JPH01294668A - Production of polycarboxylic acid anhydride isomer - Google Patents
Production of polycarboxylic acid anhydride isomerInfo
- Publication number
- JPH01294668A JPH01294668A JP12533988A JP12533988A JPH01294668A JP H01294668 A JPH01294668 A JP H01294668A JP 12533988 A JP12533988 A JP 12533988A JP 12533988 A JP12533988 A JP 12533988A JP H01294668 A JPH01294668 A JP H01294668A
- Authority
- JP
- Japan
- Prior art keywords
- acid anhydride
- anhydride
- amine
- catalyst
- adsorbent
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Granted
Links
- 150000008065 acid anhydrides Chemical class 0.000 title claims abstract description 21
- 238000004519 manufacturing process Methods 0.000 title claims description 5
- 239000003054 catalyst Substances 0.000 claims abstract description 20
- 238000006317 isomerization reaction Methods 0.000 claims abstract description 18
- 239000003463 adsorbent Substances 0.000 claims abstract description 13
- 150000001412 amines Chemical class 0.000 claims abstract description 8
- FEWJPZIEWOKRBE-UHFFFAOYSA-N Tartaric Acid Chemical compound [H+].[H+].[O-]C(=O)C(O)C(O)C([O-])=O FEWJPZIEWOKRBE-UHFFFAOYSA-N 0.000 claims abstract description 6
- 125000002723 alicyclic group Chemical group 0.000 claims abstract description 5
- 239000000203 mixture Substances 0.000 abstract description 19
- -1 amine compound Chemical class 0.000 abstract description 13
- 150000001875 compounds Chemical class 0.000 abstract description 10
- 239000002994 raw material Substances 0.000 abstract description 7
- PNEYBMLMFCGWSK-UHFFFAOYSA-N aluminium oxide Inorganic materials [O-2].[O-2].[O-2].[Al+3].[Al+3] PNEYBMLMFCGWSK-UHFFFAOYSA-N 0.000 abstract description 5
- 239000004927 clay Substances 0.000 abstract description 5
- 238000000034 method Methods 0.000 abstract description 5
- 239000003822 epoxy resin Substances 0.000 abstract description 4
- 229920000647 polyepoxide Polymers 0.000 abstract description 4
- GETQZCLCWQTVFV-UHFFFAOYSA-N trimethylamine Chemical compound CN(C)C GETQZCLCWQTVFV-UHFFFAOYSA-N 0.000 abstract description 4
- YKTSYUJCYHOUJP-UHFFFAOYSA-N [O--].[Al+3].[Al+3].[O-][Si]([O-])([O-])[O-] Chemical compound [O--].[Al+3].[Al+3].[O-][Si]([O-])([O-])[O-] YKTSYUJCYHOUJP-UHFFFAOYSA-N 0.000 abstract description 3
- ULKLGIFJWFIQFF-UHFFFAOYSA-N 5K8XI641G3 Chemical compound CCC1=NC=C(C)N1 ULKLGIFJWFIQFF-UHFFFAOYSA-N 0.000 abstract description 2
- 239000004645 polyester resin Substances 0.000 abstract description 2
- 229920001225 polyester resin Polymers 0.000 abstract description 2
- 239000004848 polyfunctional curative Substances 0.000 abstract 1
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 20
- 229910052757 nitrogen Inorganic materials 0.000 description 10
- 150000008064 anhydrides Chemical class 0.000 description 7
- ZMANZCXQSJIPKH-UHFFFAOYSA-N Triethylamine Chemical compound CCN(CC)CC ZMANZCXQSJIPKH-UHFFFAOYSA-N 0.000 description 6
