JPH0525186A - Production of polymerizable monomer - Google Patents
Production of polymerizable monomerInfo
- Publication number
- JPH0525186A JPH0525186A JP3204892A JP20489291A JPH0525186A JP H0525186 A JPH0525186 A JP H0525186A JP 3204892 A JP3204892 A JP 3204892A JP 20489291 A JP20489291 A JP 20489291A JP H0525186 A JPH0525186 A JP H0525186A
- Authority
- JP
- Japan
- Prior art keywords
- polymerizable monomer
- reaction
- added
- maleic acid
- mol
- 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.)
- Pending
Links
- 239000000178 monomer Substances 0.000 title claims abstract description 41
- 238000004519 manufacturing process Methods 0.000 title claims abstract description 11
- OFOBLEOULBTSOW-UHFFFAOYSA-N Propanedioic acid Natural products OC(=O)CC(O)=O OFOBLEOULBTSOW-UHFFFAOYSA-N 0.000 claims abstract description 23
- VZCYOOQTPOCHFL-UPHRSURJSA-N maleic acid Chemical compound OC(=O)\C=C/C(O)=O VZCYOOQTPOCHFL-UPHRSURJSA-N 0.000 claims abstract description 23
- 239000011976 maleic acid Substances 0.000 claims abstract description 23
- VZCYOOQTPOCHFL-UHFFFAOYSA-N trans-butenedioic acid Natural products OC(=O)C=CC(O)=O VZCYOOQTPOCHFL-UHFFFAOYSA-N 0.000 claims abstract description 23
- FPYJFEHAWHCUMM-UHFFFAOYSA-N maleic anhydride Chemical compound O=C1OC(=O)C=C1 FPYJFEHAWHCUMM-UHFFFAOYSA-N 0.000 claims abstract description 18
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 claims abstract description 13
- 239000002841 Lewis acid Substances 0.000 claims abstract description 7
- 239000002879 Lewis base Substances 0.000 claims abstract description 7
- 150000007517 lewis acids Chemical class 0.000 claims abstract description 7
- 150000007527 lewis bases Chemical class 0.000 claims abstract description 7
- -1 silyl ester compound Chemical class 0.000 claims description 21
- 238000006297 dehydration reaction Methods 0.000 claims description 5
- 238000005886 esterification reaction Methods 0.000 claims description 5
- 238000006243 chemical reaction Methods 0.000 abstract description 36
- 239000000126 substance Substances 0.000 abstract description 3
- 125000001181 organosilyl group Chemical group [SiH3]* 0.000 abstract 2
- YXFVVABEGXRONW-UHFFFAOYSA-N Toluene Chemical compound CC1=CC=CC=C1 YXFVVABEGXRONW-UHFFFAOYSA-N 0.000 description 30
- 239000000243 solution Substances 0.000 description 23
- ZMANZCXQSJIPKH-UHFFFAOYSA-N Triethylamine Chemical compound CCN(CC)CC ZMANZCXQSJIPKH-UHFFFAOYSA-N 0.000 description 21
- 238000000655 nuclear magnetic resonance spectrum Methods 0.000 description 18
- 238000003756 stirring Methods 0.000 description 13
- 125000003808 silyl group Chemical group [H][Si]([H])([H])[*] 0.000 description 12
- 238000010521 absorption reaction Methods 0.000 description 10
- UHOVQNZJYSORNB-UHFFFAOYSA-N Benzene Chemical compound C1=CC=CC=C1 UHOVQNZJYSORNB-UHFFFAOYSA-N 0.000 description 9
- OKKJLVBELUTLKV-UHFFFAOYSA-N Methanol Chemical compound OC OKKJLVBELUTLKV-UHFFFAOYSA-N 0.000 description 9
- 239000007795 chemical reaction product Substances 0.000 description 9
- 238000001816 cooling Methods 0.000 description 8
- 238000010438 heat treatment Methods 0.000 description 8
- 239000000203 mixture Substances 0.000 description 8
- 238000002329 infrared spectrum Methods 0.000 description 7
- 239000000047 product Substances 0.000 description 7
- 239000002904 solvent Substances 0.000 description 7
- 238000005292 vacuum distillation Methods 0.000 description 7
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 7
- WYURNTSHIVDZCO-UHFFFAOYSA-N Tetrahydrofuran Chemical compound C1CCOC1 WYURNTSHIVDZCO-UHFFFAOYSA-N 0.000 description 6
- RAXXELZNTBOGNW-UHFFFAOYSA-N imidazole Natural products C1=CNC=N1 RAXXELZNTBOGNW-UHFFFAOYSA-N 0.000 description 6
- 238000000034 method Methods 0.000 description 5
- CSNNHWWHGAXBCP-UHFFFAOYSA-L Magnesium sulfate Chemical compound [Mg+2].[O-][S+2]([O-])([O-])[O-] CSNNHWWHGAXBCP-UHFFFAOYSA-L 0.000 description 4
- 239000006227 byproduct Substances 0.000 description 4
- DKPFZGUDAPQIHT-UHFFFAOYSA-N Butyl acetate Natural products CCCCOC(C)=O DKPFZGUDAPQIHT-UHFFFAOYSA-N 0.000 description 3
- RTZKZFJDLAIYFH-UHFFFAOYSA-N Diethyl ether Chemical compound CCOCC RTZKZFJDLAIYFH-UHFFFAOYSA-N 0.000 description 3
- XEKOWRVHYACXOJ-UHFFFAOYSA-N Ethyl acetate Chemical compound CCOC(C)=O XEKOWRVHYACXOJ-UHFFFAOYSA-N 0.000 description 3
- VEXZGXHMUGYJMC-UHFFFAOYSA-N Hydrochloric acid Chemical compound Cl VEXZGXHMUGYJMC-UHFFFAOYSA-N 0.000 description 3
- ISKQADXMHQSTHK-UHFFFAOYSA-N [4-(aminomethyl)phenyl]methanamine Chemical compound NCC1=CC=C(CN)C=C1 ISKQADXMHQSTHK-UHFFFAOYSA-N 0.000 description 3
- 239000002585 base Substances 0.000 description 3
- 125000004432 carbon atom Chemical group C* 0.000 description 3
- 125000003178 carboxy group Chemical group [H]OC(*)=O 0.000 description 3
- 239000013078 crystal Substances 0.000 description 3
- FUZZWVXGSFPDMH-UHFFFAOYSA-N hexanoic acid Chemical compound CCCCCC(O)=O FUZZWVXGSFPDMH-UHFFFAOYSA-N 0.000 description 3
- MQNNNLJCDJBERF-UHFFFAOYSA-N hydroxy-tri(propan-2-yl)silane Chemical compound CC(C)[Si](O)(C(C)C)C(C)C MQNNNLJCDJBERF-UHFFFAOYSA-N 0.000 description 3
- 239000000543 intermediate Substances 0.000 description 3
- VLKZOEOYAKHREP-UHFFFAOYSA-N n-Hexane Chemical compound CCCCCC VLKZOEOYAKHREP-UHFFFAOYSA-N 0.000 description 3
- 239000007787 solid Substances 0.000 description 3
