Bureau of the Ministry of Economic Affairs-82.1 C3F),-83.5 to-84.8 (2F), -85.5 to-88.0 (3F), 126.5 (1 F),-127.4 (1F),-128.1 (1F), -1 3 0.2 (2 F), 130.4 (1F), -1 3 2.2 (1 F),-1 3 5. 8 (1 F). [Example 3] Production example of compound (5 a-1) through the ester decomposition step The paper size applies the Chinese National Standard (CNS) A4 specification (210X297 mm)-28- 593301 A7 B7 V. Description of the invention (deduction (4b -l)

COFCOF

F FF F

COOK 將例2取得之化合物(4 b - 1 ) ( 2 · 1 g )與 N a F粉末(0 · 0 2 g ) —倂置入燒瓶中,進行劇烈攪 拌之同時於油浴中1 4 0 °C下進行加熱1 〇小時。燒瓶上 部設置調節溫度於2 0 °C之迴流器。回收冷却後之液狀樣 品(2 . 0 g )。將回收之液狀樣品於含有化合物(4 b 一 1) 2 · 5倍莫耳量K〇H之K0H水溶液中進行反應 ,去除水後取得化合物(5 a — 1 )。 〔例4〕 化合物(6 b )之製造例 將例3取得之化合物(5 a — 1 )以與文獻(zh. Org. Khim·,1977 13 (12),2573)同法下於 2 2 與 K2C 〇3 同時進行加熱後,取得主生成物之化合物(6 b )。化合 物(6 b )之收率爲7 1 . 2 %。生成物中亦確定化合物 (6 a )之存在。 (請先閱讀背面之注意事項再填寫本頁) 經濟部智慧財產局員工消費合作社印製 (5a -1)COOK Put the compound (4 b-1) (2 · 1 g) and Na F powder (0 · 0 2 g) obtained in Example 2 into a flask and stir vigorously while in an oil bath 1 4 0 Heating was performed at ° C for 10 hours. The top of the flask was equipped with a reflux device to adjust the temperature to 20 ° C. Recover the cooled liquid sample (2.0 g). The recovered liquid sample was reacted in an aqueous KOH solution containing compound (4b-1) 2 · 5 times the molar amount of KOH, and the compound (5a-1) was obtained after removing water. [Example 4] Production Example of Compound (6 b) The compound (5 a — 1) obtained in Example 3 was the same as that in the literature (zh. Org. Khim ·, 1977 13 (12), 2573) in 2 2 and K2C 03 was heated at the same time to obtain the compound (6 b) as the main product. The yield of the compound (6b) was 71.2%. The presence of compound (6a) was also confirmed in the product. (Please read the notes on the back before filling this page) Printed by the Consumer Cooperatives of the Intellectual Property Bureau of the Ministry of Economic Affairs (5a -1)

F 〔例5〕 藉由速原步驟之化合物(7 b )製造例 利用重覆進行例1〜4之反應取得之化合物(6 b 本紙張尺度適用中國國家標準(CNS ) A4規格(210X297公釐) -29- 593301 B7 △ □ 五、發明説明( 後,進行還原反應。 將表1所示之觸媒(1 〇 〇 m 1 )塡入鎳鉻鐵耐熱 金600製反應管(直徑1/2 i nch,長1 cm)中 ,此由外部進行加熱後保持於1 2 0 °C ’以0 · 2 m ◦ 1 / h之流速導入化合物(6 b ),同時以1 · 0 m ο 1 / h之流速導入氫之後,進行反應。以G C進行分析反應器 出口氣體後,其結果之化合物(7 b )分別以下表1之成 績取得。又,觸媒均使用針對1 0 0質量份之椰子殼碎碳 爲擔載2質量份金屬成份者。 (請先閲讀背面之注意事項再填寫本頁} 〔表1〕 還原例 觸媒(莫耳比) 化合物(6b)之 化合物(7b)之 反應率 ‘選擇率 1 Pd 1 0 0 % 9 5% 2 Pd-Pt(10:1) 1 0 0 % 96% 3 Pd-Au(10: 1) 100% 9 8% -訂 經濟部智慧財產局員工消費合作社印製 例6〕 藉由酯化步驟之化合物(3 a - 1 )製造例 CH2OH 十 FCOCF(CF3)OCF2CF2CF3F [Example 5] The compound obtained by the compound (7 b) in the fast-prototyping step is obtained by repeating the reaction of Examples 1 to 4 (6 b This paper size applies the Chinese National Standard (CNS) A4 specification (210X297 mm) ) -29- 593301 B7 △ □ 5. Description of the invention (After that, reduction reaction is carried out. The catalyst (100m 1) shown in Table 1 is poured into a nickel-chromium-iron refractory gold 600 reaction tube (1/2 in diameter) i nch, 1 cm in length), this is heated from the outside and maintained at 120 ° C 'to introduce compound (6 b) at a flow rate of 0 · 2 m ◦ 1 / h, while at the same time 1 · 0 m ο 1 / After introducing hydrogen at a flow rate of h, the reaction was performed. After analyzing the gas at the outlet of the reactor by GC, the compound (7b) of the result was obtained in the results in Table 1 below. In addition, the catalyst used coconut for 100 parts by mass Shell crushed carbon is for those who carry 2 parts by mass of metal components. (Please read the precautions on the back before filling out this page} [Table 1] Reduction Example Catalyst (Mole ratio) Reaction of Compound (7b) Compound (6b) Rate 'selection rate 1 Pd 1 0 0% 9 5% 2 Pd-Pt (10: 1) 1 0 0% 96% 3 Pd-Au (10: 1) 100% 9 8%- Printed by the Consumers' Cooperative of the Intellectual Property Bureau of the Ministry of Economic Affairs Example 6] Production Example of Compound (3 a-1) by Esterification Step CH2OH Ten FCOCF (CF3) OCF2CF2CF3

