JP3433482B2 - Method for producing bismaleimide - Google Patents
Method for producing bismaleimideInfo
- Publication number
- JP3433482B2 JP3433482B2 JP26200293A JP26200293A JP3433482B2 JP 3433482 B2 JP3433482 B2 JP 3433482B2 JP 26200293 A JP26200293 A JP 26200293A JP 26200293 A JP26200293 A JP 26200293A JP 3433482 B2 JP3433482 B2 JP 3433482B2
- Authority
- JP
- Japan
- Prior art keywords
- bismaleimide
- solvent
- formula
- reaction
- acid
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired - Fee Related
Links
- XQUPVDVFXZDTLT-UHFFFAOYSA-N 1-[4-[[4-(2,5-dioxopyrrol-1-yl)phenyl]methyl]phenyl]pyrrole-2,5-dione Chemical compound O=C1C=CC(=O)N1C(C=C1)=CC=C1CC1=CC=C(N2C(C=CC2=O)=O)C=C1 XQUPVDVFXZDTLT-UHFFFAOYSA-N 0.000 title claims description 37
- 229920003192 poly(bis maleimide) Polymers 0.000 title claims description 37
- 238000004519 manufacturing process Methods 0.000 title claims description 9
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 17
- 239000003849 aromatic solvent Substances 0.000 claims description 16
- 238000006243 chemical reaction Methods 0.000 claims description 16
- 238000000034 method Methods 0.000 claims description 15
- 239000002253 acid Substances 0.000 claims description 12
- 239000012046 mixed solvent Substances 0.000 claims description 12
- 239000003377 acid catalyst Substances 0.000 claims description 11
- FPYJFEHAWHCUMM-UHFFFAOYSA-N maleic anhydride Chemical compound O=C1OC(=O)C=C1 FPYJFEHAWHCUMM-UHFFFAOYSA-N 0.000 claims description 11
- 239000002798 polar solvent Substances 0.000 claims description 11
- 238000007363 ring formation reaction Methods 0.000 claims description 11
- 150000004984 aromatic diamines Chemical class 0.000 claims description 10
- 238000006297 dehydration reaction Methods 0.000 claims description 10
- 238000007259 addition reaction Methods 0.000 claims description 9
- 230000018044 dehydration Effects 0.000 claims description 9
- 125000004435 hydrogen atom Chemical group [H]* 0.000 claims description 6
- KMKWGXGSGPYISJ-UHFFFAOYSA-N 4-[4-[2-[4-(4-aminophenoxy)phenyl]propan-2-yl]phenoxy]aniline Chemical compound C=1C=C(OC=2C=CC(N)=CC=2)C=CC=1C(C)(C)C(C=C1)=CC=C1OC1=CC=C(N)C=C1 KMKWGXGSGPYISJ-UHFFFAOYSA-N 0.000 claims description 5
- UHOVQNZJYSORNB-UHFFFAOYSA-N monobenzene Natural products C1=CC=CC=C1 UHOVQNZJYSORNB-UHFFFAOYSA-N 0.000 claims description 5
- 125000001997 phenyl group Chemical group [H]C1=C([H])C([H])=C(*)C([H])=C1[H] 0.000 claims description 5
- 125000000217 alkyl group Chemical group 0.000 claims description 4
- 125000004432 carbon atom Chemical group C* 0.000 claims description 4
- 125000002496 methyl group Chemical group [H]C([H])([H])* 0.000 claims description 4
- 239000000126 substance Substances 0.000 claims description 4
- 150000001555 benzenes Chemical class 0.000 claims description 3
- 150000001875 compounds Chemical class 0.000 claims description 2
- 125000005843 halogen group Chemical group 0.000 claims description 2
- URLKBWYHVLBVBO-UHFFFAOYSA-N Para-Xylene Chemical group CC1=CC=C(C)C=C1 URLKBWYHVLBVBO-UHFFFAOYSA-N 0.000 description 17
- 239000002904 solvent Substances 0.000 description 17
- YXFVVABEGXRONW-UHFFFAOYSA-N Toluene Chemical compound CC1=CC=CC=C1 YXFVVABEGXRONW-UHFFFAOYSA-N 0.000 description 11
- WFDIJRYMOXRFFG-UHFFFAOYSA-N Acetic anhydride Chemical compound CC(=O)OC(C)=O WFDIJRYMOXRFFG-UHFFFAOYSA-N 0.000 description 6
- ZMXDDKWLCZADIW-UHFFFAOYSA-N N,N-Dimethylformamide Chemical compound CN(C)C=O ZMXDDKWLCZADIW-UHFFFAOYSA-N 0.000 description 6
- 239000013078 crystal Substances 0.000 description 6
- 238000005406 washing Methods 0.000 description 6
- 238000002844 melting Methods 0.000 description 5
- 230000008018 melting Effects 0.000 description 5
- 238000003756 stirring Methods 0.000 description 5
- CSCPPACGZOOCGX-UHFFFAOYSA-N Acetone Chemical compound CC(C)=O CSCPPACGZOOCGX-UHFFFAOYSA-N 0.000 description 4
- SECXISVLQFMRJM-UHFFFAOYSA-N N-Methylpyrrolidone Chemical compound CN1CCCC1=O SECXISVLQFMRJM-UHFFFAOYSA-N 0.000 description 4
- NBIIXXVUZAFLBC-UHFFFAOYSA-N Phosphoric acid Chemical compound OP(O)(O)=O NBIIXXVUZAFLBC-UHFFFAOYSA-N 0.000 description 4
- 239000007788 liquid Substances 0.000 description 4
- 239000013557 residual solvent Substances 0.000 description 4
- NPDACUSDTOMAMK-UHFFFAOYSA-N 4-Chlorotoluene Chemical compound CC1=CC=C(Cl)C=C1 NPDACUSDTOMAMK-UHFFFAOYSA-N 0.000 description 3
- QTBSBXVTEAMEQO-UHFFFAOYSA-N Acetic acid Chemical compound CC(O)=O QTBSBXVTEAMEQO-UHFFFAOYSA-N 0.000 description 3
- OKKJLVBELUTLKV-UHFFFAOYSA-N Methanol Chemical compound OC OKKJLVBELUTLKV-UHFFFAOYSA-N 0.000 description 3