- YLQBMQCUIZJEEH-UHFFFAOYSA-N tetrahydrofuran Natural products C=1C=COC=1 YLQBMQCUIZJEEH-UHFFFAOYSA-N 0.000 description 3
- ILWRPSCZWQJDMK-UHFFFAOYSA-N triethylazanium;chloride Chemical compound Cl.CCN(CC)CC ILWRPSCZWQJDMK-UHFFFAOYSA-N 0.000 description 3
- VZSRBBMJRBPUNF-UHFFFAOYSA-N 2-(2,3-dihydro-1H-inden-2-ylamino)-N-[3-oxo-3-(2,4,6,7-tetrahydrotriazolo[4,5-c]pyridin-5-yl)propyl]pyrimidine-5-carboxamide Chemical compound C1C(CC2=CC=CC=C12)NC1=NC=C(C=N1)C(=O)NCCC(N1CC2=C(CC1)NN=N2)=O VZSRBBMJRBPUNF-UHFFFAOYSA-N 0.000 description 2
- AMQJEAYHLZJPGS-UHFFFAOYSA-N N-Pentanol Chemical compound CCCCCO AMQJEAYHLZJPGS-UHFFFAOYSA-N 0.000 description 2
- UKLDJPRMSDWDSL-UHFFFAOYSA-L [dibutyl(dodecanoyloxy)stannyl] dodecanoate Chemical compound CCCCCCCCCCCC(=O)O[Sn](CCCC)(CCCC)OC(=O)CCCCCCCCCCC UKLDJPRMSDWDSL-UHFFFAOYSA-L 0.000 description 2
- 238000000862 absorption spectrum Methods 0.000 description 2
- 125000000217 alkyl group Chemical group 0.000 description 2
- 125000003118 aryl group Chemical group 0.000 description 2
- 230000000052 comparative effect Effects 0.000 description 2
- 238000007796 conventional method Methods 0.000 description 2
- 239000012024 dehydrating agents Substances 0.000 description 2
- 238000007033 dehydrochlorination reaction Methods 0.000 description 2
- 238000010586 diagram Methods 0.000 description 2
- 239000012975 dibutyltin dilaurate Substances 0.000 description 2
- 239000000706 filtrate Substances 0.000 description 2
- 238000004817 gas chromatography Methods 0.000 description 2
- PHTQWCKDNZKARW-UHFFFAOYSA-N isoamylol Chemical compound CC(C)CCO PHTQWCKDNZKARW-UHFFFAOYSA-N 0.000 description 2
- 238000005259 measurement Methods 0.000 description 2
- 125000000962 organic group Chemical group 0.000 description 2
- 125000003107 substituted aryl group Chemical group 0.000 description 2
- XJDNKRIXUMDJCW-UHFFFAOYSA-J titanium tetrachloride Chemical compound Cl[Ti](Cl)(Cl)Cl XJDNKRIXUMDJCW-UHFFFAOYSA-J 0.000 description 2
- OHVLMTFVQDZYHP-UHFFFAOYSA-N 1-(2,4,6,7-tetrahydrotriazolo[4,5-c]pyridin-5-yl)-2-[4-[2-[[3-(trifluoromethoxy)phenyl]methylamino]pyrimidin-5-yl]piperazin-1-yl]ethanone Chemical compound N1N=NC=2CN(CCC=21)C(CN1CCN(CC1)C=1C=NC(=NC=1)NCC1=CC(=CC=C1)OC(F)(F)F)=O OHVLMTFVQDZYHP-UHFFFAOYSA-N 0.000 description 1
- 238000005160 1H NMR spectroscopy Methods 0.000 description 1
- LDXJRKWFNNFDSA-UHFFFAOYSA-N 2-(2,4,6,7-tetrahydrotriazolo[4,5-c]pyridin-5-yl)-1-[4-[2-[[3-(trifluoromethoxy)phenyl]methylamino]pyrimidin-5-yl]piperazin-1-yl]ethanone Chemical compound C1CN(CC2=NNN=C21)CC(=O)N3CCN(CC3)C4=CN=C(N=C4)NCC5=CC(=CC=C5)OC(F)(F)F LDXJRKWFNNFDSA-UHFFFAOYSA-N 0.000 description 1
- YJLUBHOZZTYQIP-UHFFFAOYSA-N 2-[5-[2-(2,3-dihydro-1H-inden-2-ylamino)pyrimidin-5-yl]-1,3,4-oxadiazol-2-yl]-1-(2,4,6,7-tetrahydrotriazolo[4,5-c]pyridin-5-yl)ethanone Chemical compound C1C(CC2=CC=CC=C12)NC1=NC=C(C=N1)C1=NN=C(O1)CC(=O)N1CC2=C(CC1)NN=N2 YJLUBHOZZTYQIP-UHFFFAOYSA-N 0.000 description 1
- YLZOPXRUQYQQID-UHFFFAOYSA-N 3-(2,4,6,7-tetrahydrotriazolo[4,5-c]pyridin-5-yl)-1-[4-[2-[[3-(trifluoromethoxy)phenyl]methylamino]pyrimidin-5-yl]piperazin-1-yl]propan-1-one Chemical compound N1N=NC=2CN(CCC=21)CCC(=O)N1CCN(CC1)C=1C=NC(=NC=1)NCC1=CC(=CC=C1)OC(F)(F)F YLZOPXRUQYQQID-UHFFFAOYSA-N 0.000 description 1
- UXVMQQNJUSDDNG-UHFFFAOYSA-L Calcium chloride Chemical compound [Cl-].[Cl-].[Ca+2] UXVMQQNJUSDDNG-UHFFFAOYSA-L 0.000 description 1
- QOSSAOTZNIDXMA-UHFFFAOYSA-N Dicylcohexylcarbodiimide Chemical compound C1CCCCC1N=C=NC1CCCCC1 QOSSAOTZNIDXMA-UHFFFAOYSA-N 0.000 description 1
- CTQNGGLPUBDAKN-UHFFFAOYSA-N O-Xylene Chemical compound CC1=CC=CC=C1C CTQNGGLPUBDAKN-UHFFFAOYSA-N 0.000 description 1
- BLRPTPMANUNPDV-UHFFFAOYSA-N Silane Chemical compound [SiH4] BLRPTPMANUNPDV-UHFFFAOYSA-N 0.000 description 1
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 description 1
- PMZURENOXWZQFD-UHFFFAOYSA-L Sodium Sulfate Chemical compound [Na+].[Na+].[O-]S([O-])(=O)=O PMZURENOXWZQFD-UHFFFAOYSA-L 0.000 description 1
- NBJODVYWAQLZOC-UHFFFAOYSA-L [dibutyl(octanoyloxy)stannyl] octanoate Chemical compound CCCCCCCC(=O)O[Sn](CCCC)(CCCC)OC(=O)CCCCCCC NBJODVYWAQLZOC-UHFFFAOYSA-L 0.000 description 1
- 125000002252 acyl group Chemical group 0.000 description 1
- 150000001338 aliphatic hydrocarbons Chemical class 0.000 description 1
- 125000003277 amino group Chemical group 0.000 description 1
- 230000003373 anti-fouling effect Effects 0.000 description 1
- 150000004945 aromatic hydrocarbons Chemical class 0.000 description 1
- FPCJKVGGYOAWIZ-UHFFFAOYSA-N butan-1-ol;titanium Chemical compound [Ti].CCCCO.CCCCO.CCCCO.CCCCO FPCJKVGGYOAWIZ-UHFFFAOYSA-N 0.000 description 1
- 150000001718 carbodiimides Chemical class 0.000 description 1
- 239000003054 catalyst Substances 0.000 description 1
- 238000000576 coating method Methods 0.000 description 1
- 125000006165 cyclic alkyl group Chemical group 0.000 description 1
- 125000000113 cyclohexyl group Chemical group [H]C1([H])C([H])([H])C([H])([H])C([H])(*)C([H])([H])C1([H])[H] 0.000 description 1
- MKNXBRLZBFVUPV-UHFFFAOYSA-L cyclopenta-1,3-diene;dichlorotitanium Chemical compound Cl[Ti]Cl.C=1C=C[CH-]C=1.C=1C=C[CH-]C=1 MKNXBRLZBFVUPV-UHFFFAOYSA-L 0.000 description 1
- 125000001559 cyclopropyl group Chemical group [H]C1([H])C([H])([H])C1([H])* 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 239000003759 ester based solvent Substances 0.000 description 1
- 230000032050 esterification Effects 0.000 description 1