CH2〇COCF(CF3)OCF2CF2CF3 (3a_l) 將例2中之2 -四氫糠醚(2 0 g )變更爲2 -糠醇 本紙張尺度適用中國國家標準(CNS ) A4規格(210X297公釐) -30- 593301 A7 B7 五、發明説明(知 (2 1 g )之外,與例1同法進行酯化步驟,確定化合物 (3 a - 1 )之生成。 19F-NMR(2 82.7MHz,CDCh?CFCl3)5(ppm): -7 9 · 9 ( 1 F ) ,- 8 1 · 3 ( 3 F ), 一 8 2 . 1 ( 3 F ) ,— 8 6 · 4 ( 1 F ), 一 129.5(2F),-131.5(1F)。 〔例7〕 藉由氟化步驟之化合物(4 b - 1 )製造例CH2〇COCF (CF3) OCF2CF2CF3 (3a_l) Change the 2-tetrahydrofurfuryl ether (2 0 g) in Example 2 to 2-furfuryl alcohol. The paper size applies the Chinese National Standard (CNS) A4 specification (210X297 mm) -30 -593301 A7 B7 V. Explanation of the invention (except for (2 1 g)), the esterification step was performed in the same manner as in Example 1 to determine the formation of compound (3 a-1). 19F-NMR (2 82.7 MHz, CDCh? CFCl3 ) 5 (ppm): -7 9 · 9 (1 F),-8 1 · 3 (3 F),-8 2. 1 (3 F),-8 6 · 4 (1 F),-129.5 (2F ), -131.5 (1F). [Example 7] Production Example of Compound (4 b-1) by fluorination step

F F 、cf2〇cocf(cf 3)OCF2CF2CF3 (3a-l) -—^ 卜F F, cf2〇cocf (cf 3) OCF2CF2CF3 (3a-l) ----- ^ Bu

F (4b-1) 將例2中化合物(3 b - 1 )變更爲5 . 5 g之例6 取得化合物(3 a - 1 )之外,與例2同法進行氟化步驟 〇 以1 9 F - N M R定量反應後之氟化物後,確定生成化 合物(4 b - 1 ),其收率爲6 4 %。 經濟部智慧財產局員工消費合作社印製 (請先閲讀背面之注意事項再填寫本頁) !9F-NMR(37 6.0MHz,CDCl3,CFCl3)6(ppm): -8 0 . 3 ( 1 F ) ,- 81.9( 3F), -82. 1 ( 3 F ),- 83.5 〜- 84.8 C2F) ,—85.5--88.〇(3F) ,— 126.5(1 F ) ,- 1 2 7 · 4 ( 1 F ) ,— 1 2 8 · 1 ( 1 F ), -1 3 0 . 2 ( 2 F ),13〇.4(1F) , -1 3 2 · 2 ( 1 F ) ,- 1 3 5 . 8 ( 1 F )。 本紙張尺度適用中國國家標準(CNS ) A4規格(210X297公釐) -31 - 593301 A7 B7 五、發明説明(的 〔例8〕 藉由酯分解步驟之化合物(5 a - 2 )製造例 (4b—1)F (4b-1) The compound (3 b-1) in Example 2 was changed to 5.5 g of Example 6 except that the compound (3 a-1) was obtained, and the fluorination step was performed in the same manner as in Example 2. F-NMR was used to quantify the fluoride after the reaction, and it was confirmed that the compound (4 b-1) was formed, and the yield was 64%. Printed by the Consumer Cooperative of the Intellectual Property Bureau of the Ministry of Economic Affairs (please read the precautions on the back before filling this page)! 9F-NMR (37 6.0MHz, CDCl3, CFCl3) 6 (ppm): -8 0. 3 (1 F) ,-81.9 (3F), -82. 1 (3 F),-83.5 to-84.8 C2F), -85.5--88.〇 (3F),-126.5 (1 F),-1 2 7 · 4 (1 F), — 1 2 8 · 1 (1 F), -1 3 0.2 (2 F), 130.4 (1F), -1 3 2 · 2 (1 F),-1 3 5. 8 (1 F). This paper size applies Chinese National Standard (CNS) A4 specification (210X297 mm) -31-593301 A7 B7 V. Description of the invention ([Example 8] Production example of compound (5 a-2) through ester decomposition step (4b -1)