- 150000001244 carboxylic acid anhydrides Chemical class 0.000 description 6
- 238000001179 sorption measurement Methods 0.000 description 5
- 238000000746 purification Methods 0.000 description 4
- 239000002253 acid Substances 0.000 description 3
- 239000003795 chemical substances by application Substances 0.000 description 3
- 239000011261 inert gas Substances 0.000 description 3
- 239000007788 liquid Substances 0.000 description 3
- XPEKVUUBSDFMDR-UHFFFAOYSA-N 4-methyl-3a,4,7,7a-tetrahydro-2-benzofuran-1,3-dione Chemical compound CC1C=CCC2C(=O)OC(=O)C12 XPEKVUUBSDFMDR-UHFFFAOYSA-N 0.000 description 2
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 description 2
- 229910021536 Zeolite Inorganic materials 0.000 description 2
- 238000006243 chemical reaction Methods 0.000 description 2
- HNPSIPDUKPIQMN-UHFFFAOYSA-N dioxosilane;oxo(oxoalumanyloxy)alumane Chemical compound O=[Si]=O.O=[Al]O[Al]=O HNPSIPDUKPIQMN-UHFFFAOYSA-N 0.000 description 2
- 238000004821 distillation Methods 0.000 description 2
- 238000001914 filtration Methods 0.000 description 2
- DAZXVJBJRMWXJP-UHFFFAOYSA-N n,n-dimethylethylamine Chemical compound CCN(C)C DAZXVJBJRMWXJP-UHFFFAOYSA-N 0.000 description 2
- RMAQACBXLXPBSY-UHFFFAOYSA-N silicic acid Chemical compound O[Si](O)(O)O RMAQACBXLXPBSY-UHFFFAOYSA-N 0.000 description 2
- 235000012239 silicon dioxide Nutrition 0.000 description 2
- 239000007787 solid Substances 0.000 description 2
- 239000000126 substance Substances 0.000 description 2
- 239000010457 zeolite Substances 0.000 description 2
- LTVUCOSIZFEASK-MPXCPUAZSA-N (3ar,4s,7r,7as)-3a-methyl-3a,4,7,7a-tetrahydro-4,7-methano-2-benzofuran-1,3-dione Chemical compound C([C@H]1C=C2)[C@H]2[C@H]2[C@]1(C)C(=O)OC2=O LTVUCOSIZFEASK-MPXCPUAZSA-N 0.000 description 1
- KNDQHSIWLOJIGP-UMRXKNAASA-N (3ar,4s,7r,7as)-rel-3a,4,7,7a-tetrahydro-4,7-methanoisobenzofuran-1,3-dione Chemical compound O=C1OC(=O)[C@@H]2[C@H]1[C@]1([H])C=C[C@@]2([H])C1 KNDQHSIWLOJIGP-UMRXKNAASA-N 0.000 description 1
- MUTGBJKUEZFXGO-OLQVQODUSA-N (3as,7ar)-3a,4,5,6,7,7a-hexahydro-2-benzofuran-1,3-dione Chemical compound C1CCC[C@@H]2C(=O)OC(=O)[C@@H]21 MUTGBJKUEZFXGO-OLQVQODUSA-N 0.000 description 1
- KMOUUZVZFBCRAM-OLQVQODUSA-N (3as,7ar)-3a,4,7,7a-tetrahydro-2-benzofuran-1,3-dione Chemical compound C1C=CC[C@@H]2C(=O)OC(=O)[C@@H]21 KMOUUZVZFBCRAM-OLQVQODUSA-N 0.000 description 1
- FALRKNHUBBKYCC-UHFFFAOYSA-N 2-(chloromethyl)pyridine-3-carbonitrile Chemical compound ClCC1=NC=CC=C1C#N FALRKNHUBBKYCC-UHFFFAOYSA-N 0.000 description 1
- VQVIHDPBMFABCQ-UHFFFAOYSA-N 5-(1,3-dioxo-2-benzofuran-5-carbonyl)-2-benzofuran-1,3-dione Chemical compound C1=C2C(=O)OC(=O)C2=CC(C(C=2C=C3C(=O)OC(=O)C3=CC=2)=O)=C1 VQVIHDPBMFABCQ-UHFFFAOYSA-N 0.000 description 1
- MWSKJDNQKGCKPA-UHFFFAOYSA-N 6-methyl-3a,4,5,7a-tetrahydro-2-benzofuran-1,3-dione Chemical compound C1CC(C)=CC2C(=O)OC(=O)C12 MWSKJDNQKGCKPA-UHFFFAOYSA-N 0.000 description 1