- 239000004210 ether based solvent Substances 0.000 description 1
- 125000001495 ethyl group Chemical group [H]C([H])([H])C([H])([H])* 0.000 description 1
- 238000001914 filtration Methods 0.000 description 1
- 239000011521 glass Substances 0.000 description 1
- 229910052736 halogen Inorganic materials 0.000 description 1
- 150000002367 halogens Chemical class 0.000 description 1
- 150000003840 hydrochlorides Chemical class 0.000 description 1
- 238000002347 injection Methods 0.000 description 1
- 239000007924 injection Substances 0.000 description 1
- 238000007689 inspection Methods 0.000 description 1
- 125000000959 isobutyl group Chemical group [H]C([H])([H])C([H])(C([H])([H])[H])C([H])([H])* 0.000 description 1
- 125000001449 isopropyl group Chemical group [H]C([H])([H])C([H])(*)C([H])([H])[H] 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 230000014759 maintenance of location Effects 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 125000002496 methyl group Chemical group [H]C([H])([H])* 0.000 description 1
- 239000002808 molecular sieve Substances 0.000 description 1
- 238000003541 multi-stage reaction Methods 0.000 description 1
- 125000004108 n-butyl group Chemical group [H]C([H])([H])C([H])([H])C([H])([H])C([H])([H])* 0.000 description 1
- 125000004123 n-propyl group Chemical group [H]C([H])([H])C([H])([H])C([H])([H])* 0.000 description 1
- 125000000449 nitro group Chemical group [O-][N+](*)=O 0.000 description 1
- 239000004033 plastic Substances 0.000 description 1
- 229920003023 plastic Polymers 0.000 description 1
- 229920000642 polymer Polymers 0.000 description 1
- 238000006116 polymerization reaction Methods 0.000 description 1
- 238000001556 precipitation Methods 0.000 description 1
- 238000010526 radical polymerization reaction Methods 0.000 description 1
- 150000003839 salts Chemical class 0.000 description 1
- 125000002914 sec-butyl group Chemical group [H]C([H])([H])C([H])([H])C([H])(*)C([H])([H])[H] 0.000 description 1
- 229910000077 silane Inorganic materials 0.000 description 1
- 239000000741 silica gel Substances 0.000 description 1
- 229910002027 silica gel Inorganic materials 0.000 description 1
- URGAHOPLAPQHLN-UHFFFAOYSA-N sodium aluminosilicate Chemical compound [Na+].[Al+3].[O-][Si]([O-])=O.[O-][Si]([O-])=O URGAHOPLAPQHLN-UHFFFAOYSA-N 0.000 description 1
- 238000000967 suction filtration Methods 0.000 description 1
- 125000000999 tert-butyl group Chemical group [H]C([H])([H])C(*)(C([H])([H])[H])C([H])([H])[H] 0.000 description 1
- FGWRMMTYIZKYMA-UHFFFAOYSA-N tert-butyl-hydroxy-dimethylsilane Chemical compound CC(C)(C)[Si](C)(C)O FGWRMMTYIZKYMA-UHFFFAOYSA-N 0.000 description 1
- UNAYGNMKNYRIHL-UHFFFAOYSA-N tert-butyl-hydroxy-diphenylsilane Chemical compound C=1C=CC=CC=1[Si](O)(C(C)(C)C)C1=CC=CC=C1 UNAYGNMKNYRIHL-UHFFFAOYSA-N 0.000 description 1
- BCNZYOJHNLTNEZ-UHFFFAOYSA-N tert-butyldimethylsilyl chloride Chemical compound CC(C)(C)[Si](C)(C)Cl BCNZYOJHNLTNEZ-UHFFFAOYSA-N 0.000 description 1
- 150000003606 tin compounds Chemical class 0.000 description 1
- 150000003609 titanium compounds Chemical class 0.000 description 1
- 238000005406 washing Methods 0.000 description 1
- 239000008096 xylene Substances 0.000 description 1
Classifications
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P20/00—Technologies relating to chemical industry
- Y02P20/50—Improvements relating to the production of bulk chemicals
- Y02P20/52—Improvements relating to the production of bulk chemicals using catalysts, e.g. selective catalysts
Landscapes
- Low-Molecular Organic Synthesis Reactions Using Catalysts (AREA)
- Addition Polymer Or Copolymer, Post-Treatments, Or Chemical Modifications (AREA)
Abstract
Description
【0001】[0001]
【産業上の利用分野】本発明は、マレイン酸モノエステ
ルのシリルエステル化物からなる重合性モノマ―を製造
する方法に関する。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method for producing a polymerizable monomer composed of a silyl ester of maleic acid monoester.
【0002】[0002]
【従来の技術】従来より、マレイン酸モノエステルのカ
ルボキシル基をシリルエステル化して、分子内にシリル
基を導入した重合性モノマ―は、たとえば、特開昭63
−215780号公報に示されているように、一般的に
は、マレイン酸モノエステルとトリオルガノクロロシラ
ンとを、トリエチルアミンなどの塩基の存在下で、脱塩
化水素する方法で製造されている。2. Description of the Related Art Conventionally, a polymerizable monomer obtained by silyl esterifying a carboxyl group of maleic acid monoester to introduce a silyl group into the molecule is disclosed in, for example, JP-A-63 / 1988.
As disclosed in JP-A-215780, it is generally produced by a method of dehydrochlorinating maleic acid monoester and triorganochlorosilane in the presence of a base such as triethylamine.
【0003】[0003]
【発明が解決しようとする課題】しかるに、トリエチル
アミンなどの塩基を用いた脱塩化水素による方法では、
一般に、まずマレイン酸モノエステルのアミン塩を中間
体として形成したのちに、トリオルガノクロロシランと
反応させることになるため、反応工程が多段階となり、
またトリエチルアミン塩酸塩などの結晶性の塩酸塩が副
生するため、この塩酸塩を取り除く工程が必要となるな
ど、製造工程上の不利を免れなかつた。また、目的とす
るマレイン酸モノエステルのシリルエステル化物の収率
および純度が低いという問題もあつた。However, in the method using dehydrochlorination using a base such as triethylamine,
Generally, first, an amine salt of maleic acid monoester is formed as an intermediate, and then it is reacted with triorganochlorosilane, so that the reaction process has multiple stages,
Further, since a crystalline hydrochloride such as triethylamine hydrochloride is produced as a by-product, a step of removing this hydrochloride is required, which is disadvantageous in the manufacturing process. There is also a problem that the yield and purity of the target silyl esterified product of maleic acid monoester are low.