COFCOF

F FF F

CO〇Isj*^ (5a-2) 例3中K〇Η變更爲N a〇Η之外,與例3酯分解步 驟同法進行反應取得化合物(5 a - 2 )。 ---------P 裝 II (請先閱讀背面之注意事項再填寫本頁) 〔例9〕 化合物 之製造例CO〇Isj * ^ (5a-2) In Example 3, except that K〇Η was changed to NaoΗ, the reaction was carried out in the same manner as in the ester decomposition step of Example 3 to obtain the compound (5a-2). --------- P Pack II (Please read the precautions on the back before filling out this page) [Example 9] Production example of the compound

F 訂 經濟部智慧財產局員工消費合作社印製 將Μ 4之化合物(5 a - 1 )變更爲例8取得之化合 物(5 a — 2 ),將K 2 C〇3變更爲N a 2 C〇3之外,與 例4同法進行反應取得主成份之化合物(6 a )。化合物 (6 a )之收率爲6 1 · 0 %者。又,生成物中亦確定生 成化合物(6 b )。 〔例1 0〕 藉由還原步驟之化合物(7 a )製造例 藉由例6〜9之反應重覆進行取得之化合物(6 a ) 直接含化合物(6 b )使用後,於表2所示之觸媒存在下 與例5同法進行還原步驟後,取得化合物(7 a )。以 本紙張尺度適用中國國家標準(CNS ) A4規格(210X297公釐) -32- 593301 A7 B7 五、發明说明(知 G C分析反應挤出口氣體之結果如表2所示。出口氣體中 亦確定化合物(7 b )之存在。 丄表2〕 還原例 觸媒(莫耳比) 化合物(6a)之 化合物(7a)之 反應率 選擇率 ^ 1 Pd 100% 94% — 2 Pd-Pt(10:l) 100% 95% 3 Pd-Au(10: 1) 1 0 0 % 98% (請先閲讀背面之注意事項再填寫本頁) 經濟部智慧財產局員工消費合作社印製 〔例1 1〕 做爲乾蝕刻劑之評定例 (例1 1 - 1 )於平行平板型等離子蝕刻裝置中固定 長面形成氧化矽膜之直徑1 5 0 m m之矽晶圓,系內做成 真空後,例4之生成物蒸餾取得之化合物(6 b )進氣化 後,導入5 0 m 1 /分鐘(氣體溫度2 0。(:)。設定系內 壓力爲3 9 · 9 P a (絕對壓),使等離子密度 刻 3 蝕其 ο ) 驗壓 實膜 刻之 蝕點 行3 進意 後任 秒上 ο 圓 6 日ΗΘ 射定 照測 子行 離進 等後 之 1刖 3 亥 蝕 於 係 度 速F Order Printed by the Consumer Cooperative of the Intellectual Property Bureau of the Ministry of Economic Affairs to change the compound (5 a-1) of M 4 to the compound (5 a-2) obtained in Example 8, and change K 2 C03 to Na 2 C. Except 3, the same method as in Example 4 was followed to obtain the main compound (6a). The yield of the compound (6 a) is 61. 0%. It was also confirmed that a compound (6 b) was formed in the product. [Example 1 0] Production Example of Compound (7a) by Reduction Step Compound (6a) obtained by repeating the reaction of Examples 6 to 9 The compound (6a) containing the compound (6b) directly after use is shown in Table 2. In the presence of a catalyst, a reduction step was performed in the same manner as in Example 5 to obtain a compound (7a). Applicable to China Paper Standard (CNS) A4 (210X297 mm) at this paper scale -32- 593301 A7 B7 V. Description of the Invention (The results of GC analysis of the reaction gas at the extrusion port are shown in Table 2. Compounds were also identified in the outlet gas. (7 b). 丄 Table 2] Reduction Example Catalyst (Mole ratio) Compound (6a) Compound (7a) Reaction Rate Selectivity ^ 1 Pd 100% 94% — 2 Pd-Pt (10: l ) 100% 95% 3 Pd-Au (10: 1) 1 0 0% 98% (Please read the notes on the back before filling out this page) Printed by the Consumer Cooperatives of the Intellectual Property Bureau of the Ministry of Economic Affairs [Example 1 1] as Evaluation Example of Dry Etching Agent (Example 1-1) A silicon wafer with a diameter of 150 mm and a silicon oxide film formed on the long surface was fixed in a parallel flat-plate plasma etching device. After the inside was made into a vacuum, Example 4 was generated. After the compound (6 b) obtained by chemical distillation is gasified, it is introduced into 50 m 1 / min (gas temperature 20. (:). The internal pressure is set to 3 9 · 9 P a (absolute pressure) to make the plasma density Etch 3 etch it ο) check the etch point of the compacted film etch 3 to enter the second for any second ο circle 6 day Once into the 3 1 INTRODUCTION Hai erosion speed at the Department of