- ZMANZCXQSJIPKH-UHFFFAOYSA-N Triethylamine Chemical compound CCN(CC)CC ZMANZCXQSJIPKH-UHFFFAOYSA-N 0.000 description 3
- 238000009835 boiling Methods 0.000 description 3
- 239000012024 dehydrating agents Substances 0.000 description 3
- 238000001035 drying Methods 0.000 description 3
- FSQQTNAZHBEJLS-UPHRSURJSA-N maleamic acid Chemical compound NC(=O)\C=C/C(O)=O FSQQTNAZHBEJLS-UPHRSURJSA-N 0.000 description 3
- AUHZEENZYGFFBQ-UHFFFAOYSA-N mesitylene Substances CC1=CC(C)=CC(C)=C1 AUHZEENZYGFFBQ-UHFFFAOYSA-N 0.000 description 3
- 125000001827 mesitylenyl group Chemical group [H]C1=C(C(*)=C(C([H])=C1C([H])([H])[H])C([H])([H])[H])C([H])([H])[H] 0.000 description 3
- 239000000203 mixture Substances 0.000 description 3
- 229920000642 polymer Polymers 0.000 description 3
- 239000000843 powder Substances 0.000 description 3
- 239000000047 product Substances 0.000 description 3
- 238000010992 reflux Methods 0.000 description 3
- JOXIMZWYDAKGHI-UHFFFAOYSA-N toluene-4-sulfonic acid Chemical compound CC1=CC=C(S(O)(=O)=O)C=C1 JOXIMZWYDAKGHI-UHFFFAOYSA-N 0.000 description 3
- DSNHSQKRULAAEI-UHFFFAOYSA-N 1,4-Diethylbenzene Chemical compound CCC1=CC=C(CC)C=C1 DSNHSQKRULAAEI-UHFFFAOYSA-N 0.000 description 2
- IAZDPXIOMUYVGZ-UHFFFAOYSA-N Dimethylsulphoxide Chemical compound CS(C)=O IAZDPXIOMUYVGZ-UHFFFAOYSA-N 0.000 description 2
- YNQLUTRBYVCPMQ-UHFFFAOYSA-N Ethylbenzene Chemical compound CCC1=CC=CC=C1 YNQLUTRBYVCPMQ-UHFFFAOYSA-N 0.000 description 2
- ATUOYWHBWRKTHZ-UHFFFAOYSA-N Propane Chemical compound CCC ATUOYWHBWRKTHZ-UHFFFAOYSA-N 0.000 description 2
- QAOWNCQODCNURD-UHFFFAOYSA-N Sulfuric acid Chemical compound OS(O)(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-N 0.000 description 2
- WYURNTSHIVDZCO-UHFFFAOYSA-N Tetrahydrofuran Chemical compound C1CCOC1 WYURNTSHIVDZCO-UHFFFAOYSA-N 0.000 description 2
- DTQVDTLACAAQTR-UHFFFAOYSA-N Trifluoroacetic acid Chemical compound OC(=O)C(F)(F)F DTQVDTLACAAQTR-UHFFFAOYSA-N 0.000 description 2
- 238000013019 agitation Methods 0.000 description 2
- 229910000147 aluminium phosphate Inorganic materials 0.000 description 2
- 150000001408 amides Chemical class 0.000 description 2
- 150000001412 amines Chemical class 0.000 description 2
- 125000003277 amino group Chemical group 0.000 description 2
- 238000011088 calibration curve Methods 0.000 description 2
- 239000007810 chemical reaction solvent Substances 0.000 description 2
- MVPPADPHJFYWMZ-UHFFFAOYSA-N chlorobenzene Chemical compound ClC1=CC=CC=C1 MVPPADPHJFYWMZ-UHFFFAOYSA-N 0.000 description 2
- 150000004985 diamines Chemical class 0.000 description 2
- 239000007789 gas Substances 0.000 description 2
- 150000007524 organic acids Chemical class 0.000 description 2
- 238000001556 precipitation Methods 0.000 description 2
- CYSGHNMQYZDMIA-UHFFFAOYSA-N 1,3-Dimethyl-2-imidazolidinon Chemical compound CN1CCN(C)C1=O CYSGHNMQYZDMIA-UHFFFAOYSA-N 0.000 description 1
- YSHJKHGZZYAHAF-UHFFFAOYSA-N 4-(2-methyl-4-propylphenoxy)aniline Chemical compound CC1=CC(CCC)=CC=C1OC1=CC=C(N)C=C1 YSHJKHGZZYAHAF-UHFFFAOYSA-N 0.000 description 1
- XXBIBSRALRGHMT-UHFFFAOYSA-N 4-[4-[1-[4-(4-aminophenoxy)-3,5-dimethylphenyl]ethyl]-2,6-dimethylphenoxy]aniline Chemical compound C=1C(C)=C(OC=2C=CC(N)=CC=2)C(C)=CC=1C(C)C(C=C1C)=CC(C)=C1OC1=CC=C(N)C=C1 XXBIBSRALRGHMT-UHFFFAOYSA-N 0.000 description 1
- ZORDDHGAHBVRDS-UHFFFAOYSA-N 4-[4-[1-[4-(4-aminophenoxy)phenyl]-1-phenylethyl]phenoxy]aniline Chemical compound C=1C=C(OC=2C=CC(N)=CC=2)C=CC=1C(C=1C=CC(OC=2C=CC(N)=CC=2)=CC=1)(C)C1=CC=CC=C1 ZORDDHGAHBVRDS-UHFFFAOYSA-N 0.000 description 1
- SCPMRYRMHUNXQD-UHFFFAOYSA-N 4-[4-[2-[4-(4-aminophenoxy)-3,5-dimethylphenyl]propan-2-yl]-2,6-dimethylphenoxy]aniline Chemical compound CC1=CC(C(C)(C)C=2C=C(C)C(OC=3C=CC(N)=CC=3)=C(C)C=2)=CC(C)=C1OC1=CC=C(N)C=C1 SCPMRYRMHUNXQD-UHFFFAOYSA-N 0.000 description 1
- WWCYYWZFJAUUQO-UHFFFAOYSA-N 4-[4-[2-[4-(4-aminophenoxy)-3-butylphenyl]propan-2-yl]-2-butylphenoxy]aniline Chemical compound CCCCC1=CC(C(C)(C)C=2C=C(CCCC)C(OC=3C=CC(N)=CC=3)=CC=2)=CC=C1OC1=CC=C(N)C=C1 WWCYYWZFJAUUQO-UHFFFAOYSA-N 0.000 description 1
- -1 4-maleimidophenoxy Chemical group 0.000 description 1
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N EtOH Substances CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 description 1
- PEEHTFAAVSWFBL-UHFFFAOYSA-N Maleimide Chemical compound O=C1NC(=O)C=C1 PEEHTFAAVSWFBL-UHFFFAOYSA-N 0.000 description 1
- UEZVMMHDMIWARA-UHFFFAOYSA-N Metaphosphoric acid Chemical compound OP(=O)=O UEZVMMHDMIWARA-UHFFFAOYSA-N 0.000 description 1
- FXHOOIRPVKKKFG-UHFFFAOYSA-N N,N-Dimethylacetamide Chemical compound CN(C)C(C)=O FXHOOIRPVKKKFG-UHFFFAOYSA-N 0.000 description 1