【0004】本発明は、上記従来の問題点に鑑み、マレ
イン酸モノエステルのシリルエステル化物からなる重合
性モノマ―を製造する方法において、反応工程を簡素化
し、製造工程上の不利を回避するとともに、上記重合性
モノマ―の収率および純度を向上させることを目的とし
ている。In view of the above-mentioned conventional problems, the present invention simplifies the reaction step and avoids the disadvantages in the production process in the method for producing a polymerizable monomer comprising a silyl esterified product of maleic acid monoester. The purpose of the present invention is to improve the yield and purity of the polymerizable monomer.
【0005】[0005]
【課題を解決するための手段】本発明者らは、上記の目
的を達成するために、鋭意検討した結果、マレイン酸モ
ノエステルのシリルエステル化が、特定の触媒を用いる
ことによつて、カルボキシル基とトリオルガノシラノ―
ルとの脱水反応により達成でき、これによると、反応工
程の簡素化とともに、目的とするシリルエステル化物の
収率および純度を大きく向上できることを知り、本発明
を完成するに至つた。Means for Solving the Problems The inventors of the present invention have conducted extensive studies in order to achieve the above-mentioned object. As a result, the silyl esterification of maleic acid monoester was confirmed to be carried out by using a specific catalyst. Radicals and triorganosilano
The present invention has been completed based on the finding that this can be achieved by a dehydration reaction with silane, which can greatly improve the yield and purity of the target silyl esterified product as well as simplifying the reaction process.
【0006】すなわち、本発明は、無水マレイン酸に、
一価アルコ―ル、トリオルガノシラノ―ルおよびルイス
酸またはルイス塩基を加え、脱水反応を伴うエステル化
反応を行わせて、マレイン酸モノエステルのシリルエス
テル化物からなる重合性モノマ―を製造することを特徴
とする重合性モノマ―の製造法に係るものである。That is, the present invention relates to maleic anhydride.
A monovalent alcohol, triorganosilanol and Lewis acid or Lewis base are added to carry out an esterification reaction accompanied by a dehydration reaction to produce a polymerizable monomer composed of a silyl esterified product of maleic acid monoester. The present invention relates to a method for producing a polymerizable monomer characterized by:
【0007】[0007]
【発明の構成・作用】本発明に用いる一価アルコ―ルと
しては、炭素数が通常1〜12個である、直鎖状、分岐
状または環状のアルキルアルコ―ルが挙げられ、その1
種を単独でまたは2種以上を混合して使用することがで
きる。The monovalent alcohol used in the present invention includes linear, branched or cyclic alkyl alcohols having usually 1 to 12 carbon atoms.
The seeds may be used alone or in combination of two or more.
【0008】本発明に用いるトリオルガノシラノ―ル
は、3個の有機基が互いに同一の基であつても異なる基
であつてもよい。有機基としては、炭素数が通常1〜2
1個の直鎖状、分岐状または環状のアルキル基が挙げら
れ、その他アリ―ル基や置換アリ―ル基であつてもよ
い。In the triorganosilanol used in the present invention, the three organic groups may be the same or different from each other. The organic group usually has 1 to 2 carbon atoms.
One linear, branched or cyclic alkyl group may be mentioned, and it may be an aryl group or a substituted aryl group.
【0009】上記のアルキル基としては、たとえば、メ
チル、エチル、n−プロピル、n−ブチル、n−オクチ
ル、イソプロピル、イソブチル、s−ブチル、t−ブチ
ル、2−エチルヘキシル、シクロプロピル、シクロヘキ
シルなどがあり、置換アリ―ル基としては、ハロゲン、
炭素数が10程度までのアルキル基、アシル基、ニトロ
基またはアミノ基などで置換されたアリ―ル基がある。Examples of the above alkyl group include methyl, ethyl, n-propyl, n-butyl, n-octyl, isopropyl, isobutyl, s-butyl, t-butyl, 2-ethylhexyl, cyclopropyl and cyclohexyl. And the substituted aryl group is halogen,
There is an aryl group substituted with an alkyl group, an acyl group, a nitro group or an amino group having up to about 10 carbon atoms.
【0010】本発明に用いるルイス酸またはルイス塩基
としては、たとえば、ジブチル錫ジラウレ―ト、ジブチ
ル錫ジアセテ―ト、ジブチル錫ジオクトエ―トなどの有
機錫化合物、四塩化チタン、テトラブトキシチタン、チ
タノセンジクロライドなどのチタン化合物などのルイス
酸や、トリエチルアミン、イミダゾ―ルなどのルイス塩
基が挙げられる。Examples of the Lewis acid or Lewis base used in the present invention include organic tin compounds such as dibutyltin dilaurate, dibutyltin diacetate and dibutyltin dioctoate, titanium tetrachloride, tetrabutoxytitanium and titanocene dichloride. And Lewis acids such as titanium compounds, and Lewis bases such as triethylamine and imidazole.
【0011】本発明においては、無水マレイン酸に、上
記の一価アルコ―ル、トリオルガノシラノ―ルおよびル
イス酸またはルイス塩基を加えて、脱水反応を伴うエス
テル化反応を行わせるが、このエステル化反応は、言う
までもなく、無水マレイン酸と一価アルコ―ルとのモノ
エステル化反応と、さらにトリオルガノシラノ―ルとの
シリルエステル化反応との両反応を含むものである。In the present invention, the above-mentioned monovalent alcohol, triorganosilanol and Lewis acid or Lewis base are added to maleic anhydride to carry out an esterification reaction accompanied by a dehydration reaction. Needless to say, the chemical reaction includes both a monoesterification reaction of maleic anhydride and a monovalent alcohol and a silyl esterification reaction of triorganosilanol.
【0012】この両反応は、いずれを先に行つても、ま
た同時に行つてもよく、したがつて無水マレイン酸に対
する一価アルコ―ルおよびトリオルガノシラノ―ルの添
加順序は特に限定されない。しかし、通常は、まず一価
アルコ―ルを加え、つづいてトリオルガノシラノ―ルを
加えるのが普通である。Both of these reactions may be carried out first or simultaneously, and therefore the order of addition of the monovalent alcohol and the triorganosilanol to maleic anhydride is not particularly limited. However, it is usually usual to add the monovalent alcohol first, followed by the triorganosilanol.
【0013】上記の一価アルコ―ルを加えるにあたり、
無水マレイン酸は、固体(結晶)状態のままであつて
も、加温により溶融させた状態であつてもよく、さらに
溶剤に溶解させた溶液状態とされていてもよい。反応の
均一性という点では、後二者の方が望ましい。仮に固体
が残存していても、反応上特に支障はない。In adding the above monovalent alcohol,
Maleic anhydride may be in a solid (crystal) state, may be in a molten state by heating, or may be in a solution state in which it is dissolved in a solvent. The latter two are preferable in terms of reaction uniformity. Even if the solid remains, there is no particular problem in the reaction.
【0014】無水マレイン酸と一価アルコ―ルとのモノ
エステル化反応は、常温でも進行するが、吸熱反応のた
め加温するのも有効である。一価アルコ―ルは、無水マ
レイン酸のカルボキシル基1当量に対し、通常1〜3モ
ルの割合で用いられる。The monoesterification reaction between maleic anhydride and monovalent alcohol proceeds even at room temperature, but it is also effective to heat it because it is an endothermic reaction. The monohydric alcohol is usually used in a proportion of 1 to 3 mol per 1 equivalent of the carboxyl group of maleic anhydride.