- 239000005995 Aluminium silicate Substances 0.000 description 1
- JLTDJTHDQAWBAV-UHFFFAOYSA-N N,N-dimethylaniline Chemical compound CN(C)C1=CC=CC=C1 JLTDJTHDQAWBAV-UHFFFAOYSA-N 0.000 description 1
- LGRFSURHDFAFJT-UHFFFAOYSA-N Phthalic anhydride Natural products C1=CC=C2C(=O)OC(=O)C2=C1 LGRFSURHDFAFJT-UHFFFAOYSA-N 0.000 description 1
- GSEJCLTVZPLZKY-UHFFFAOYSA-N Triethanolamine Chemical compound OCCN(CCO)CCO GSEJCLTVZPLZKY-UHFFFAOYSA-N 0.000 description 1
- 230000002378 acidificating effect Effects 0.000 description 1
- 125000001931 aliphatic group Chemical group 0.000 description 1
- 229910000272 alkali metal oxide Inorganic materials 0.000 description 1
- 125000000217 alkyl group Chemical group 0.000 description 1
- 235000012211 aluminium silicate Nutrition 0.000 description 1
- 150000004982 aromatic amines Chemical class 0.000 description 1
- 239000000440 bentonite Substances 0.000 description 1
- 229910000278 bentonite Inorganic materials 0.000 description 1
- SVPXDRXYRYOSEX-UHFFFAOYSA-N bentoquatam Chemical compound O.O=[Si]=O.O=[Al]O[Al]=O SVPXDRXYRYOSEX-UHFFFAOYSA-N 0.000 description 1
- JHIWVOJDXOSYLW-UHFFFAOYSA-N butyl 2,2-difluorocyclopropane-1-carboxylate Chemical compound CCCCOC(=O)C1CC1(F)F JHIWVOJDXOSYLW-UHFFFAOYSA-N 0.000 description 1
- 125000004432 carbon atom Chemical group C* 0.000 description 1
- 238000005266 casting Methods 0.000 description 1
- 230000003197 catalytic effect Effects 0.000 description 1
- 230000000052 comparative effect Effects 0.000 description 1
- 238000005443 coulometric titration Methods 0.000 description 1
- 125000003438 dodecyl group Chemical group [H]C([H])([H])C([H])([H])C([H])([H])C([H])([H])C([H])([H])C([H])([H])C([H])([H])C([H])([H])C([H])([H])C([H])([H])C([H])([H])C([H])([H])* 0.000 description 1
- 230000008014 freezing Effects 0.000 description 1
- 238000007710 freezing Methods 0.000 description 1
- ANSXAPJVJOKRDJ-UHFFFAOYSA-N furo[3,4-f][2]benzofuran-1,3,5,7-tetrone Chemical compound C1=C2C(=O)OC(=O)C2=CC2=C1C(=O)OC2=O ANSXAPJVJOKRDJ-UHFFFAOYSA-N 0.000 description 1
- LNEPOXFFQSENCJ-UHFFFAOYSA-N haloperidol Chemical compound C1CC(O)(C=2C=CC(Cl)=CC=2)CCN1CCCC(=O)C1=CC=C(F)C=C1 LNEPOXFFQSENCJ-UHFFFAOYSA-N 0.000 description 1
- 150000002460 imidazoles Chemical class 0.000 description 1
- 229910052500 inorganic mineral Inorganic materials 0.000 description 1
- 239000011810 insulating material Substances 0.000 description 1
- 239000003456 ion exchange resin Substances 0.000 description 1
- 229920003303 ion-exchange polymer Polymers 0.000 description 1
- NLYAJNPCOHFWQQ-UHFFFAOYSA-N kaolin Chemical compound O.O.O=[Al]O[Si](=O)O[Si](=O)O[Al]=O NLYAJNPCOHFWQQ-UHFFFAOYSA-N 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- VYKXQOYUCMREIS-UHFFFAOYSA-N methylhexahydrophthalic anhydride Chemical compound C1CCCC2C(=O)OC(=O)C21C VYKXQOYUCMREIS-UHFFFAOYSA-N 0.000 description 1
- 239000011707 mineral Substances 0.000 description 1