- OAICVXFJPJFONN-UHFFFAOYSA-N Phosphorus Chemical compound [P] OAICVXFJPJFONN-UHFFFAOYSA-N 0.000 description 1
- NINIDFKCEFEMDL-UHFFFAOYSA-N Sulfur Chemical compound [S] NINIDFKCEFEMDL-UHFFFAOYSA-N 0.000 description 1
- 239000000853 adhesive Substances 0.000 description 1
- 230000001070 adhesive effect Effects 0.000 description 1
- 150000004945 aromatic hydrocarbons Chemical class 0.000 description 1
- 229910052799 carbon Inorganic materials 0.000 description 1
- 239000007795 chemical reaction product Substances 0.000 description 1
- 230000000052 comparative effect Effects 0.000 description 1
- 238000001816 cooling Methods 0.000 description 1
- 238000002425 crystallisation Methods 0.000 description 1
- 230000008025 crystallization Effects 0.000 description 1
- 230000007423 decrease Effects 0.000 description 1
- 230000008021 deposition Effects 0.000 description 1
- 238000004821 distillation Methods 0.000 description 1
- 238000005187 foaming Methods 0.000 description 1
- 150000008282 halocarbons Chemical class 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- GNOIPBMMFNIUFM-UHFFFAOYSA-N hexamethylphosphoric triamide Chemical compound CN(C)P(=O)(N(C)C)N(C)C GNOIPBMMFNIUFM-UHFFFAOYSA-N 0.000 description 1
- 239000011810 insulating material Substances 0.000 description 1
- 150000002576 ketones Chemical class 0.000 description 1
- 239000002648 laminated material Substances 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 239000002184 metal Substances 0.000 description 1
- 150000007522 mineralic acids Chemical class 0.000 description 1
- 238000005191 phase separation Methods 0.000 description 1
- 229910052698 phosphorus Inorganic materials 0.000 description 1
- 239000011574 phosphorus Substances 0.000 description 1
- 229920005575 poly(amic acid) Polymers 0.000 description 1
- 229920000768 polyamine Polymers 0.000 description 1
- 229920000137 polyphosphoric acid Polymers 0.000 description 1
- YLLIGHVCTUPGEH-UHFFFAOYSA-M potassium;ethanol;hydroxide Chemical compound [OH-].[K+].CCO YLLIGHVCTUPGEH-UHFFFAOYSA-M 0.000 description 1
- 239000002244 precipitate Substances 0.000 description 1
- 239000001294 propane Substances 0.000 description 1
- 239000003566 sealing material Substances 0.000 description 1
- 238000000926 separation method Methods 0.000 description 1
- 239000002002 slurry Substances 0.000 description 1
- 125000001424 substituent group Chemical group 0.000 description 1
- 229910052717 sulfur Inorganic materials 0.000 description 1
- 239000011593 sulfur Substances 0.000 description 1
- AKEJUJNQAAGONA-UHFFFAOYSA-N sulfur trioxide Inorganic materials O=S(=O)=O AKEJUJNQAAGONA-UHFFFAOYSA-N 0.000 description 1
- YLQBMQCUIZJEEH-UHFFFAOYSA-N tetrahydrofuran Natural products C=1C=COC=1 YLQBMQCUIZJEEH-UHFFFAOYSA-N 0.000 description 1
- 125000003944 tolyl group Chemical group 0.000 description 1
- YNJBWRMUSHSURL-UHFFFAOYSA-N trichloroacetic acid Chemical compound OC(=O)C(Cl)(Cl)Cl YNJBWRMUSHSURL-UHFFFAOYSA-N 0.000 description 1
- ITMCEJHCFYSIIV-UHFFFAOYSA-N triflic acid Chemical compound OS(=O)(=O)C(F)(F)F ITMCEJHCFYSIIV-UHFFFAOYSA-N 0.000 description 1
Landscapes
- Pyrrole Compounds (AREA)
Description
【0001】[0001]
【産業上の利用分野】本発明は、ビスマレイミドの製造
方法に関する。本発明の方法で得られるビスマレイミド
は、積層材料、封止材料、電気絶縁材料、導電性ペース
ト、接着剤及び構造材料として有用なものである。FIELD OF THE INVENTION The present invention relates to a method for producing bismaleimide. The bismaleimide obtained by the method of the present invention is useful as a laminate material, a sealing material, an electric insulating material, a conductive paste, an adhesive and a structural material.
【0002】[0002]
【従来の技術】従来、ポリマレイミドの製造方法として
は、アセトン等のケトン溶媒またはN,N−ジメチルホ
ルムアミド等の極性溶媒の存在下、無水酢酸等の脱水剤
を用い、トリエチルアミン等の塩基及び金属化合物を加
えて脱水閉環反応する方法(特公昭59−52660
号、特開昭63−66164号公報等)が知られている
が、この方法では閉環反応が十分進行せず、製造された
ポリマレイミドは未閉環のマレアミド酸がかなり存在す
る。更に、無水酢酸を脱水剤として用いる方法では、反
応により副生する酢酸を除去する煩雑な工程が必要であ
る。2. Description of the Related Art Conventionally, as a method for producing polymaleimide, a dehydrating agent such as acetic anhydride is used in the presence of a ketone solvent such as acetone or a polar solvent such as N, N-dimethylformamide, and a base and a metal such as triethylamine. A method of adding a compound and performing a dehydration ring closure reaction (Japanese Patent Publication No. 59-52660).
JP-A-63-66164), but the ring-closing reaction does not proceed sufficiently by this method, and the polymaleimide produced has a considerable amount of unringed maleamic acid. Furthermore, the method using acetic anhydride as a dehydrating agent requires a complicated step of removing acetic acid by-produced by the reaction.
