JPH09249657A - Purification of glycidyl (meth)acrilate - Google Patents
Purification of glycidyl (meth)acrilateInfo
- Publication number
- JPH09249657A JPH09249657A JP5560896A JP5560896A JPH09249657A JP H09249657 A JPH09249657 A JP H09249657A JP 5560896 A JP5560896 A JP 5560896A JP 5560896 A JP5560896 A JP 5560896A JP H09249657 A JPH09249657 A JP H09249657A
- Authority
- JP
- Japan
- Prior art keywords
- meth
- epichlorohydrin
- acrylate
- glycidyl
- crude
- 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
- 125000003055 glycidyl group Chemical group C(C1CO1)* 0.000 title claims abstract description 37
- 238000000746 purification Methods 0.000 title description 9
- BRLQWZUYTZBJKN-UHFFFAOYSA-N Epichlorohydrin Chemical compound ClCC1CO1 BRLQWZUYTZBJKN-UHFFFAOYSA-N 0.000 claims abstract description 53
- NIXOWILDQLNWCW-UHFFFAOYSA-M Acrylate Chemical compound [O-]C(=O)C=C NIXOWILDQLNWCW-UHFFFAOYSA-M 0.000 claims abstract description 33
- 150000003839 salts Chemical class 0.000 claims abstract description 22
- CERQOIWHTDAKMF-UHFFFAOYSA-N Methacrylic acid Chemical compound CC(=C)C(O)=O CERQOIWHTDAKMF-UHFFFAOYSA-N 0.000 claims abstract description 16
- 229910052783 alkali metal Inorganic materials 0.000 claims abstract description 13
- 150000007514 bases Chemical class 0.000 claims abstract description 11
- -1 alkali metal salt Chemical class 0.000 claims abstract description 10
- LSNNMFCWUKXFEE-UHFFFAOYSA-M Bisulfite Chemical compound OS([O-])=O LSNNMFCWUKXFEE-UHFFFAOYSA-M 0.000 claims abstract description 8
- 229910052784 alkaline earth metal Inorganic materials 0.000 claims abstract description 8
- BDHFUVZGWQCTTF-UHFFFAOYSA-M sulfonate Chemical compound [O-]S(=O)=O BDHFUVZGWQCTTF-UHFFFAOYSA-M 0.000 claims abstract description 8
- 150000001342 alkaline earth metals Chemical class 0.000 claims abstract description 7
- 238000004821 distillation Methods 0.000 claims description 27
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 26
- 238000000034 method Methods 0.000 claims description 24
- 150000001340 alkali metals Chemical class 0.000 claims description 9
- 238000001914 filtration Methods 0.000 claims description 8
- 238000005406 washing Methods 0.000 claims description 7
- ZAMOUSCENKQFHK-UHFFFAOYSA-N Chlorine atom Chemical compound [Cl] ZAMOUSCENKQFHK-UHFFFAOYSA-N 0.000 abstract description 14
- 239000000460 chlorine Substances 0.000 abstract description 14
- 229910052801 chlorine Inorganic materials 0.000 abstract description 14
- 239000002994 raw material Substances 0.000 abstract description 9
- 150000001805 chlorine compounds Chemical class 0.000 abstract description 7
- 229910052751 metal Inorganic materials 0.000 abstract description 3
- 239000002184 metal Substances 0.000 abstract description 3