【0015】トリオルガノシラノ―ルを加え、ルイス酸
またはルイス塩基の存在下で行わせる脱水反応は、通常
は−70〜300℃、好ましくは−30〜250℃の温
度で、行うことができる。トリオルガノシラノ―ルは、
無水マレイン酸のカルボキシル基1当量に対し、通常1
〜5モルとするのがよい。The dehydration reaction in which triorganosilanol is added and carried out in the presence of a Lewis acid or a Lewis base can be carried out usually at a temperature of -70 to 300 ° C, preferably -30 to 250 ° C. Triorganosilanol
Usually, it is 1 per 1 equivalent of the carboxyl group of maleic anhydride.
It is preferable to set it to ˜5 mol.
【0016】上記の両反応において、反応中に生成する
水分を除去するために、脱水剤を用いてもよい。このよ
うな脱水剤としては、たとえば、無水硫酸マグネシウ
ム、無水硫酸ナトリウム、無水塩化カルシウムなどの無
水無機塩、N・N′−ジシクロヘキシルカルボジイミド
などのカルボジイミド類、シリカゲル、モレキユラ―シ
―ブスなどが挙げられる。In both of the above reactions, a dehydrating agent may be used to remove the water produced during the reaction. Examples of such a dehydrating agent include anhydrous inorganic salts such as anhydrous magnesium sulfate, anhydrous sodium sulfate and anhydrous calcium chloride, carbodiimides such as N.N'-dicyclohexylcarbodiimide, silica gel and molecular sieves. ..
【0017】また、上記の両反応において、無水マレイ
ン酸を溶解したり、溶液反応に使用したりする溶剤とし
ては、ベンゼン、トルエン、キシレンなどの芳香族炭化
水素系溶剤、酢酸エチル、酢酸ブチルなどのエステル系
溶剤、ジエチルエ―テル、テトラヒドロフランなどのエ
―テル系溶剤、ヘキサンなどの脂肪族炭化水素系溶剤な
どがあり、一価アルコ―ルやトリオルガノシラノ―ルの
種類などに応じて適宜選択すればよい。In both of the above reactions, as a solvent for dissolving maleic anhydride or used for the solution reaction, an aromatic hydrocarbon solvent such as benzene, toluene, xylene, ethyl acetate, butyl acetate, etc. There are ester-based solvents, diethyl ether, tetrahydrofuran and other ether-based solvents, and hexane and other aliphatic hydrocarbon-based solvents, etc., which can be selected appropriately according to the type of monovalent alcohol or triorganosilanol. do it.
【0018】このようにして得られる反応生成物は、マ
レイン酸モノエステルのシリルエステル化物を主成分と
したものであつて、これには、言うまでもなく、従来の
ようなアミン塩酸塩の結晶などが全く含まれていない。
このため、この反応生成物の溶液より、溶剤を留去して
から減圧蒸留することにより、目的とするマレイン酸モ
ノエステルのシリルエステル化物からなる重合性モノマ
―を、通常75重量%以上、好適には80重量%以上の
高収率で、かつ通常90重量%以上、好適には95重量
%以上の高純度で、得ることができる。The reaction product thus obtained is mainly composed of a silyl ester of maleic acid monoester, and it goes without saying that the conventional amine hydrochloride crystals and the like are contained therein. Not included at all.
Therefore, the solvent is distilled off from the solution of this reaction product, and then the solvent is distilled off under reduced pressure to obtain a target polymerizable monomer comprising a silyl esterified product of maleic acid monoester in an amount of generally 75% by weight or more. Can be obtained in a high yield of 80% by weight or more and usually in a high purity of 90% by weight or more, preferably 95% by weight or more.
【0019】なお、上記シリルエステル化物であること
の確認は、赤外線吸収スペクトル(IR)や核磁気共鳴
スペクトル(NMR)にて、容易に行える。また、上記
シリルエステル化物の純度は、ガスクロマトグラフイ―
にて測定できる。The silyl esterified product can be easily confirmed by an infrared absorption spectrum (IR) or a nuclear magnetic resonance spectrum (NMR). The purity of the silyl ester compound is determined by gas chromatography.
Can be measured at.
【0020】本発明の方法にて得られるマレイン酸モノ
エステルのシリルエステル化物は、重合性モノマ―とし
て、既知のラジカル重合法などの任意の重合方法にて、
高分子ポリマ―とされ、このポリマ―は、側鎖にシリル
基を有するものとして、加水分解性プラスチツク、水中
防汚被覆剤、医療用高分子材料などの各種の用途に、幅
広く使用することができる。The silyl esterified product of maleic acid monoester obtained by the method of the present invention can be used as a polymerizable monomer by any known polymerization method such as radical polymerization method.
As a polymer, it has a silyl group in its side chain and can be widely used in various applications such as hydrolyzable plastics, underwater antifouling coatings, and polymeric materials for medical use. it can.
【0021】[0021]
【発明の効果】以上のように、本発明の重合性モノマ―
の製造法によれば、従来の塩基存在下での脱塩化水素に
よる方法とは異なり、アミン塩などの中間体を経ること
がないため、多段階の反応が軽減されて、反応工程の簡
素化を図ることができ、またトリエチルアミン塩酸塩な
どの固体の副生成物を分離除去する工程も不要になる。
さらに、上記従来の方法に比べて、得られるマレイン酸
モノエステルのシリルエステル化物からなる重合性モノ
マ―の収率および純度を大きく向上できるなどの顕著な
効果が得られる。As described above, the polymerizable monomer of the present invention is used.
Unlike the conventional method of dehydrochlorination in the presence of a base, the production method of does not pass through intermediates such as amine salts, thus reducing multi-step reactions and simplifying the reaction process. It is also possible to eliminate the step of separating and removing solid by-products such as triethylamine hydrochloride.
Further, as compared with the above-mentioned conventional method, remarkable effects such as a great improvement in yield and purity of the polymerizable monomer composed of the obtained silyl ester of maleic acid monoester can be obtained.
【0022】[0022]
【実施例】以下、実施例により、本発明を具体的に説明
する。EXAMPLES The present invention will be specifically described below with reference to examples.
【0023】実施例1 攪拌機および加温冷却装置を付けた5リツトルの4つ口
フラスコに、酢酸ブチル1リツトルを入れ、その中に無
水マレイン酸1モルを加え、常温にて溶解させたのち、
さらにメチルアルコ―ル1モルを加えた。その後、継続
して攪拌し、トリエチルアミン10ミリモルを加えた。
つぎに、t−ヘキシルジメチルシラノ―ル1.5モルを
40分かけて滴下した。滴下終了後、反応液を80℃に
加熱し、さらに2時間攪拌を継続した。生成した水を還
流状態にして除去したのち、反応を終了した。Example 1 1 liter of butyl acetate was placed in a 5-liter four-necked flask equipped with a stirrer and a heating / cooling device, and 1 mol of maleic anhydride was added to the flask and dissolved at room temperature.
Further, 1 mol of methyl alcohol was added. Then, stirring was continued and 10 mmol of triethylamine was added.
Next, 1.5 mol of t-hexyldimethylsilanol was added dropwise over 40 minutes. After the dropwise addition was completed, the reaction solution was heated to 80 ° C., and stirring was continued for another 2 hours. The produced water was refluxed and removed, and then the reaction was terminated.