【0003】一方、脱水剤を用いない方法としては、ポ
リアミンと無水マレイン酸とを芳香族系溶媒と非プロト
ン性極性溶媒との混合溶媒中で反応させてポリアミド酸
を得た後、酸触媒を用いて脱水閉環反応させて高純度の
ポリマレイミドを得る方法(特開昭60−26062
3、63−301226号公報等)が知られている。し
かし、これらの芳香族系溶媒と非プロトン性極性溶媒と
の混合溶媒中で反応させる方法で、2,2−ビス[4−
(4−マレイミドフェノキシ)フェニル]プロパンのよ
うな芳香族ジアミンからエーテルイミド型ビスマレイミ
ドを製造しようとする場合、芳香族系溶媒中で結晶析出
させると結晶内に該溶媒が内包される。On the other hand, as a method without using a dehydrating agent, polyamine and maleic anhydride are reacted in a mixed solvent of an aromatic solvent and an aprotic polar solvent to obtain a polyamic acid, and then an acid catalyst is used. A method for obtaining a highly pure polymaleimide by carrying out a dehydration ring closure reaction using the same (JP-A-60-26062).
3, 63-301226, etc.) is known. However, the method of reacting in a mixed solvent of these aromatic solvents and an aprotic polar solvent gives 2,2-bis [4-
When an etherimide type bismaleimide is produced from an aromatic diamine such as (4-maleimidophenoxy) phenyl] propane, the solvent is included in the crystal when crystallized in an aromatic solvent.
【0004】特開平1−211563号公報によれば、
エーテルイミド型ビスマレイミドを製造する方法とし
て、ベンゼン、トルエン、エチルベンゼン、クロルベン
ゼン等の芳香族系溶媒と非プロトン性極性溶媒との混合
溶媒中、低温で付加反応させた後、閉環反応を行い、未
反応のビスマレアミド酸がかなり残存する状態でビスマ
レイミドの結晶を析出させ、得られた結晶をメタノール
洗浄することにより溶媒を内包しない高純度のビスマレ
イミドを得る例が挙げられている。According to Japanese Patent Laid-Open No. 1-211563,
As a method for producing an etherimide type bismaleimide, benzene, toluene, ethylbenzene, in a mixed solvent of an aromatic solvent such as chlorobenzene and an aprotic polar solvent, after an addition reaction at a low temperature, a ring closure reaction is carried out, An example is given in which crystals of bismaleimide are precipitated in a state where unreacted bismaleamic acid remains considerably, and the obtained crystals are washed with methanol to obtain high-purity bismaleimide that does not include a solvent.
【0005】しかしながら、上記芳香族系溶媒と非プロ
トン性極性溶媒との混合溶媒中、反応条件を最適化して
マレアミド酸等がほとんど、あるいは全く存在しない反
応液からビスマレイミドを得ようとする場合、結晶内に
芳香族系溶媒が内包され、通常の乾燥方法では析出した
結晶から内包された溶媒を完全に除くことができず、こ
れをそのまま硬化反応に用いたのでは発泡してしまうと
いう問題を生じる。そのため、溶媒を内包しない高純度
品を得るには低沸点ハロゲン化炭化水素溶媒で再結晶さ
せる方法(特開平1−238568号公報参照)、ある
いは、乾燥して得られたビスマレイミドをテトラヒドロ
フランやアセトンに溶解して水で再沈させる方法(特開
平3−145462号公報)をとる必要があり、製造工
程が煩雑となっている。However, when trying to obtain a bismaleimide from a reaction solution containing little or no maleamic acid in a mixed solvent of the above aromatic solvent and aprotic polar solvent, the reaction conditions are optimized. Aromatic solvent is included in the crystal, it is not possible to completely remove the included solvent from the precipitated crystal by a normal drying method, and if this is used for the curing reaction as it is, the problem of foaming occurs. Occurs. Therefore, in order to obtain a high-purity product which does not include a solvent, a method of recrystallizing it with a low boiling point halogenated hydrocarbon solvent (see JP-A-1-238568) or a bismaleimide obtained by drying is used in tetrahydrofuran or acetone. It is necessary to use a method of dissolving in water and reprecipitating with water (JP-A-3-145462), which complicates the manufacturing process.
【0006】[0006]
【発明が解決しようとする課題】本発明は芳香族系炭化
水素と非プロトン性極性溶媒とを用いるエーテルイミド
系ビスマレイミドの製造法において、溶媒を内包しない
高純度ビスマレイミドを工業的に有利に、簡易に得る方
法を提供しようとするものである。DISCLOSURE OF THE INVENTION The present invention provides a method for producing an etherimide bismaleimide using an aromatic hydrocarbon and an aprotic polar solvent, which is industrially advantageous for producing a high purity bismaleimide containing no solvent. , Is intended to provide a simple way to get.
【0007】[0007]
【課題を解決するための手段】すなわち、本発明は、一
般式[I]That is, the present invention has the general formula [I]
【0008】[0008]
【化3】 [Chemical 3]
【0009】(式中、R1 〜R4 は、水素原子、または
炭素数1〜4のアルキル基を示し、R5 は水素原子、ま
たは、メチル基を示し、R6 は水素原子、メチル基もし
くはフェニル基を示す。)で示される芳香族ジアミンと
無水マレイン酸とを一般式[II](In the formula, R 1 to R 4 represent a hydrogen atom or an alkyl group having 1 to 4 carbon atoms, R 5 represents a hydrogen atom or a methyl group, and R 6 represents a hydrogen atom or a methyl group. Or a phenyl group) and a maleic anhydride represented by the general formula [II]
【0010】[0010]
【化4】 [Chemical 4]
【0011】(式中、X,Yはハロゲン原子、炭素数1
〜2のアルキル基を示し、nは1〜3の整数を示し、n
=1の場合、XとYはパラ位の位置関係にある)で示さ
れる置換ベンゼンより選ばれた芳香族系溶媒と非プロト
ン性極性溶媒の混合溶媒中、70〜150℃で付加反応
させてビスマレアミド酸を得た後、酸触媒の存在下、脱
水閉環反応させ副生する水を芳香族系溶媒と共沸除去
し、反応液を冷却して生成マレイミドを析出分離し、溶
媒を内包しない高純度ビスマレイミドを得ることを特徴
とする工業的に有利な一般式[III] (In the formula, X and Y are halogen atoms and have 1 carbon atom.