C m 之 度X 速成 刻記 触 下 點以 爲 均 平Degree of C m X Instant engraving

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例之 爲定 更測 變法 \1|/ jIRi cd IX 之爲 得果 取結 本紙張尺度適用中國國家標準(CNS ) A4規格(210X297公釐) -33- 593301 A7 B7 五、發明説明(h (例1 1 一 3 )比較例 將化合物(6 a )變更爲八氟環戊烯之外,與例1 1 - 1 R法測疋之。結果爲X者,触刻反應完全未進行,石夕 晶圓上呈黃褐色聚合物之沈積物。 〔例1 2〕 做爲去水乾燥溶劑之評定例 預先洗淨不銹鋼網篩(5 c m X 5 c m ),再將浸櫝 水中者做爲被洗淨物品。例1 〇所合成之化合物(7 a ) 直接使用含化合物(7 b )者。該化合物(7 b )中加入 乙醇後調整乙醇濃度調成5質量%之混合溶劑。 再將被洗淨物浸漬於3 0 °C之混合溶劑,利用超音波 進行去水1分鐘。再於化合物(7 a )之蒸氣領域下進行 3 0秒之蒸氣洗淨。進行觀測蒸氣洗淨之乾燥性,與浸漬 去水後混合溶劑之狀態,以及浸漬去水時,浮於混合溶劑 液面之水的狀態,依以下A〜D進行判定結果爲A者。a ;無斑點完全乾燥。B ;乾燥却稍有斑點。c ;殘存水份 。D ;殘留極多水份。 又,混合溶劑之狀態,依以下A〜D進行判定結果爲 A者。A ;無濁度。B ;稍有白濁感。c ;有白濁。D ; 強烈白濁狀。 另外,浮於液面之水狀態依以下A〜D進行判定結果 爲A者。A ;迅速浮上。B ;稍慢浮上。c ;浮上遲緩。 D ;水的浮上極爲緩慢。 本紙張尺度適用中國國家標準(CNS ) A4規格(210X297公釐) (請先閱讀背面之注意事項再填寫本頁) .i%4·For example, the method of change and change measurement \ 1 | / jIRi cd IX is the result. The paper size applies the Chinese National Standard (CNS) A4 specification (210X297 mm) -33- 593301 A7 B7 V. Description of the invention (h ( Example 1 1 to 3) Comparative Example The compound (6 a) was changed to octafluorocyclopentene except that it was measured by the method of Example 1 1-1 R. If the result was X, the contact etching reaction did not proceed at all, Shi Xi A yellow-brown polymer deposit on the wafer. [Example 1 2] As an evaluation example of dehydration and drying solvent, the stainless steel mesh sieve (5 cm X 5 cm) was washed in advance, and the person immersed in water was washed. Clean article. The compound (7 a) synthesized in Example 10 was directly used as the compound (7 b). After adding ethanol to the compound (7 b), the ethanol concentration was adjusted to a mixed solvent of 5% by mass. Then it was washed. The net was immersed in a mixed solvent at 30 ° C, and the water was removed by ultrasound for 1 minute. Then, the compound was cleaned by steam for 30 seconds in the steam field of compound (7 a). Observe the dryness of the steam wash, The state of the mixed solvent after immersion and removal of water, and the water floating on the liquid level of the mixed solvent when immersion is removed The state of A is determined by the following A to D. A: A; no spots are completely dry. B; dry but slightly spotted. C; residual moisture. D; extremely residual moisture. In addition, the state of the mixed solvent According to the following A ~ D, the judgment result is A. A; no turbidity. B; slightly white turbidity. C; white turbidity. D; strong white turbidity. In addition, the state of the water floating on the liquid surface is A ~ The result of D's judgment is A. A; floats quickly. B; floats slowly. C; floats slowly. D; water floats very slowly. This paper applies the Chinese National Standard (CNS) A4 specification (210X297 mm) ( (Please read the notes on the back before filling out this page) .i% 4 ·