【0024】このようにして得た反応生成物の溶液か
ら、ロ―タリ―エバポレ―タ―にて酢酸ブチルを留去し
たのち、減圧蒸留に供した。圧力2.0mmHgにて141
〜143℃を本留として取り出した。得られた重合性モ
ノマ―の収率は79.8重量%、純度は97.9重量%
であつた。From the solution of the reaction product thus obtained, butyl acetate was distilled off with a rotary evaporator, and the solution was subjected to vacuum distillation. 141 at a pressure of 2.0 mmHg
A main distillate of ˜143 ° C. was taken out. The yield of the obtained polymerizable monomer was 79.8% by weight, and the purity was 97.9% by weight.
It was.
【0025】なお、純度は、ガスクロマトグラフイ―に
より測定したものであるが、この測定条件は、下記のと
おりである。 機種:HP社 5890 SERIES II カラム:G−100(化学品検査協会製) カラム温度:230℃(固定) インジエクシヨン・デイジエクシヨン温度:250℃ 流量:19.8ml/分 リテンシヨンタイム:30分The purity is measured by gas chromatography, and the measurement conditions are as follows. Model: HP 5890 SERIES II Column: G-100 (manufactured by Chemicals Inspection Association) Column temperature: 230 ° C (fixed) Injection / Digiexion temperature: 250 ° C Flow rate: 19.8 ml / min Retention time: 30 minutes
【0026】また、上記の実施例1で得られた重合性モ
ノマ―が、マレイン酸モノエステルのシリルエステル化
物であることについては、IRにより、下記の特性吸収
を調べることにより、確認した。 −C(=O)− ; 1700〜1750cm-1 −Si−C− ; 1400〜1480cm-1 −Si−O− ; 1120〜1180cm-1 1200〜1260cm-1 1370〜1410cm-1 The fact that the polymerizable monomer obtained in Example 1 above was a silyl ester of maleic acid monoester was confirmed by investigating the following characteristic absorption by IR. -C (= O)-; 1700 to 1750 cm -1 -Si-C-; 1400 to 1480 cm -1 -Si-O-; 1120 to 1180 cm -1 1200 to 1260 cm -1 1370 to 1410 cm -1
【0027】さらに、NMRにより、 1H−NMR特性
吸収:δ(ppm )を調べることによつても、上記のシリ
ルエステル化物であることを確認した。表1に上記の特
性吸収を示す。NMRの測定条件としては、CDCl3
溶液中、内部標準CHCl3 (δ=7.27)である。Further, it was confirmed by NMR that the 1 H-NMR characteristic absorption: δ (ppm) was the above silyl ester compound. Table 1 shows the above characteristic absorption. The measurement conditions of NMR include CDCl 3
In solution, it is an internal standard CHCl 3 (δ = 7.27).
【0028】[0028]
【表1】 [Table 1]
【0029】なお、参考のために、図1に実施例1で得
た重合性モノマ―のIRスペクトルを、図2に同重合性
モノマ―のNMRスペクトルを、それぞれ示す。For reference, FIG. 1 shows the IR spectrum of the polymerizable monomer obtained in Example 1, and FIG. 2 shows the NMR spectrum of the polymerizable monomer.
【0030】実施例2 攪拌機および加温冷却装置を付けた5リツトルの4つ口
フラスコに、テトラヒドロフラン2リツトルを入れ、そ
の中に無水マレイン酸1モルを加え、常温にて溶解させ
たのち、さらにメチルアルコ―ル1モルを加えた。その
後、継続して攪拌し、ジブチル錫ジアセテ―ト7ミリモ
ルを加えた。つぎに、t−ブチルジメチルシラノ―ル
1.1モルを20分かけて滴下した。滴下終了後、反応
液を80℃に加熱し、さらに2時間攪拌を継続した。生
成した水を還流状態にして除去したのち、反応を終了し
た。Example 2 2 liters of tetrahydrofuran was placed in a 5 liter four-necked flask equipped with a stirrer and a heating / cooling device, and 1 mol of maleic anhydride was added thereto and dissolved at room temperature. 1 mol of methyl alcohol was added. Then, the mixture was continuously stirred and 7 mmol of dibutyltin diacetate was added. Next, 1.1 mol of t-butyldimethylsilanol was added dropwise over 20 minutes. After the dropwise addition was completed, the reaction solution was heated to 80 ° C., and stirring was continued for another 2 hours. The produced water was refluxed and removed, and then the reaction was terminated.
【0031】このようにして得た反応生成物の溶液か
ら、ロ―タリ―エバポレ―タ―にてテトラヒドロフラン
を留去したのち、減圧蒸留に供した。圧力1.0mmHgに
て68〜70℃を本留として取り出した。得られた重合
性モノマ―の収率は91.1重量%、純度は98.1重
量%であつた。Tetrahydrofuran was distilled off from the solution of the reaction product thus obtained by a rotary evaporator, and then the solution was subjected to vacuum distillation. At a pressure of 1.0 mmHg, 68 to 70 ° C. was taken out as the main distillate. The yield of the obtained polymerizable monomer was 91.1% by weight, and the purity was 98.1% by weight.
【0032】なお、この重合性モノマ―が、マレイン酸
モノエステルのシリルエステル化物であることについて
は、実施例1の場合と同様に、IRおよびNMRによ
り、確認同定した。表2にこの重合性モノマ―のNMR
の特性吸収を示す。The fact that the polymerizable monomer was a silyl ester of maleic acid monoester was confirmed and identified by IR and NMR as in the case of Example 1. Table 2 shows the NMR of this polymerizable monomer.
Shows the characteristic absorption of.
【0033】[0033]
【表2】 [Table 2]
【0034】実施例3 攪拌機および加温冷却装置を付けた5リツトルの4つ口
フラスコに、ベンゼン2リツトルを入れ、その中に無水
マレイン酸1モルを加え、常温にて溶解させたのち、メ
チルアルコ―ル1モルを加えた。その後、継続して攪拌
し、イミダゾ―ル12ミリモルを加えた。つぎに、トリ
イソプロピルシラノ―ル1.1モルを40分かけて滴下
した。滴下終了後、反応液を80℃に加熱し、さらに2
時間攪拌を継続した。生成した水を還流状態にして除去
したのち、反応を終了した。Example 3 2 liters of benzene were placed in a 5-liter four-necked flask equipped with a stirrer and a heating / cooling device, and 1 mol of maleic anhydride was added to the flask and dissolved at room temperature. 1 mol of alcohol was added. Then, the mixture was continuously stirred and 12 mmol of imidazole was added. Next, 1.1 mol of triisopropylsilanol was added dropwise over 40 minutes. After the completion of dropping, the reaction solution is heated to 80 ° C. and further 2
Stirring was continued for hours. The produced water was refluxed and removed, and then the reaction was terminated.
【0035】このようにして得た反応生成物の溶液か
ら、ロ―タリ―エバポレ―タ―にてベンゼンを留去した
のち、減圧蒸留に供した。圧力1.5mmHgにて85〜8
7℃を本留として取り出した。得られた重合性モノマ―
の収率は81.4重量%、純度は98.8重量%であつ
た。From the solution of the reaction product thus obtained, benzene was distilled off with a rotary evaporator, and then the solution was subjected to vacuum distillation. 85-8 at a pressure of 1.5 mmHg
The main distillate was taken out at 7 ° C. Obtained polymerizable monomer
The yield was 81.4% by weight and the purity was 98.8% by weight.