- FZPXKEPZZOEPGX-UHFFFAOYSA-N n,n-dibutylaniline Chemical compound CCCCN(CCCC)C1=CC=CC=C1 FZPXKEPZZOEPGX-UHFFFAOYSA-N 0.000 description 1
- YWFWDNVOPHGWMX-UHFFFAOYSA-N n,n-dimethyldodecan-1-amine Chemical compound CCCCCCCCCCCCN(C)C YWFWDNVOPHGWMX-UHFFFAOYSA-N 0.000 description 1
- SMBYUOXUISCLCF-UHFFFAOYSA-N n-ethyl-n-methylpropan-1-amine Chemical compound CCCN(C)CC SMBYUOXUISCLCF-UHFFFAOYSA-N 0.000 description 1
- 229930014626 natural product Natural products 0.000 description 1
- 229910001562 pearlite Inorganic materials 0.000 description 1
- 150000003018 phosphorus compounds Chemical class 0.000 description 1
- 229920000728 polyester Polymers 0.000 description 1
- 238000002360 preparation method Methods 0.000 description 1
- 238000003672 processing method Methods 0.000 description 1
- 150000003242 quaternary ammonium salts Chemical class 0.000 description 1
- 238000007789 sealing Methods 0.000 description 1
- 239000000377 silicon dioxide Substances 0.000 description 1
- 238000003860 storage Methods 0.000 description 1
- 229940014800 succinic anhydride Drugs 0.000 description 1
- IMFACGCPASFAPR-UHFFFAOYSA-N tributylamine Chemical compound CCCCN(CCCC)CCCC IMFACGCPASFAPR-UHFFFAOYSA-N 0.000 description 1
- SRPWOOOHEPICQU-UHFFFAOYSA-N trimellitic anhydride Chemical compound OC(=O)C1=CC=C2C(=O)OC(=O)C2=C1 SRPWOOOHEPICQU-UHFFFAOYSA-N 0.000 description 1
- 239000002966 varnish Substances 0.000 description 1
Landscapes
- Furan Compounds (AREA)
- Solid-Sorbent Or Filter-Aiding Compositions (AREA)
- Low-Molecular Organic Synthesis Reactions Using Catalysts (AREA)
Abstract
Description
【発明の詳細な説明】
[産業上の利用分野]
本発明は、立体異性化によるポリカルボン酸無水物異性
体の製造方法に関する。DETAILED DESCRIPTION OF THE INVENTION [Industrial Field of Application] The present invention relates to a method for producing polycarboxylic acid anhydride isomers by stereoisomerization.
[従来の技術とその課題]
不飽和脂環式1.2−ジカルボン酸無水物はエポキシ樹
脂硬化剤やポリエステル樹脂原料として工業的に大いに
利用されており、作業性の観点から常温で液状物が賞月
される。[Prior art and its problems] Unsaturated alicyclic 1,2-dicarboxylic acid anhydrides are widely used industrially as epoxy resin curing agents and polyester resin raw materials, and from the viewpoint of workability, they cannot be liquid at room temperature. Awarded.
一般に、不飽和1.2−ジカルボン酸無水物の単独ある
いは混合物を立体異性化することによって常温で液状の
酸無水物が得られることはよく知られている。斯かる立
体異性化に適する触媒として、各種の異性化触媒が提案
されており、具体的には、アルカリ金属酸化物(特公昭
58−54146号)、酸性イオン交換樹脂(特公昭5
9−3997@)、第4級アンモニウム塩(特公昭58
−34476号)、リン系化合物(特開昭55−339
号)、アミン系化合物(特開昭54−151941号)
等が例示される。これらの中でも、アミン系化合物は、
特に優れた異性化触媒能を有している。It is generally well known that acid anhydrides that are liquid at room temperature can be obtained by stereoisomerizing unsaturated 1,2-dicarboxylic acid anhydrides alone or in mixtures. Various isomerization catalysts have been proposed as catalysts suitable for such stereoisomerization, specifically, alkali metal oxides (Japanese Patent Publication No. 58-54146), acidic ion exchange resins (Japanese Patent Publication No.