- HEMHJVSKTPXQMS-UHFFFAOYSA-M Sodium hydroxide Chemical compound [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 description 39
- VOZRXNHHFUQHIL-UHFFFAOYSA-N glycidyl methacrylate Chemical compound CC(=C)C(=O)OCC1CO1 VOZRXNHHFUQHIL-UHFFFAOYSA-N 0.000 description 32
- 238000006243 chemical reaction Methods 0.000 description 21
- 239000000203 mixture Substances 0.000 description 11
- 238000007664 blowing Methods 0.000 description 10
- 230000000052 comparative effect Effects 0.000 description 10
- OKIZCWYLBDKLSU-UHFFFAOYSA-M N,N,N-Trimethylmethanaminium chloride Chemical compound [Cl-].C[N+](C)(C)C OKIZCWYLBDKLSU-UHFFFAOYSA-M 0.000 description 9
- 238000002360 preparation method Methods 0.000 description 9
- RPQRDASANLAFCM-UHFFFAOYSA-N oxiran-2-ylmethyl prop-2-enoate Chemical compound C=CC(=O)OCC1CO1 RPQRDASANLAFCM-UHFFFAOYSA-N 0.000 description 6
- 239000000047 product Substances 0.000 description 6
- JOXIMZWYDAKGHI-UHFFFAOYSA-N toluene-4-sulfonic acid Chemical compound CC1=CC=C(S(O)(=O)=O)C=C1 JOXIMZWYDAKGHI-UHFFFAOYSA-N 0.000 description 6
- 150000003242 quaternary ammonium salts Chemical class 0.000 description 5
- VEXZGXHMUGYJMC-UHFFFAOYSA-M Chloride anion Chemical compound [Cl-] VEXZGXHMUGYJMC-UHFFFAOYSA-M 0.000 description 4
- KVCGISUBCHHTDD-UHFFFAOYSA-M sodium;4-methylbenzenesulfonate Chemical compound [Na+].CC1=CC=C(S([O-])(=O)=O)C=C1 KVCGISUBCHHTDD-UHFFFAOYSA-M 0.000 description 4
- WJFKNYWRSNBZNX-UHFFFAOYSA-N 10H-phenothiazine Chemical compound C1=CC=C2NC3=CC=CC=C3SC2=C1 WJFKNYWRSNBZNX-UHFFFAOYSA-N 0.000 description 3
- WMFOQBRAJBCJND-UHFFFAOYSA-M Lithium hydroxide Chemical compound [Li+].[OH-] WMFOQBRAJBCJND-UHFFFAOYSA-M 0.000 description 3
- KWYUFKZDYYNOTN-UHFFFAOYSA-M Potassium hydroxide Chemical compound [OH-].[K+] KWYUFKZDYYNOTN-UHFFFAOYSA-M 0.000 description 3
- CDBYLPFSWZWCQE-UHFFFAOYSA-L Sodium Carbonate Chemical compound [Na+].[Na+].[O-]C([O-])=O CDBYLPFSWZWCQE-UHFFFAOYSA-L 0.000 description 3
- 239000007864 aqueous solution Substances 0.000 description 3
- 239000006227 byproduct Substances 0.000 description 3
- 229950000688 phenothiazine Drugs 0.000 description 3
- 238000006116 polymerization reaction Methods 0.000 description 3
- SONHXMAHPHADTF-UHFFFAOYSA-M sodium;2-methylprop-2-enoate Chemical compound [Na+].CC(=C)C([O-])=O SONHXMAHPHADTF-UHFFFAOYSA-M 0.000 description 3
- 239000000243 solution Substances 0.000 description 3
- NEBBLNDVSSWJLL-UHFFFAOYSA-N 2,3-bis(2-methylprop-2-enoyloxy)propyl 2-methylprop-2-enoate Chemical compound CC(=C)C(=O)OCC(OC(=O)C(C)=C)COC(=O)C(C)=C NEBBLNDVSSWJLL-UHFFFAOYSA-N 0.000 description 2
- UPTHZKIDNHJFKQ-UHFFFAOYSA-N 2-methylprop-2-enoic acid;propane-1,2,3-triol Chemical compound CC(=C)C(O)=O.CC(=C)C(O)=O.OCC(O)CO UPTHZKIDNHJFKQ-UHFFFAOYSA-N 0.000 description 2