、1T 經濟部智慧財產局員工消費合作社印製 - 34- 593301 A7 _B7_ 五、發明説明($2 〔例1 3〕 做爲洗淨劑及潤濕劑之評定例 (請先閱讀背面之注意事項再填寫本頁) 於預先洗淨之不銹鋼網篩(5 c m X 5 c m )進行塗 佈切削油(商品名:Daphnicut AS-40HO出光興產公司製) ,於1 0 0 °C下進行加熱1小時者做爲被洗淨物品。 將被洗淨物進行浸漬洗淨3 0秒於異十二烷(6 0 °C )中,以下例1 0取得之化合物(7 a )直接含化合物( 7 b )使用之。利用化合物(7 a )於3 0 t:下進行浸漬 潤濕3 0秒後,最後,於化合物(7 a )之蒸氣領域下進 行蒸氣洗淨3 0秒。 由切削油塗佈前及塗佈後,又洗淨乾燥後之被洗淨物 質量測定結果算出切削油之殘存率,且,觀察蒸氣洗淨後 之被洗淨物乾燥狀態,依以下基準進行評定之結果爲A者 。油之殘存率爲A ;小於〇 · 1重量%,B ; 〇 . 1重量 %〜0 · 5重量%,C ; 〇 · 5重量%〜2重量%,D ; 2重量%以上。另外,乾燥狀態依以下基準進行評之結果 爲A。A ;立刻乾燥,B ;慢慢乾燥,C ;部份乾燥,D ;未乾燥。 經濟部智慧財產局員工消費合作社印製 &lt;產業上可利用性&gt; 本發明爲提供一種適於工業上實施之方法者,且,於 經濟面有利之方法下’製造效率佳之氟化環狀醚之方法者 。本發明氟化環狀醚係做爲去水乾燥劑、乾蝕刻劑、或洗 淨劑等功能劑有用之化合物者,且,本發明可提供—種做 爲氟化環狀醚中間體有用之新穎化合物者。 本紙張尺度適用中國國家標準(CNS ) A4規格(210X297公釐) -35-Printed by the Consumer Cooperative of the Intellectual Property Bureau of the Ministry of Economic Affairs, 1T-34- 593301 A7 _B7_ V. Description of the invention ($ 2 [Example 1 3] As an example of the evaluation of detergents and wetting agents (Please read the precautions on the back before Fill in this page) Apply cutting oil (trade name: Daphnicut AS-40HO Idemitsu Kosan Co., Ltd.) to a stainless steel mesh sieve (5 cm X 5 cm) that has been cleaned in advance, and heat it at 100 ° C for 1 hour The object to be washed is immersed and washed in the isododecane (60 ° C) for 30 seconds. The compound (7 a) obtained in Example 10 below directly contains the compound (7 b ). Use compound (7 a) for 30 seconds at 30 t: dipping and wetting, and finally, steam clean in the steam area of compound (7 a) for 30 seconds. Coating with cutting oil The residual rate of cutting oil was calculated after measuring the mass of the cleaned material before and after coating and drying, and the dry state of the cleaned material after steam cleaning was observed. The result of evaluation based on the following criteria was A. The residual ratio of the oil is A; less than 0.1% by weight, and B; 0.1% by weight to 0.5% by weight 0.5% to 2% by weight, D; 2% by weight or more. In addition, the dry state is evaluated according to the following criteria and the result is A. A; immediately dried, B; slowly dried, C; partially dried , D; not dried. Printed by the Consumer Cooperatives of the Intellectual Property Bureau of the Ministry of Economic Affairs &lt; Industrial availability &gt; A method for a fluorinated cyclic ether with good efficiency. The fluorinated cyclic ether of the present invention is a compound useful as a functional agent such as a desiccant, a dry etchant, or a detergent, and the present invention can provide— As a novel compound useful as a fluorinated cyclic ether intermediate. This paper size is applicable to China National Standard (CNS) A4 (210X297 mm) -35-

Claims (1)