~ 2 alkyl group, n is an integer of 1-3, n
In the case of = 1, X and Y are in the para-positional relation), and the addition reaction is carried out at 70 to 150 ° C. in a mixed solvent of an aromatic solvent selected from substituted benzenes represented by After obtaining bismaleamic acid, dehydration ring closure reaction is carried out in the presence of an acid catalyst to azeotropically remove water by-produced with an aromatic solvent, and the reaction solution is cooled to precipitate and separate maleimide formed, and a high solvent-free solvent is included. Industrially advantageous general formula [III] characterized by obtaining pure bismaleimide
【化6】
[III](式中R 1 〜R 6 は前記と同義である。)で示される
ビ
スマレイミドの製造方法を提供するものである。[Chemical 6] [III] A method for producing a bismaleimide represented by the formula ( wherein R 1 to R 6 are as defined above) is provided.
【0012】(反応溶媒)混合溶媒に用いられる上記一
般式[II]で示される芳香族系溶媒としては、ビスマレ
イミドに内包されず、さらにビスマレイミドを完全に溶
解させることの出来る溶媒である。これらは、ベンゼン
環に置換基を2〜4個有し、2個の場合にはp−置換体
であるため、ベンゼン環の周囲の環境が混みあってお
り、立体的に内包を阻害しているものである。具体的に
は、p−キシレン、p−ジエチルベンゼン、p−クロロ
トルエン、メシチレン等が挙げられる。これらのなか
で、p−キシレンが適度な沸点及びビスマレイミドに対
する溶解性を有する点で特に好ましい。(Reaction Solvent) The aromatic solvent represented by the above general formula [II] used as the mixed solvent is a solvent which is not included in bismaleimide and is capable of completely dissolving bismaleimide. Since these have 2 to 4 substituents on the benzene ring and are p-substitutes in the case of two, the environment around the benzene ring is crowded and sterically hinders inclusion. There is something. Specific examples include p-xylene, p-diethylbenzene, p-chlorotoluene, mesitylene and the like. Among these, p-xylene is particularly preferable because it has an appropriate boiling point and solubility with respect to bismaleimide.
【0013】非プロトン性極性溶媒としては、付加反応
で生成するマレアミド酸を溶解しやすい溶媒、例えば、
N,N−ジメチルホルムアミド、N,N−ジメチルアセ
トアミド、N−メチル−2−ピロリドン、1,3−ジメ
チル−2−イミダゾリジノン、テトラメチル尿素酸等の
アミド系溶媒、ジメチルスルホキシド等のイオウ系溶
媒、ヘキサメチルホスホロアミド等のリン系溶媒等が挙
げられる。非プロトン性極性溶媒は、沸点150℃以上
で、水と共沸しにくいものが好ましく、前記の中でもア
ミド系溶媒が好ましく用いられる。全溶媒中の非プロト
ン性極性溶媒の量は、ビスマレイミドの析出、分離の点
で少ないほうが好ましく、通常、0.1〜30重量%、
好ましくは1〜20重量%である。混合溶媒は、アミン
類1重量部に対し、1〜50重量部、好ましくは2〜2
0重量部の割合で使用する。As the aprotic polar solvent, a solvent which easily dissolves maleamic acid produced in the addition reaction, for example,
N, N-dimethylformamide, N, N-dimethylacetamide, N-methyl-2-pyrrolidone, 1,3-dimethyl-2-imidazolidinone, amide solvents such as tetramethylureaic acid, and sulfur such as dimethyl sulfoxide. Examples of the solvent include phosphorus solvents such as hexamethylphosphoramide. The aprotic polar solvent preferably has a boiling point of 150 ° C. or higher and does not easily azeotrope with water, and among them, amide solvents are preferably used. The amount of the aprotic polar solvent in all the solvents is preferably small in terms of precipitation and separation of bismaleimide, and is usually 0.1 to 30% by weight,
It is preferably 1 to 20% by weight. The mixed solvent is 1 to 50 parts by weight, preferably 2 to 2 parts by weight with respect to 1 part by weight of amines.
Used in a proportion of 0 parts by weight.
【0014】(芳香族ジアミン)ビスマレイミドの製造
に用いられる前記一般式[I]で示される芳香族ジアミ
ンとしては、2,2−ビス[4−(4−アミノフェノキ
シ)フェニル]プロパン、2,2−ビス[3−メチル−
4−(4−アミノフェノキシ)フェニル]プロパン、
2,2−ビス[3−ブチル−4−(4−アミノフェノキ
シ)フェニル]プロパン、2,2−ビス[3,5−ジメ
チル−4−(4−アミノフェノキシ)フェニル]プロパ
ン、1−フェニル−1,1−ビス[4−(4−アミノフ
ェノキシ)フェニル]エタン、1−フェニル−1,1−
ビス[3,5−ジメチル−4−(4−アミノフェノキ
シ)フェニル]エタン等が挙げられる。これらのジアミ
ンの中で特に好ましいのは、2,2−ビス[4−(4−
アミノフェノキシ)フェニル]プロパンである。The aromatic diamine represented by the above general formula [I] used for the production of (aromatic diamine) bismaleimide includes 2,2-bis [4- (4-aminophenoxy) phenyl] propane, 2,2-bis [4- (4-aminophenoxy) phenyl] propane, 2-bis [3-methyl-
4- (4-aminophenoxy) phenyl] propane,
2,2-bis [3-butyl-4- (4-aminophenoxy) phenyl] propane, 2,2-bis [3,5-dimethyl-4- (4-aminophenoxy) phenyl] propane, 1-phenyl- 1,1-bis [4- (4-aminophenoxy) phenyl] ethane, 1-phenyl-1,1-
Examples thereof include bis [3,5-dimethyl-4- (4-aminophenoxy) phenyl] ethane. Among these diamines, 2,2-bis [4- (4-
Aminophenoxy) phenyl] propane.
【0015】(無水マレイン酸)芳香族ジアミンに対す
る無水マレイン酸の割合は、芳香族ジアミンの全アミノ
基1当量に対し無水マレイン酸を0.9〜5モル、好ま
しくは、1.0〜1.3モルを用いる。(Maleic anhydride) The ratio of maleic anhydride to the aromatic diamine is 0.9 to 5 mol, preferably 1.0 to 1. mol of maleic anhydride to 1 equivalent of all amino groups of the aromatic diamine. 3 mol is used.