9-3997@), quaternary ammonium salt (Special Publication No. 1983)
-34476), phosphorus compounds (JP-A-55-339)
No.), amine compounds (Japanese Unexamined Patent Publication No. 151941/1983)
etc. are exemplified. Among these, amine compounds are
It has particularly excellent isomerization catalytic ability.
しかしながら、アミン系化合物を触媒として用いて得ら
れたポリカルボン酸無水物異性体をそのまま精製工程な
しにエポキシ樹脂硬化剤として用いた場合、貯蔵中に吸
湿して無水基が開環する等して変質し易くなる傾向が認
められ、これを解消するためには精製工程が不可欠であ
るが、これまでの蒸留による精製方法では収率よ(異性
体を得ることが出来なかった。However, if the polycarboxylic anhydride isomer obtained using an amine compound as a catalyst is used as an epoxy resin curing agent without a purification process, it may absorb moisture during storage and open the anhydride group. It has been observed that there is a tendency for the product to deteriorate easily, and a purification step is essential to overcome this problem, but the conventional purification method using distillation has not been able to obtain isomers at a low yield.
本発明者らは、斯かる現状に鑑み、蒸留により精製する
ことなく触媒を除去し、収率よくポリカルボン酸無水物
異性体を得ることを目的に鋭意検討した結果、異性化触
媒で必るアミン系化合物は、特定の化合物に効率良く吸
着され、斯かる化合物を用いて吸着処理することによっ
て所期の目的が達成されることを見い出し、この知見に
基づいて本発明を完成するに至った。In view of the current situation, the present inventors have conducted extensive studies with the aim of removing the catalyst without purification by distillation and obtaining polycarboxylic acid anhydride isomers in good yield. The inventors discovered that amine compounds are efficiently adsorbed by specific compounds, and that the intended purpose can be achieved by adsorption treatment using such compounds, and based on this knowledge, the present invention was completed. .
即ち、本発明は、アミン系異性化触媒を容易に除去し得
る工程を含む、工業的に優れ、かつ高収率でポリカルボ
ン酸異性体を製造する新規な方法を提供することを目的
とする。That is, an object of the present invention is to provide a novel method for producing polycarboxylic acid isomers in an industrially superior and high yield, which includes a step in which the amine-based isomerization catalyst can be easily removed. .
[課題を解決するための手段]
本発明に係るポリカルボン酸異性体の製造方法は、不飽
和脂環式1,2−ジカルボン酸無水物をアミン系触媒の
存在下で異性化して対応する立体異性体を製造するに際
し、アミン系異性化触媒を吸着剤を用いて吸着除去する
ことを特徴とする。[Means for Solving the Problems] The method for producing polycarboxylic acid isomers according to the present invention comprises isomerizing an unsaturated alicyclic 1,2-dicarboxylic acid anhydride in the presence of an amine catalyst to obtain the corresponding stereoisomer. When producing isomers, the amine isomerization catalyst is adsorbed and removed using an adsorbent.
本発明において原料となる不飽和1.2−ジカルボン酸
無水物とは、アミン系化合物によって立体異性化し得る
不飽和1,2−ジカルボン酸無水物であって、具体的に
はテトラヒドロ無水フタル酸の炭素数1〜8のアルキル
核置換体及びそれらの構造異性体並びにエンドメチレン
基を有する上記の酸無水物が例示され、より具体的には
3−メチル−△4−テトラヒドロ無水フタル酸及びその
構造異性体が例示される。The unsaturated 1,2-dicarboxylic anhydride used as a raw material in the present invention is an unsaturated 1,2-dicarboxylic anhydride that can be stereoisomerized with an amine compound, and specifically, it is an unsaturated 1,2-dicarboxylic anhydride that can be stereoisomerized with an amine compound. The above-mentioned acid anhydrides having an alkyl nucleus having 1 to 8 carbon atoms, structural isomers thereof, and endomethylene groups are exemplified, and more specifically, 3-methyl-△4-tetrahydrophthalic anhydride and its structure Examples include isomers.