【0036】なお、この重合性モノマ―が、マレイン酸
モノエステルのシリルエステル化物であることについて
は、実施例1の場合と同様に、IRおよびNMRによ
り、確認同定した。表3にこの重合性モノマ―のNMR
の特性吸収を示す。The fact that the polymerizable monomer was a silyl ester of maleic acid monoester was confirmed and identified by IR and NMR as in the case of Example 1. Table 3 shows the NMR of this polymerizable monomer.
Shows the characteristic absorption of.
【0037】[0037]
【表3】 [Table 3]
【0038】実施例4 攪拌機および加温冷却装置を付けた5リツトルの4つ口
フラスコに、トルエン2リツトルを入れ、その中に無水
マレイン酸1モルを加え、常温にて溶解させたのち、さ
らにイソアミルアルコ―ル1モルを加えた。その後、常
温にて攪拌しながら、ジブチル錫ジラウレ―ト0.01
モルを加えた。つぎに、トリイソプロピルシラノ―ル1
モルを30分かけて滴下した。滴下終了後、反応液を5
0℃に加熱し、さらに2時間攪拌を継続した。生成した
水を還流状態にして除去したのち、反応を終了した。Example 4 2 liters of toluene was placed in a 5 liters four-necked flask equipped with a stirrer and a heating / cooling device, and 1 mol of maleic anhydride was added to and dissolved in the mixture at room temperature. 1 mol of isoamyl alcohol was added. Then, while stirring at room temperature, dibutyltin dilaurate 0.01
Mole was added. Next, triisopropylsilanol 1
Molar was added dropwise over 30 minutes. After dropping, add 5
Heat to 0 ° C. and continue stirring for an additional 2 hours. The produced water was refluxed and removed, and then the reaction was terminated.
【0039】このようにして得た反応生成物の溶液か
ら、ロ―タリ―エバポレ―タ―にてトルエンを留去した
のち、減圧蒸留に供した。圧力1.5mmHgにて155〜
157℃を本留として取り出した。得られた重合性モノ
マ―の収率は83.3重量%、純度は98.7重量%で
あつた。From the solution of the reaction product thus obtained, toluene was distilled off with a rotary evaporator, and then the solution was subjected to vacuum distillation. 155 at a pressure of 1.5 mmHg
The main distillate was taken out at 157 ° C. The yield of the obtained polymerizable monomer was 83.3% by weight, and the purity was 98.7% by weight.
【0040】なお、この重合性モノマ―が、マレイン酸
モノエステルのシリルエステル化物であることについて
は、実施例1の場合と同様に、IRおよびNMRによ
り、確認同定した。表4にこの重合性モノマ―のNMR
の特性吸収を示す。The fact that the polymerizable monomer was a silyl ester of maleic acid monoester was confirmed and identified by IR and NMR as in the case of Example 1. Table 4 shows the NMR of this polymerizable monomer.
Shows the characteristic absorption of.
【0041】[0041]
【表4】 [Table 4]
【0042】実施例5 攪拌機および加温冷却装置を付けた5リツトルの4つ口
フラスコに、無水マレイン酸1モルを加え、さらにメチ
ルアルコ―ル1モルを加えて、常温にて1時間攪拌を続
けた。5℃に冷却し、継続して攪拌しながら、四塩化チ
タン5ミリモルと無水硫酸マグネシウム0.5モルを加
えた。つぎに、t−ブチルジフエニルシラノ―ル1モル
を30分かけて滴下した。滴下終了後、トルエン1.5
リツトルを加え、反応液を30℃に加温し、さらに2時
間攪拌を継続したのち、反応を終了した。反応中に生成
した水は、無水硫酸マグネシウムにてトラツプした。Example 5 To a 5 liter 4-necked flask equipped with a stirrer and a heating / cooling device, 1 mol of maleic anhydride and 1 mol of methyl alcohol were added, and the mixture was stirred at room temperature for 1 hour. Continued. After cooling to 5 ° C., 5 mmol of titanium tetrachloride and 0.5 mol of anhydrous magnesium sulfate were added with continuous stirring. Next, 1 mol of t-butyldiphenylsilanol was added dropwise over 30 minutes. After completion of dropping, toluene 1.5
A reactor was added, the reaction solution was heated to 30 ° C., stirring was continued for 2 hours, and then the reaction was completed. The water produced during the reaction was trapped with anhydrous magnesium sulfate.
【0043】このようにして得た反応生成物の溶液か
ら、ロ―タリ―エバポレ―タ―にてトルエンを留去した
のち、減圧蒸留に供した。圧力1.0mmHgにて141〜
144℃を本留として取り出した。得られた重合性モノ
マ―の収率は83.1重量%、純度は97.4重量%で
あつた。From the solution of the reaction product thus obtained, toluene was distilled off with a rotary evaporator, and then the solution was subjected to vacuum distillation. 141-at a pressure of 1.0 mmHg
The main distillate was taken out at 144 ° C. The yield of the obtained polymerizable monomer was 83.1% by weight, and the purity was 97.4% by weight.
【0044】なお、この重合性モノマ―が、マレイン酸
モノエステルのシリルエステル化物であることについて
は、実施例1の場合と同様に、IRおよびNMRによ
り、確認同定した。表5にこの重合性モノマ―のNMR
の特性吸収を示す。The fact that the polymerizable monomer was a silyl ester of maleic acid monoester was confirmed and identified by IR and NMR as in the case of Example 1. Table 5 shows the NMR of this polymerizable monomer.
Shows the characteristic absorption of.
【0045】[0045]
【表5】 [Table 5]
【0046】実施例6 攪拌機および加温冷却装置を付けた5リツトルの4つ口
フラスコに、無水マレイン酸1モルを加え、80℃に加
温して溶融させたのち、さらにn−アミルアルコ―ル1
モルを加え、80℃に30分間保持した。その後、継続
して攪拌し、ジブチル錫ジアセテ―ト10ミリモルおよ
び無水硫酸マグネシウム0.5モルを加えた。トルエン
2リツトルを加入後、トリイソプロピルシラノ―ル1.
1モルを40分かけて滴下した。滴下終了後、反応液を
50℃に加熱し、さらに2時間攪拌を継続した。生成し
た水を還流状態にして除去したのち、反応を終了した。Example 6 1 mol of maleic anhydride was added to a 5 liter 4-necked flask equipped with a stirrer and a heating / cooling device, and the mixture was heated to 80 ° C. to be melted and then n-amyl alcohol. 1
Mol was added and the mixture was kept at 80 ° C. for 30 minutes. Then, the mixture was continuously stirred, and 10 mmol of dibutyltin diacetate and 0.5 mol of anhydrous magnesium sulfate were added. After adding 2 liters of toluene, triisopropylsilanol 1.
1 mol was added dropwise over 40 minutes. After the dropwise addition was completed, the reaction solution was heated to 50 ° C., and stirring was continued for 2 hours. The produced water was refluxed and removed, and then the reaction was terminated.
【0047】このようにして得た反応生成物の溶液か
ら、ロ―タリ―エバポレ―タ―にてトルエンを留去した
のち、減圧蒸留に供した。圧力2.0mmHgにて141〜
143℃を本留として取り出した。得られた重合性モノ
マ―の収率は85.0重量%、純度は96.8重量%で
あつた。From the solution of the reaction product thus obtained, toluene was distilled off with a rotary evaporator, and then the solution was subjected to vacuum distillation. 141-at a pressure of 2.0 mmHg
The main distillate was taken out at 143 ° C. The yield of the obtained polymerizable monomer was 85.0% by weight, and the purity was 96.8% by weight.