【0016】(付加反応)芳香族ジアミンと無水マレイ
ン酸との付加反応は、前記混合溶媒中、70〜150℃
で行われ、ビスマレアミド酸を生成させる。付加反応温
度が70℃未満であると反応が十分進行しないため、ま
た、150℃を超えると重合物が多くなるため、ビスマ
レイミドの純度が低下する。具体的には、無水マレイン
酸を芳香族系溶媒、あるいは、混合溶媒に溶解し、所定
温度に加熱する。芳香族ジアミンを芳香族系溶媒、ある
いは、混合溶媒に溶解した後、前記、無水マレイン酸溶
液中に滴下する。滴下時間は、0.5〜5時間で、滴下
終了後、更に0.1〜5時間加熱して反応を継続してビ
スマレアミド酸のスラリー液を生成させ、ジアミンが無
くなった点を終点とする。付加反応生成液は、次いで、
酸触媒を添加して脱水閉環反応に供される。(Addition reaction) The addition reaction between the aromatic diamine and maleic anhydride is carried out in the mixed solvent at 70 to 150 ° C.
To produce bismaleamic acid. If the addition reaction temperature is lower than 70 ° C., the reaction does not proceed sufficiently, and if it exceeds 150 ° C., the amount of the polymer increases, and the purity of the bismaleimide decreases. Specifically, maleic anhydride is dissolved in an aromatic solvent or a mixed solvent and heated to a predetermined temperature. After the aromatic diamine is dissolved in an aromatic solvent or a mixed solvent, it is dropped into the maleic anhydride solution. The dripping time is 0.5 to 5 hours, and after the dripping is finished, the reaction is continued by further heating for 0.1 to 5 hours to produce a slurry liquid of bismaleamic acid, and the point at which the diamine is exhausted is the end point. The addition reaction product liquid is then
An acid catalyst is added and the dehydration ring closure reaction is performed.
【0017】(酸触媒)脱水閉環反応に使用される酸触
媒としては、硫酸、無水硫酸、リン酸、ポリリン酸、メ
タリン酸、縮合リン酸等の無機酸触媒、及び、p−トル
エンスルホン酸、トリクロル酢酸、トリフルオロ酢酸、
トリフルオロメタンスルホン酸等の有機酸触媒が挙げら
れ、有機酸触媒が好ましく用いられる。これらの酸触媒
の使用量は、アミン類のアミノ基1当量に対して0.0
001〜1モル、好ましくは0.001〜0.5モルの
範囲である。(Acid catalyst) As the acid catalyst used in the dehydration ring-closing reaction, inorganic acid catalysts such as sulfuric acid, sulfuric anhydride, phosphoric acid, polyphosphoric acid, metaphosphoric acid and condensed phosphoric acid, and p-toluenesulfonic acid, Trichloroacetic acid, trifluoroacetic acid,
Examples thereof include organic acid catalysts such as trifluoromethanesulfonic acid, and organic acid catalysts are preferably used. The amount of these acid catalysts used is 0.0 with respect to 1 equivalent of amino groups of amines.
001 to 1 mol, preferably 0.001 to 0.5 mol.
【0018】(脱水閉環反応)脱水閉環反応は、酸触媒
の添加後、温度80〜200℃、好ましくは、80〜1
50℃で、また、圧力760〜0.1mmHgの範囲で
生成水を反応溶媒と共沸留去しながら行われる。生成水
と共沸した溶媒は、冷却、相分離後、反応系に戻され
る。反応は、ビスマレアミド酸がなくなった点、具体的
には、不均一系から均一系に変化した点を終点とする。
脱水閉環温度が80℃未満では、脱水反応が進行しにく
く、また、200℃を超えると重合物が多く生成する。(Dehydration ring-closing reaction) The dehydration ring-closing reaction is carried out at a temperature of 80 to 200 ° C., preferably 80 to 1 after addition of the acid catalyst.
It is carried out at 50 ° C. and while azeotropically distilling off the produced water with the reaction solvent at a pressure in the range of 760 to 0.1 mmHg. The solvent azeotropically distilled with the produced water is returned to the reaction system after cooling and phase separation. The reaction is terminated at the point where the bismaleamic acid disappears, specifically, the point at which the heterogeneous system changes to a homogeneous system.
If the dehydration ring-closing temperature is lower than 80 ° C, the dehydration reaction is difficult to proceed, and if it exceeds 200 ° C, a large amount of polymer is produced.
【0019】(後処理法)上記のようにして得られた反
応液を水洗後、そのままか、あるいは、濃縮し冷却して
ビスマレイミドを析出させる。洗浄は、反応液中に含ま
れる、生成したビスマレイミド1重量部に対し、0.1
〜20重量部、好ましくは0.3〜10重量部の水を加
えて、撹拌後、静置し、油水分離して洗浄する。撹拌
は、一般に、回転数30〜300rpmで3〜30分間
撹拌することにより行われる。洗浄は、20〜95℃の
温度範囲で、1〜5回、好ましくは2回以上行う。(Post-Treatment Method) The reaction solution obtained as described above is washed with water and then left as it is, or concentrated and cooled to precipitate bismaleimide. The washing was performed with 0.1 part by weight of the produced bismaleimide contained in the reaction solution.
-20 parts by weight, preferably 0.3-10 parts by weight of water is added, and after stirring, the mixture is allowed to stand, separated from oily water, and washed. Stirring is generally performed by stirring at a rotation speed of 30 to 300 rpm for 3 to 30 minutes. Washing is performed 1 to 5 times, preferably 2 or more times, in a temperature range of 20 to 95 ° C.
【0020】晶析は、60℃以下、特に好ましくは50
℃以下で、撹拌下で行われ、最初の結晶析出後30分以
上、好ましくは1時間以上撹拌を続けるのがよい。析出
したビスマレイミドは、濾別後、乾燥させて目的物を得
る。乾燥は、50℃から融点以下の温度で1〜100時
間、好ましくは、3〜50時間の範囲で行う。このよう
な方法により得られるビスマレイミドは、液体クロマト
グラフ(示差屈折率検出器)の面積百分率で測定したオ
リゴマー及びポリマー成分5%以下、ガスクロマトグラ
フ(FID)の絶対検量線法で測定した残存溶媒量1重
量%以下、N/10KOHエタノール溶液で滴定した酸
価が2.5(mg・KOH/g)以下の高純度品であ
る。Crystallization is performed at 60 ° C. or lower, particularly preferably 50.