異性化触媒としては、従来公知のアミン系化合物であれ
ばいずれでもよく、例えばトリメチルアミン、トリエチ
ルアミン、トリブチルアミン、ジメチルエチルアミン、
トリエタノールアミン、ジメチルエチルアミン、メチル
エチルプロピルアミン、ジメチルラウリルアミン、ジメ
チルアニリン、ジブチルアニリン等の脂肪族、脂環族若
しくは芳香族アミン、2−エチル−4−メチルイミダゾ
ール等のイミダゾール類が挙げられ、通常、酸無水物1
00重量部当り0.01〜2重量部程置部用される。The isomerization catalyst may be any conventionally known amine compound, such as trimethylamine, triethylamine, tributylamine, dimethylethylamine,
Examples include aliphatic, alicyclic or aromatic amines such as triethanolamine, dimethylethylamine, methylethylpropylamine, dimethyllaurylamine, dimethylaniline and dibutylaniline, imidazoles such as 2-ethyl-4-methylimidazole, Usually acid anhydride 1
It is used in an amount of 0.01 to 2 parts by weight per 00 parts by weight.
異性化反応は、90〜250℃程度の温度で1〜10時
間程度不活性ガス雰囲気下で反応させればよい。The isomerization reaction may be carried out at a temperature of about 90 to 250°C for about 1 to 10 hours under an inert gas atmosphere.
本発明に係る適当な吸着剤としては、シリカ−アルミナ
系化合物が例示される。Examples of suitable adsorbents according to the present invention include silica-alumina compounds.
ここで、シリカ−アルミナ系化合物とは、シリカとアル
ミナを含む組成を有するものであって、当該吸着反応に
関与し、所期の目的を達成し得るものであれば足り、具
体的にはベントナイト、パーライト、カオリン、ゼオラ
イト、活性白土等の天然物あるいはそれらから誘導され
た類似の性質を有する他の固体ケイ酸系物質及び人為的
に合成された前記の天然鉱物類と類似の性質を有する固
体ケイ酸系物質等が例示される。前記のシリカ−アルミ
ナ系化合物の中でも酸性度の高い化合物が好ましく、特
に、活性白土、合成ケイ酸アルミニウム等が推奨される
。Here, the silica-alumina compound has a composition containing silica and alumina, and is sufficient as long as it participates in the adsorption reaction and can achieve the intended purpose. Specifically, bentonite is used as a compound. , natural products such as pearlite, kaolin, zeolite, and activated clay, or other solid silicic acid-based substances derived from them that have similar properties, and artificially synthesized solids that have properties similar to the above-mentioned natural minerals. Examples include silicic acid-based substances. Among the above-mentioned silica-alumina compounds, compounds with high acidity are preferred, and activated clay, synthetic aluminum silicate, etc. are particularly recommended.
当該吸着剤の好ましい添加量は、アミン系化合物を含有
するポリカルボン酸無水物の異性体混合物100重舒部
に対し、0.01〜5重量部程置部より好ましくは0.
05〜3重量部であるが、触媒として用いたアミン系化
合物の種類によっては更に低濃度の使用も可能である。The adsorbent is preferably added in an amount of 0.01 to 5 parts by weight, preferably 0.01 to 5 parts by weight, per 100 parts by weight of the polycarboxylic anhydride isomer mixture containing the amine compound.
Although the amount is 0.5 to 3 parts by weight, it is possible to use an even lower concentration depending on the type of amine compound used as a catalyst.
本発明における一般的な処理方法を以下に示す。A general processing method in the present invention is shown below.
即ち、攪拌機、温度計、冷却器、不活性ガス導入口及び
減圧口のついた反応器に所定量の原料酸無水物異性体混
合物(異性化触媒を含んだもの)及び所定量の吸着剤を
仕込み、不活性ガス下あるいは必要に応じて減圧下O〜
200℃程度、好ましくは室温〜150℃の温度条件下
で10分〜5時間程度吸着処理する。吸着処理終了後、
濾過又は傾斜法により吸着剤を分離して、目的物である
アミン系化合物の少ない酸無水物を得る。That is, a predetermined amount of a raw material acid anhydride isomer mixture (containing an isomerization catalyst) and a predetermined amount of adsorbent are placed in a reactor equipped with a stirrer, a thermometer, a cooler, an inert gas inlet, and a pressure reduction port. Preparation, under inert gas or under reduced pressure if necessary.