593301 A8 B8 C8 D8 澳本丨 i i Ό Β I ¥、申請專利範圍 第9110303 9號專利申請案 中文申請專利範圍修正本 民國93年1月30日修正 1 · 一種氟化不飽和環狀醚之製造方法,其特徵係下 式(5 )所示化合物經熱分解後,製得1種以上選自下式 (6 a )所示之化合物及下式(6 b )所示化合物之氟化 不飽和環狀醚者,但,A F代表全氟四氫呋喃基、X代表氟 原子、或一〇'M+ (其中,M +爲對離子)者 AF COX (5) (請先閲讀背面之注意事項再填寫本頁)593301 A8 B8 C8 D8 Australian version 丨 ii Ό Β I ¥, Patent Application No. 9110303 Patent Application No. 9 Chinese Application for Patent Scope Amendment January 30, 1993 Amendment 1 · Manufacture of a fluorinated unsaturated cyclic ether The method is characterized in that, after thermally decomposing a compound represented by the following formula (5), one or more compounds selected from the compounds represented by the following formula (6 a) and the compounds represented by the following formula (6 b) are fluorinated and unsaturated. For cyclic ethers, however, AF represents perfluorotetrahydrofuranyl, X represents a fluorine atom, or 10′M + (where M + is a counter ion). AF COX (5) (Please read the precautions on the back before completing this page) (6 a) F(6 a) F (6b) 經濟部智慧財產局員工消費合作社印製 物 2 .如申請專利範圍第l項之製造方法,其中該式 所示之化合物爲下式(5 a )所示之化合物者(6b) Printed by the Consumer Cooperative of the Intellectual Property Bureau of the Ministry of Economic Affairs 2. The manufacturing method as described in item 1 of the scope of patent application, wherein the compound represented by the formula is a compound represented by the following formula (5 a) 3 ·如申請專利範圍第1項之製造方法,其中該式( 所示化合物中,X爲氟原子之下式(5 ί )所示化合 而,下式(1 )所示化合物與下式(2 )所示化合物 本紙張尺度適用中國國家標準(CNS ) Α4規格(21〇Χ297公釐) 593301 8 88 8 ABCD 六、申請專利範圍 經反應後做爲下式(3 )所示化合物,該式(3 )所示化 合物經氟化做爲下式(4 )所示化合物,該式(4 )所示 之化合物酯鍵結進行分解反應後取得之化合物, 其中,A F與上記相同意味者,r c代表1價有機基, R c F與R c爲相同之1價有機基,或R C代表被氟化之1價 有機基,X1代表鹵原子,A爲選自下式(la)、下式( lb)、下式(lc)及下式(id)之式所代表基,或 該選取式中氫原子1個以上被氟原子取代之式所代表之基 者。 ACH2〇H (1) RcC〇X] (2) ACH2 OCORc (3) AF CF2 OCORCF (4) AF C〇F (5 f ) ---------βί ^-- (請先閱讀背面之注意事項再填寫本頁) 、1Τ3. The manufacturing method according to item 1 of the scope of patent application, wherein in the compound shown in the formula (where X is a fluorine atom, X is a compound represented by the formula (5)), and the compound represented by the following formula (1) and the following formula ( 2) Compounds shown on this paper are in accordance with Chinese National Standard (CNS) A4 specifications (21 × 297 mm) 593301 8 88 8 ABCD 6. The scope of patent application is reacted as the compound shown by formula (3) below. (3) The compound represented by the following formula (4) is fluorinated as a compound represented by the following formula (4), and the compound obtained by the ester bond of the compound represented by the formula (4) is obtained by a decomposition reaction, where AF has the same meaning as the above, rc Represents a monovalent organic group, R c F and R c are the same monovalent organic group, or RC represents a fluorinated monovalent organic group, X1 represents a halogen atom, and A is selected from the following formula (la), the following formula ( lb), the group represented by the following formula (lc) and the following formula (id), or the group represented by the formula in which one or more hydrogen atoms are replaced by fluorine atoms: ACH2〇H (1) RcC. X] (2) ACH2 OCORc (3) AF CF2 OCORCF (4) AF C〇F (5 f) --------- βί ^-(Please read the notes on the back first Then fill out this page), 1Τ (la) (lb) (lc) (id) 經濟部智慧財產局員工消費合作社印製 o 4 ·如申請專利範圍第3項之製造方法,其中該式( 1 )所不化合物爲下式(1 )所示之化合物、式(3 )所 示化合物爲下式(3 )所代表之化合物、式(4 )所示之 化合物中AF爲2 —全氟四氫呋喃基、式(5 f )所示之化 合物爲下式(5a)所示之化合物者, 其中,Rc與上記意義相同者,A1爲選自下式(1 a 一 1)、下式(lb — 1)、下式(lc — 1)、及下式 本紙張尺度適用中國國家標準(CNS ) A4規格(210X297公釐)-2 - 593301 Λ8 B8 C8 ______ DS 六、申請專利範圍 上氫原子 (1 d — 1 )所代表之基 '或該選取式中;L個以 爲被氟原子取代所示之基者, A3 CH2 OH ⑴ A3 CH2 〇C〇Rc (3)(la) (lb) (lc) (id) Printed by the Consumer Cooperatives of the Intellectual Property Bureau of the Ministry of Economic Affairs. o As in the manufacturing method for the third item of the patent application, where the compound in formula (1) is the following formula (1) The compound represented by) and the compound represented by formula (3) are compounds