It is carried out at a temperature of not more than 0 ° C. under agitation, and the agitation is continued for 30 minutes or more, preferably 1 hour or more after the first crystal precipitation. The precipitated bismaleimide is filtered off and dried to obtain the desired product. The drying is performed at a temperature of 50 ° C. to the melting point or lower for 1 to 100 hours, preferably 3 to 50 hours. The bismaleimide obtained by such a method is an oligomer and polymer component of 5% or less measured by the area percentage of a liquid chromatograph (differential refractive index detector), and a residual solvent measured by an absolute calibration curve method of a gas chromatograph (FID). It is a highly pure product with an amount of 1% by weight or less and an acid value titrated with an N / 10 KOH ethanol solution of 2.5 (mg · KOH / g) or less.
【0021】[0021]
【実施例】以下、実施例により本発明を詳細に説明す
る。
実施例1
冷却器、温度計、撹拌器および水分離器を備えた500
mLの四口フラスコ内に、無水マレイン酸23.5gお
よびp−キシレン140gを仕込み、内温を100℃に
調整した。次に、2,2−ビス[4−(4−アミノフェ
ノキシ)フェニル]プロパン41.0gをp−キシレン
90gおよびN−メチル−2−ピロリドン8.2gに溶
解した溶液を内温100℃に調整しながら1時間かけて
滴下し、終了後、さらに同温度で1時間撹拌し、付加反
応させた。The present invention will be described in detail below with reference to examples. Example 1 500 with cooler, thermometer, stirrer and water separator
A 3.5-mL four-necked flask was charged with 23.5 g of maleic anhydride and 140 g of p-xylene, and the internal temperature was adjusted to 100 ° C. Next, a solution of 41.0 g of 2,2-bis [4- (4-aminophenoxy) phenyl] propane dissolved in 90 g of p-xylene and 8.2 g of N-methyl-2-pyrrolidone was adjusted to an internal temperature of 100 ° C. While the solution was added dropwise over 1 hour, after completion, the mixture was further stirred at the same temperature for 1 hour to carry out an addition reaction.
【0022】続いて、パラトルエンスルホン酸1.9g
を添加後昇温し、常圧下、p−キシレンの還流下(13
8℃)に2.4時間保ち閉環反応を遂行した。この間に
生成した水はp−キシレンとともに系外へ留去せしめ
た。反応終了後、純水100g、温度90〜95℃で4
回洗浄した。水洗後、反応液を温度70〜80℃、減圧
下(200〜10mmHg)で、p−キシレン135g
(仕込p−キシレンに対する留去率58.7%、残存p
−キシレン95g)を留去し、撹拌しながら冷却してビ
スマレイミドを析出させ(析出温度52℃)、その後2
時間撹拌した。析出物を濾別し、減圧下50℃で24時
間、60℃で24時間乾燥して淡黄色のビスマレイミド
の粉末51.9gを得た(ビスマレイミドの理論量に対
する収率91.1%)。Subsequently, 1.9 g of paratoluenesulfonic acid
Was added and the temperature was raised, and under normal pressure, under reflux of p-xylene (13
The ring-closing reaction was carried out by keeping the temperature at 8 ° C. for 2.4 hours. The water generated during this time was distilled out of the system together with p-xylene. After completion of the reaction, 100 g of pure water and a temperature of 90 to 95 ° C. for 4 hours
Washed twice. After washing with water, the reaction solution was heated to 70 to 80 ° C. under reduced pressure (200 to 10 mmHg) to give 135 g of p-xylene.
(Distillation rate to charged p-xylene 58.7%, residual p
-Xylene (95 g) was distilled off, and the mixture was cooled with stirring to precipitate bismaleimide (deposition temperature 52 ° C).
Stir for hours. The precipitate was filtered off and dried under reduced pressure at 50 ° C. for 24 hours and at 60 ° C. for 24 hours to obtain 51.9 g of a pale yellow bismaleimide powder (yield 91.1% based on the theoretical amount of bismaleimide). .
【0023】このビスマレイミドのキャピラリー法によ
る融点は、140〜144℃、液体クロマトグラフ(示
差屈折率検出器)の面積百分率で測定した純度は、9
8.8%、ガスクロマトグラフ(FID)の絶対検量線
法で測定した残存溶媒量は、0.8重量%、N/10K
OHエタノール溶液で滴定した酸価は、2.1(mg・
KOH/g)であった。The melting point of this bismaleimide by the capillary method is 140 to 144 ° C., and the purity measured by the area percentage of a liquid chromatograph (differential refractive index detector) is 9
8.8%, residual solvent amount measured by gas chromatograph (FID) absolute calibration curve method is 0.8% by weight, N / 10K
The acid value titrated with OH-ethanol solution is 2.1 (mg
KOH / g).
【0024】実施例2
芳香族系溶媒をメシチレンに代え、反応を減圧下、メシ
チレンの還流下(温度110℃、減圧度140mmH
g)で行い、水洗後の濃縮を行わなかった以外は、実施
例1と同様の操作を行い淡黄色のビスマレイミドの粉末
47.8gを得た(収率83.9%)。このビスマレイ
ミドは、融点149〜154℃、純度97.4%、残存
溶媒量0.5重量%および酸価2.0(mg・KOH/
g)であった。Example 2 The aromatic solvent was replaced with mesitylene, and the reaction was carried out under reduced pressure and under reflux of mesitylene (temperature 110 ° C., reduced pressure 140 mmH).
g), and the same operation as in Example 1 was performed except that the concentration after washing with water was not carried out to obtain 47.8 g of a pale yellow bismaleimide powder (yield 83.9%). This bismaleimide has a melting point of 149 to 154 ° C., a purity of 97.4%, a residual solvent amount of 0.5% by weight, and an acid value of 2.0 (mg · KOH /
g).
【0025】実施例3
芳香族系溶媒をp−クロロトルエンに代え、反応を減圧
下、p−クロロトルエンの還流下(温度110℃、減圧
度160mmHg)で行い、水洗後の濃縮を行わなかっ
た以外は、実施例1と同様の操作を行い淡黄色のビスマ
レイミドの粉末46.3gを得た(収率81.2%)。
このビスマレイミドは、融点126〜148℃、純度9
8.4%、残存溶媒量0.6重量%および酸価1.0
(mg・KOH/g)であった。Example 3 The aromatic solvent was changed to p-chlorotoluene, the reaction was carried out under reduced pressure and under reflux of p-chlorotoluene (temperature 110 ° C., reduced pressure 160 mmHg), and no concentration was carried out after washing with water. Other than that, the same operation as in Example 1 was carried out to obtain 46.3 g of a pale yellow bismaleimide powder (yield 81.2%).