The adsorption treatment is performed at a temperature of about 200°C, preferably room temperature to 150°C, for about 10 minutes to 5 hours. After the adsorption process is completed,
The adsorbent is separated by filtration or decanting to obtain the target acid anhydride containing less amine compounds.
又、必要に応じて他の多価カルボン酸無水物、例えば、
無水コハク酸、無水′フタル酸、無水トリメリット酸、
無水ピロメリット酸、無水ナジック酸、無水メチルナジ
ック酸、テトラヒドロ無水フタル酸、メチルテトラヒド
ロ無水フタル酸、ヘキサヒドロ無水フタル酸、メチルへ
キサヒドロ無水フタル酸、トチセニル無水コハク酸、ベ
ンゾフェノンテトラカルボン酸無水物等を異性化反応前
接並びに吸着処理前接に添加し、より低凝固点の液状ポ
リカルボン酸無水物としても差支えない。In addition, other polyvalent carboxylic acid anhydrides, such as
Succinic anhydride, phthalic anhydride, trimellitic anhydride,
Pyromellitic anhydride, nadic anhydride, methyl nadic anhydride, tetrahydrophthalic anhydride, methyltetrahydrophthalic anhydride, hexahydrophthalic anhydride, methylhexahydrophthalic anhydride, tothicenylsuccinic anhydride, benzophenonetetracarboxylic anhydride, etc. It may be added before the isomerization reaction or before the adsorption treatment to form a liquid polycarboxylic acid anhydride with a lower freezing point.
本発明に係るポリカルボン酸無水物は、ポリエステルの
酸成分として、又、電子部品の封止、電気部品の注型、
モーター用コイルの含浸ワニス等の絶縁材料としてのエ
ポキシ樹脂の硬化剤として優れた特性を有する。The polycarboxylic acid anhydride according to the present invention can be used as an acid component of polyester, as well as for sealing electronic parts, casting electric parts,
It has excellent properties as a hardening agent for epoxy resins used as insulating materials such as impregnated varnish for motor coils.
[実施例] 以下に実施例を示して本発明の詳細な説明する。[Example] The present invention will be described in detail below with reference to Examples.
尚、アミン系化合物の除去効果については、テルミュー
レン反応電量滴定方式により仝窒素分を測定して判断し
た。The effectiveness of removing amine compounds was determined by measuring the nitrogen content using the Termuerne reaction coulometric titration method.
実施例1
3−メチル−Δ4−テトラヒドロ無水フタル酸/4−メ
チル−Δ4−テトラヒドロ無水フタル酸−7/3(重量
比)の混合酸無水物100重量部に対し、異性化触媒と
してラウリルジメヂルアミンを500ppm添加し、こ
のものを180℃の温度条件下において3時間撹拌する
ことにより異性体混合物を1qだ。この異性体混合物中
に存在する窒素含量は33ppmであった。当該異性化
混合物に活性白土を異性化触媒の吸着剤として原料酸無
水物に対し1重量%添加し、120℃の加熱下、5 #
H’;Jの減圧下で1時間処理した。その後、このも
のを減圧濾過して窒素を0.lppm含有するカルボン
酸無水物を99%の収率で得た。Example 1 Lauryl dimedium was added as an isomerization catalyst to 100 parts by weight of a mixed acid anhydride of 3-methyl-Δ4-tetrahydrophthalic anhydride/4-methyl-Δ4-tetrahydrophthalic anhydride-7/3 (weight ratio). 500 ppm of Lamine was added, and the mixture was stirred at a temperature of 180° C. for 3 hours to obtain 1 q of the isomer mixture. The nitrogen content present in this isomer mixture was 33 ppm. Activated clay was added to the isomerization mixture in an amount of 1% by weight based on the raw material acid anhydride as an adsorbent for the isomerization catalyst, and heated at 120° C. to 5 #
The mixture was treated under reduced pressure H';J for 1 hour. After that, this material was filtered under reduced pressure to remove 0.0% nitrogen. A carboxylic acid anhydride containing 1 ppm was obtained with a yield of 99%.