【0048】なお、この重合性モノマ―が、マレイン酸
モノエステルのシリルエステル化物であることについて
は、実施例1の場合と同様に、IRおよびNMRによ
り、確認同定した。表6にこの重合性モノマ―のNMR
の特性吸収を示す。The fact that the polymerizable monomer was a silyl ester of maleic acid monoester was confirmed and identified by IR and NMR as in the case of Example 1. Table 6 shows the NMR of this polymerizable monomer.
Shows the characteristic absorption of.
【0049】[0049]
【表6】 [Table 6]
【0050】比較例1 攪拌機および加温冷却装置を付けた5リツトルの4つ口
フラスコに、トルエン1リツトルを入れ、その中に無水
マレイン酸1モルを加えて、溶解させたのち、さらにメ
チルアルコ―ル1モルを加えた。その後、反応液を5℃
にし、攪拌しながら、トリエチルアミン1モルを1時間
かけて滴下した。滴下部は黄色するが、攪拌することに
より無色透明になつた。反応温度は20℃に維持した。Comparative Example 1 1 liter of toluene was placed in a 4-necked 5-liter four-necked flask equipped with a stirrer and a heating / cooling device, and 1 mol of maleic anhydride was added to and dissolved in the mixture. -1 mol of ru was added. After that, the reaction solution is 5 ° C.
Then, with stirring, 1 mol of triethylamine was added dropwise over 1 hour. The dropping part turned yellow, but became colorless and transparent by stirring. The reaction temperature was maintained at 20 ° C.
【0051】つぎに、この透明液体を10℃に保ち、継
続して攪拌しながら、t−ブチルジメチルクロロシラン
1モルを15分かけて滴下した。滴下直後からトリエチ
ルアミンの塩酸塩の析出が観察された。滴下終了後、常
温にてさらに2時間攪拌を続けた。Next, while maintaining the transparent liquid at 10 ° C. and continuously stirring, 1 mol of t-butyldimethylchlorosilane was added dropwise over 15 minutes. Immediately after the dropping, precipitation of hydrochloride of triethylamine was observed. After completion of the dropping, stirring was continued for another 2 hours at room temperature.
【0052】このようにして得た反応生成物の溶液を、
ガラスフイルタ―にて吸引ろ過してトリエチルアミンの
塩酸塩を除去した。ろ過残渣はトルエン0.5リツトル
にて洗浄し、この洗浄溶剤をろ液に加えた。ついで、ロ
―タリ―エバポレ―タ―にて、ろ液からトルエンを留去
したのち、減圧蒸留に供した。圧力8.0mmHgにて11
2〜115℃を本留として取り出した。蒸留物中に一部
白色針状晶が認められた。得られた重合性モノマ―の収
率は71.5重量%、純度は82.2重量%であつた。The solution of the reaction product thus obtained is
Suction filtration was performed using a glass filter to remove the triethylamine hydrochloride. The filtration residue was washed with 0.5 liter of toluene, and this washing solvent was added to the filtrate. Then, toluene was distilled off from the filtrate with a rotary evaporator, and the residue was subjected to vacuum distillation. 11 at a pressure of 8.0 mmHg
The main distillate was taken out at 2 to 115 ° C. Some white needle-like crystals were found in the distillate. The yield of the obtained polymerizable monomer was 71.5% by weight, and the purity was 82.2% by weight.
【0053】なお、この重合性モノマ―が、マレイン酸
モノエステルのシリルエステル化物であることについて
は、実施例1の場合と同様に、IRおよびNMRによ
り、確認同定した。このIR特性吸収およびNMR特性
吸収は、前記の実施例2の結果とほぼ同じであつた。The fact that the polymerizable monomer was a silyl ester of maleic acid monoester was confirmed and identified by IR and NMR as in the case of Example 1. The IR characteristic absorption and the NMR characteristic absorption were almost the same as the results of Example 2 described above.
【0054】以上の結果から明らかなように、実施例1
〜6においては、いずれも反応工程が簡素化されてお
り、かつ反応中に副生成物の発生がみられず、目的とす
る重合性モノマ―の収率および純度も良好であつた。As is clear from the above results, Example 1
In Nos. 6 to 6, the reaction process was simplified, no by-products were generated during the reaction, and the yield and purity of the target polymerizable monomer were good.
【0055】これに対し、比較例1では、マレイン酸モ
ノエステルのアミン塩からなる中間体を生成する工程が
必要であり、かつ反応中に副生成物であるトリエチルア
ミンの塩酸塩の発生がみられ、反応後にこれを取り除く
工程が必要となるなど、製造工程上の不利を免れなかつ
た。また、目的とする重合性モノマ―の収率および純度
が低かつた。On the other hand, in Comparative Example 1, a step of producing an intermediate consisting of an amine salt of maleic acid monoester is required, and generation of a hydrochloride of triethylamine as a by-product is observed during the reaction. However, there was a disadvantage in the manufacturing process such as the step of removing this after the reaction was necessary. In addition, the yield and purity of the target polymerizable monomer were low.
【図1】実施例1で得られた重合性モノマ―の赤外線吸
収スペクトルを示す特性図である。FIG. 1 is a characteristic diagram showing an infrared absorption spectrum of a polymerizable monomer obtained in Example 1.
【図2】実施例1で得られた重合性モノマ―の核磁気共
鳴スペクトルを示す特性図である。2 is a characteristic diagram showing a nuclear magnetic resonance spectrum of the polymerizable monomer obtained in Example 1. FIG.
Claims (1)
リオルガノシラノ―ルおよびルイス酸またはルイス塩基
を加え、脱水反応を伴うエステル化反応を行わせて、マ
レイン酸モノエステルのシリルエステル化物からなる重
合性モノマ―を製造することを特徴とする重合性モノマ
―の製造法。Claims: 1. Maleic anhydride is added with monovalent alcohol, triorganosilanol and Lewis acid or Lewis base to carry out an esterification reaction accompanied by a dehydration reaction to give maleic acid. A method for producing a polymerizable monomer, which comprises producing a polymerizable monomer comprising a monoester silyl ester compound.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP3204892A JPH0525186A (en) | 1991-07-20 | 1991-07-20 | Production of polymerizable monomer |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP3204892A JPH0525186A (en) | 1991-07-20 | 1991-07-20 | Production of polymerizable monomer |
Publications (1)
Publication Number | Publication Date |
---|---|
JPH0525186A true JPH0525186A (en) | 1993-02-02 |
Family
ID=16498127
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP3204892A Pending JPH0525186A (en) | 1991-07-20 | 1991-07-20 | Production of polymerizable monomer |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH0525186A (en) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP1431301A1 (en) * | 2002-12-20 | 2004-06-23 | Sigma Coatings B.V. | Process for the production of silyl carboxylate monomers |
WO2004056838A1 (en) * | 2002-12-20 | 2004-07-08 | Sigma Coatings B.V. | Process for the production of silyl carboxylate monomers |
-
1991
- 1991-07-20 JP JP3204892A patent/JPH0525186A/en active Pending
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP1431301A1 (en) * | 2002-12-20 | 2004-06-23 | Sigma Coatings B.V. | Process for the production of silyl carboxylate monomers |
WO2004056838A1 (en) * | 2002-12-20 | 2004-07-08 | Sigma Coatings B.V. | Process for the production of silyl carboxylate monomers |
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