This bismaleimide has a melting point of 126 to 148 ° C. and a purity of 9
8.4%, residual solvent amount 0.6% by weight and acid value 1.0
(Mg · KOH / g).
【0026】比較例1
実施例1において、芳香族系溶媒をトルエンに変え、水
洗後の濃縮を行わなかった以外は、実施例1と同様にし
て淡黄色のビスマレイミド55.4gを得た(見かけの
収率97.2%)。このビスマレイミドは、トルエン1
3.1重量%を含み(トルエンを除外した純度は、9
8.2%)、融点140〜145℃、酸価2.48(m
g・KOH/g)であった。Comparative Example 1 A light yellow bismaleimide (55.4 g) was obtained in the same manner as in Example 1 except that the aromatic solvent was changed to toluene and concentration after washing with water was not carried out. Apparent yield 97.2%). This bismaleimide is toluene 1
Contains 3.1% by weight (purity excluding toluene is 9
8.2%), melting point 140-145 ° C, acid value 2.48 (m
g · KOH / g).
【0027】[0027]
【発明の効果】本発明によれば芳香族ジアミンと無水マ
レイン酸とを選ばれた芳香族系溶媒と非プロトン性極性
溶媒の混合溶媒中、反応させると溶媒を内包しない高純
度ビスマレイミドを得ることができる。According to the present invention, when an aromatic diamine and maleic anhydride are reacted in a mixed solvent of an aromatic solvent selected and an aprotic polar solvent, a high-purity bismaleimide containing no solvent is obtained. be able to.
───────────────────────────────────────────────────── フロントページの続き (56)参考文献 特開 平5−230017(JP,A) (58)調査した分野(Int.Cl.7,DB名) C07D 207/452 CA(STN) REGISTRY(STN)─────────────────────────────────────────────────── ─── Continuation of the front page (56) Reference JP-A-5-230017 (JP, A) (58) Fields investigated (Int.Cl. 7 , DB name) C07D 207/452 CA (STN) REGISTRY (STN )
Claims (2)
アルキル基を示し、 R5は水素原子、または、メチル
基を示し、R6は水素原子、メチル基もしくはフェニル
基を示す。)で示される芳香族ジアミンと無水マレイン
酸とを一般式[II] 【化2】 (式中、X,Yはハロゲン原子、炭素数1〜2のアルキ
ル基を示し、nは1〜3の整数を示し、n=1の場合、
XとYはパラ位の位置関係にある)で示される置換ベン
ゼンより選ばれた芳香族系溶媒と非プロトン性極性溶媒
の混合溶媒中、70〜150℃で付加反応させてビスマ
レアミド酸を得た後、酸触媒の存在下、脱水閉環反応さ
せ副生する水を共沸除去し、反応液を冷却して生成ビス
マレイミドを析出分離し、高純度ビスマレイミドを得る
ことを特徴とする一般式[III] 【化3】 (式中R 1 〜R 6 は前記と同義である。)で示されるビ
スマレイミドの製造方法。1. A compound represented by the general formula [I]: (In the formula, R 1 to R 4 represent a hydrogen atom or an alkyl group having 1 to 4 carbon atoms, R 5 represents a hydrogen atom or a methyl group, and R 6 represents a hydrogen atom, a methyl group or a phenyl group. Of the aromatic diamine and maleic anhydride represented by the general formula [II] (In the formula, X and Y represent a halogen atom and an alkyl group having 1 to 2 carbon atoms, n represents an integer of 1 to 3, and in the case of n = 1,
X and Y are in the para-positional relationship) and a bismaleamic acid is obtained by addition reaction at 70 to 150 ° C. in a mixed solvent of an aromatic solvent selected from substituted benzenes represented by a substituted benzene and an aprotic polar solvent. After that, in the presence of an acid catalyst, dehydration ring-closing reaction is carried out to azeotropically remove by-produced water, and the reaction solution is cooled to precipitate and separate the produced bismaleimide, thereby obtaining a high-purity bismaleimide . III] [Chemical Formula 3] (In the formula, R 1 to R 6 have the same meanings as described above.) A method for producing a bismaleimide.
2,2−ビス[4−(4−アミノフェノキシ)フェニ
ル]プロパンである請求項1に記載の方法。2. The method according to claim 1, wherein the aromatic diamine represented by the formula [I] is 2,2-bis [4- (4-aminophenoxy) phenyl] propane.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP26200293A JP3433482B2 (en) | 1993-10-20 | 1993-10-20 | Method for producing bismaleimide |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP26200293A JP3433482B2 (en) | 1993-10-20 | 1993-10-20 | Method for producing bismaleimide |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPH07118230A JPH07118230A (en) | 1995-05-09 |
| JP3433482B2 true JP3433482B2 (en) | 2003-08-04 |
Family
ID=17369652
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP26200293A Expired - Fee Related JP3433482B2 (en) | 1993-10-20 | 1993-10-20 | Method for producing bismaleimide |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JP3433482B2 (en) |
Families Citing this family (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| ATE541879T1 (en) | 2008-06-09 | 2012-02-15 | Mitsubishi Gas Chemical Co | BISMALEAMIC ACID, BISMALEIMIDE AND HARDENED PRODUCT THEREOF |
| KR20200128008A (en) | 2018-02-28 | 2020-11-11 | 미쯔비시 가스 케미칼 컴파니, 인코포레이티드 | Compound, resin, composition and film-forming material for lithography using the same |
| JP6555792B1 (en) | 2018-05-10 | 2019-08-07 | ユニチカ株式会社 | Method for producing maleimide |
| CN114674937B (en) * | 2020-12-24 | 2024-07-05 | 沈阳药科大学 | Method for determining long-chain fatty amine in maleic acid long-chain fatty amide |
-
1993
- 1993-10-20 JP JP26200293A patent/JP3433482B2/en not_active Expired - Fee Related
Also Published As
| Publication number | Publication date |
|---|---|
| JPH07118230A (en) | 1995-05-09 |
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