実施例2
吸着剤として合成ケイ酸アルミニウムを原料酸無水物に
対し2重量%使用した以外は、実施例1に準じて異性体
混合物を処理した結果、窒素含量がo、ippmである
カルボン酸無水物が99%の収率で得られた。Example 2 An isomer mixture was treated according to Example 1, except that 2% by weight of synthetic aluminum silicate was used as an adsorbent based on the raw acid anhydride. As a result, a carboxylic acid anhydride with a nitrogen content of o, ippm was obtained. The product was obtained in 99% yield.
実施例3
実施例1と同様の混合酸無水物100重量部に対し、異
性化触媒としてトリエチルアミン200ppmを添加し
、このものを180℃の温度条件下において6時間撹拌
することにより異性体混合物を得た。この異性体混合物
中に存在する窒素含量は28ppmであった。当該異性
化混合物に活性白土を異性化触媒の吸着剤として原料酸
無水物に対し1重M%添加し、120℃の加熱下、常圧
下で1時間処理した。その債、このものを減圧濾過して
窒素含量が0.lppmであるカルボン酸無水物を99
%の収率で得た。Example 3 200 ppm of triethylamine was added as an isomerization catalyst to 100 parts by weight of the same mixed acid anhydride as in Example 1, and the mixture was stirred at a temperature of 180°C for 6 hours to obtain an isomer mixture. Ta. The nitrogen content present in this isomer mixture was 28 ppm. Activated clay was added to the isomerization mixture as an adsorbent for the isomerization catalyst in an amount of 1% by weight based on the raw material acid anhydride, and the mixture was heated at 120° C. and treated under normal pressure for 1 hour. After filtering this product under reduced pressure, the nitrogen content is 0. 99 lppm of carboxylic acid anhydride
% yield.
実施例4
吸着剤として合成ゼオライトを原料酸無水物に対し3重
量%使用した以外は、実施例3に準じて異性体混合物を
処理した結果、窒素含量が0.5ppmであるカルボン
酸無水物が99%の収率で得られた。Example 4 An isomer mixture was treated according to Example 3, except that 3% by weight of synthetic zeolite was used as an adsorbent based on the raw acid anhydride. As a result, a carboxylic acid anhydride with a nitrogen content of 0.5 ppm was obtained. Obtained with a yield of 99%.
実施例5
原料酸無水物として3−メチル−Δ4−テトラヒドロ無
水フタル酸を使用した以外は実施例1と同様に処理した
結果、窒素含量が0.2ppmであるカルボン酸無水物
が99%の収率で得られた。Example 5 As a result of the same treatment as in Example 1 except that 3-methyl-Δ4-tetrahydrophthalic anhydride was used as the raw material acid anhydride, a 99% yield of carboxylic acid anhydride with a nitrogen content of 0.2 ppm was obtained. obtained at a rate.
比較例1
実施例1で得られた異性体混合物(酸無水物中の窒素含
a=aappm)を単@留して得られた0、lppmの
窒素を含有する異性体混合物の収率は94%であった。Comparative Example 1 The yield of the isomer mixture containing 0.1 ppm of nitrogen obtained by single @ distillation of the isomer mixture obtained in Example 1 (nitrogen content a in acid anhydride = aappm) was 94 %Met.
特許出願人 新日本理化株式会社Patent applicant: Shin Nippon Rika Co., Ltd.
Claims (1)
系触媒の存在下で異性化して対応する立体異性体を製造
するに際し、アミン系異性化触媒を吸着剤を用いて吸着
除去することを特徴とするポリカルボン酸無水物異性体
の製造方法。1. When unsaturated alicyclic 1,2-dicarboxylic acid anhydride is isomerized in the presence of an amine catalyst to produce the corresponding stereoisomer, the amine isomerization catalyst is adsorbed and removed using an adsorbent. A method for producing a polycarboxylic acid anhydride isomer, characterized by:
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JP12533988A JP2720044B2 (en) | 1988-05-23 | 1988-05-23 | Method for producing polycarboxylic anhydride isomer |
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JP12533988A JP2720044B2 (en) | 1988-05-23 | 1988-05-23 | Method for producing polycarboxylic anhydride isomer |
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JP2720044B2 JP2720044B2 (en) | 1998-02-25 |
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