represented by the following formula (3). Among the compounds represented by formula (4), AF is 2-perfluorotetrahydrofuranyl, and the compound represented by formula (5f) The compound is a compound represented by the following formula (5a), wherein Rc has the same meaning as the above, and A1 is selected from the following formula (1 a to 1), the following formula (lb — 1), and the following formula (lc — 1) The following paper standards apply to the Chinese National Standard (CNS) A4 specifications (210X297 mm)-2-5330301 Λ8 B8 C8 ______ DS VI. The base represented by the hydrogen atom (1 d — 1) on the scope of patent application 'or In this selection formula, L is a group shown to be substituted by a fluorine atom, A3 CH2 OH ⑴ A3 CH2 〇C〇Rc (3) (la_l) (lb-1) (1c -1) (Id -1)(la_l) (lb-1) (1c -1) (Id -1) 5 ·如申請專利範圍第3項或第4項之製造 中該式(3 )所示之化合物係由式(4 )所示化 鍵結經分解反應之反應生成物取得式(5 )所示 下式(2 a )所示化合物後,該式(2 a )所示 式(1 )所示化合物相互反應後取得之化合物, 其中,.R e F與上記爲相同意義者 R c F 〇 C F (2a) 。 6 · —種氟化不飽和環狀醚之製造方法,其 式(1 )所示化合物與下式(2 )所示化合物經 爲下式(3 )所示化合物,該式(3 )所示化合 中與氟反應經氟化做爲下式(4 )所示化合物, )所示之化合物酯鍵結進行分解反應後成爲下式 示之化合物,將該式(5ί)所示之化合物予以熱 獲得選自下式(62)所示之化合物及下式(6b) 本纸张尺度適用中國國家.標準(CNS )人4反格(2丨OX 297公潑) 方法,其 合物之酯 化合物與 化合物與 部 智 慧 財 k h 員 工 消 f 合 作 社 印 特徵係下 反應後做 物在液相 該式(4 (5f )所 分解,而 所示之化 W301 Λ8 B8 C8 ^__ T、申請專利範圍 合物之一種以上氟化不飽和環狀醚者, 但’ A F與上記相同意義,R c代表1價有機基, R e F與R e爲相同之1價有機基,或R c代表被氟化之1價 有機基,X1代表鹵原子,A爲選自下式(la)、下式( lb)、下式(lc)及下式(Id)之式所代表之基, 或該選取式中氫原子1個以上被氟原子取代之式所代表之 基者。 A C Η 2 Ο Η ( 1 ) (3 ) (4 ) (5 f ) 經濟部智慧財產局員工涓費合作社印製5. If the compound represented by formula (3) in the manufacture of item 3 or 4 of the scope of application for a patent is obtained from the reaction product of the chemical bond and decomposition reaction obtained by formula (4), the formula (5) is obtained. After the compound represented by the following formula (2a), the compound obtained by the reaction of the compound represented by the formula (1) represented by the formula (2a), wherein .R e F is the same as R c F 〇CF (2a). 6. A method for producing a fluorinated unsaturated cyclic ether, wherein the compound represented by the formula (1) and the compound represented by the following formula (2) are compounds represented by the following formula (3), and the formula (3) The reaction with fluorine in the compound is fluorinated to form a compound represented by the following formula (4), and the compound represented by) is ester-bonded to undergo a decomposition reaction to become a compound represented by the following formula. This paper is selected from the compound shown by the following formula (62) and the following formula (6b). The paper size is applicable to the Chinese national standard. (CNS) standard 4 inverse (2 丨 OX 297). The ester compound of the compound and The compound reacts with the Ministry of Intellectual Property, employees, and cooperatives, and the product is decomposed in the liquid phase by the formula (4 (5f)), and the chemical composition shown is W301 Λ8 B8 C8 ^ __ T. One or more fluorinated unsaturated cyclic ethers, but 'AF has the same meaning as above, R c represents a monovalent organic group, R e F and Re are the same monovalent organic group, or R c represents one fluorinated one. Valent organic group, X1 represents a halogen atom, and A is selected from the following formula (la), the following formula (lb), and the following formula (Lc) and the base represented by the following formula (Id), or the base represented by the formula in which one or more hydrogen atoms are replaced by fluorine atoms: AC 选取 2 Ο Η (1) (3) ( 4) (5 f) Printed by the staff of the Intellectual Property Bureau of the Ministry of Economy (讀先閱讀背面之注ί項再填寫本頁) d (3c) (Id) 7 · —種氟化飽和環狀醚之製造方法,其特徵係下式 (5 )所示化合物經熱分解後取得1種以上選自下式(6 a )所示化合物及下式(6 b )所示化合物之化合物後, 本纸張尺度適用中國國家標準(〇奶)六^说格(2】0&gt;( 297;分) 593301 A8 B8 C8 D8 六、申請專利範圍 爯進行該1種以上化合物之還原反應後,取得1種以上選 自式(6 a )所示化合物被還原之下式(7 a )所示化合 物及式(6 b )所示化合物被還原之式(7 b )所示化合 物之氟化飽和環狀醚者, 其中,人1:及)(分別與上述之意義爲相同者 AF COX (5)(Please read the note on the back and read this page first, then fill in this page) d (3c) (Id) 7 · —A method for producing a fluorinated saturated cyclic ether, which is characterized by the thermal decomposition of the compound represented by the following formula (5) After obtaining more than one compound selected from the compound represented by the following formula (6 a) and the compound represented by the following formula (6 b), the paper size applies the Chinese national standard (〇 奶) 六 ^ 格格 (2) 0 &gt;(297; points) 593301 A8 B8 C8 D8 6. Scope of patent application: After performing the reduction reaction of more than one compound, one or more compounds selected from the formula (6 a) are reduced to the following formula (7 a) A compound represented by the formula and a compound represented by the formula (6 b) which has been reduced is a fluorinated saturated cyclic ether of the compound represented by the formula (7 b), in which, human 1: and) (respectively have the same meaning as the above AF COX (5) (6a) F R F(6a) F R F Η (7 a)Η (7 a) (6b) ρ (7b) 8 .如申請專利範圍第7項之製造方法,其中該式 5 )所示之化合物爲下式(5 a )所示之化合物者 F' F(6b) ρ (7b) 8. The manufacturing method according to item 7 of the scope of patent application, wherein the compound represented by formula 5) is a compound represented by the following formula (5a) F 'F F—^——F .F (5a) COF 9 · 一種以下式(3a — 2) 、(3b - 2) 、 (4 經濟部智慧財產局員工消費合作社印一·次 (讀先閱讀背面之注項再填寫本頁) b — 2 )所示之任一化合物,其中R e 1及R e F 1係分別示 全氟化烷基' 全氟化(部份氯烷基)基、全氟化(含有醚 性氧原子之烷基)基' 全氟化(部份氯(含有醚性氧原子 之烷基)基或全氟化四氫呋喃基。 本纸張尺度速用中國國家禕準(CNS ) A4規格(2)0&gt;(297公釐) 州301 Α8 Β8 C8 D8 、申請專利範圍F — ^ —— F .F (5a) COF 9 · One of the following formulas (3a — 2), (3b-2), (4 Employee Cooperatives of the Intellectual Property Bureau of the Ministry of Economic Affairs printed one time (read the note on the back first) Please fill in this page again for any one of the compounds shown in b) 2), in which Re 1 and Re F 1 respectively show perfluorinated alkyl 'perfluorinated (partially chloroalkyl) and perfluorinated (Alkyl group containing etheric oxygen atom) group 'Perfluorinated (partially chlorinated (alkyl group containing etheric oxygen atom) group or perfluorinated tetrahydrofuranyl group. This paper is based on China National Standards (CNS) A4 specifications (2) 0 &gt; (297 mm) State 301 Α8 Β8 C8 D8, patent application scope CH2〇C〇Rc] 、〇/ \cH2〇C〇RC] CF] (3b-2) (4b-2) 1 〇 · —種功能劑,其特徵含有1種以上選自下式( 6 a )所示化合物及下式(6 b )所示之化合物之氟化不 飽和環狀醚,或1種以上選自下式(7 a )所示化合物及 下式(7 b )所示之化合物之氟化飽和環狀醚者 F\ JP K F F (6a) FCH2〇C〇Rc], 〇 / \ cH2〇C〇RC] CF] (3b-2) (4b-2) 1 〇 ·-a functional agent containing one or more selected from the following formula (6 a) Fluorinated unsaturated cyclic ether of the compound represented by the formula and the compound represented by the following formula (6 b), or one or more selected from the compounds represented by the following formula (7 a) and the compound represented by the following formula (7 b) Fluorinated saturated cyclic ether F \ JP KFF (6a) F (6b) ^---- -- —II —J)i — i i - - - · I I I 1 · (請先閲讀背面之注項再填寫本頁)(6b) ^ -----—II —J) i — i i---· I I I 1 · (Please read the note on the back before filling this page) (7a) F(7a) F F (7b) 種功能劑,其特徵爲含下式(7 a )所示之 、1T 化合物者F (7b) functional agents, characterized by containing a 1T compound represented by the following formula (7a) Η (7a) 絲 經濟部智慧財產局員工消費合作社印製 1 2 .如申請專利範圍第1 〇項或第1 1項之功能劑 ,其中該功能劑爲去水乾燥溶劑 '乾蝕刻劑、或洗淨劑者 本纸张尺皮逷用中國國家標準(CNS ) Μ規格(2]ϋΧ 297公分)7 (7a) Printed by the Consumer Cooperative of the Intellectual Property Bureau of the Ministry of Silk Economy 1 2. If the functional agent in the scope of patent application No. 10 or No. 11 is used, the functional agent is a dehydrating solvent, a dry etchant, or Detergents This paper uses the Chinese national standard (CNS) M specifications (2) (× 297 cm)
TW91103039A 2001-02-21 2002-02-21 Processes for producing fluorinated cyclic ethers and use thereof TW593301B (en)

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US20050011859A1 (en) * 2003-07-15 2005-01-20 Bing Ji Unsaturated oxygenated fluorocarbons for selective aniostropic etch applications
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