- NLXLAEXVIDQMFP-UHFFFAOYSA-N Ammonia chloride Chemical compound [NH4+].[Cl-] NLXLAEXVIDQMFP-UHFFFAOYSA-N 0.000 description 2
- VTYYLEPIZMXCLO-UHFFFAOYSA-L Calcium carbonate Chemical compound [Ca+2].[O-]C([O-])=O VTYYLEPIZMXCLO-UHFFFAOYSA-L 0.000 description 2
- 239000004593 Epoxy Substances 0.000 description 2
- AFVFQIVMOAPDHO-UHFFFAOYSA-N Methanesulfonic acid Chemical compound CS(O)(=O)=O AFVFQIVMOAPDHO-UHFFFAOYSA-N 0.000 description 2
- 229910001860 alkaline earth metal hydroxide Inorganic materials 0.000 description 2
- 238000004458 analytical method Methods 0.000 description 2
- HTZCNXWZYVXIMZ-UHFFFAOYSA-M benzyl(triethyl)azanium;chloride Chemical compound [Cl-].CC[N+](CC)(CC)CC1=CC=CC=C1 HTZCNXWZYVXIMZ-UHFFFAOYSA-M 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 239000007789 gas Substances 0.000 description 2
- 229920000642 polymer Polymers 0.000 description 2
- 238000011085 pressure filtration Methods 0.000 description 2
- 239000011541 reaction mixture Substances 0.000 description 2
- 238000010992 reflux Methods 0.000 description 2
- 238000007086 side reaction Methods 0.000 description 2
- SQGYOTSLMSWVJD-UHFFFAOYSA-N silver(1+) nitrate Chemical compound [Ag+].[O-]N(=O)=O SQGYOTSLMSWVJD-UHFFFAOYSA-N 0.000 description 2
- 238000003756 stirring Methods 0.000 description 2
- 150000003871 sulfonates Chemical class 0.000 description 2
- 150000003460 sulfonic acids Chemical class 0.000 description 2
- NHGXDBSUJJNIRV-UHFFFAOYSA-M tetrabutylammonium chloride Chemical compound [Cl-].CCCC[N+](CCCC)(CCCC)CCCC NHGXDBSUJJNIRV-UHFFFAOYSA-M 0.000 description 2
- LWIHDJKSTIGBAC-UHFFFAOYSA-K tripotassium phosphate Chemical compound [K+].[K+].[K+].[O-]P([O-])([O-])=O LWIHDJKSTIGBAC-UHFFFAOYSA-K 0.000 description 2
- LDMOEFOXLIZJOW-UHFFFAOYSA-N 1-dodecanesulfonic acid Chemical compound CCCCCCCCCCCCS(O)(=O)=O LDMOEFOXLIZJOW-UHFFFAOYSA-N 0.000 description 1
- SMZOUWXMTYCWNB-UHFFFAOYSA-N 2-(2-methoxy-5-methylphenyl)ethanamine Chemical compound COC1=CC=C(C)C=C1CCN SMZOUWXMTYCWNB-UHFFFAOYSA-N 0.000 description 1
- ZVNYKZKUBKIIAH-UHFFFAOYSA-N 2-(oxiran-2-yl)acetic acid Chemical compound OC(=O)CC1CO1 ZVNYKZKUBKIIAH-UHFFFAOYSA-N 0.000 description 1
- NIXOWILDQLNWCW-UHFFFAOYSA-N 2-Propenoic acid Natural products OC(=O)C=C NIXOWILDQLNWCW-UHFFFAOYSA-N 0.000 description 1
- WBIQQQGBSDOWNP-UHFFFAOYSA-N 2-dodecylbenzenesulfonic acid Chemical compound CCCCCCCCCCCCC1=CC=CC=C1S(O)(=O)=O WBIQQQGBSDOWNP-UHFFFAOYSA-N 0.000 description 1
- 229910019142 PO4 Inorganic materials 0.000 description 1
- 239000004820 Pressure-sensitive adhesive Substances 0.000 description 1
- QAOWNCQODCNURD-UHFFFAOYSA-L Sulfate Chemical compound [O-]S([O-])(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-L 0.000 description 1
- NPGKBLFMWGHJGI-UHFFFAOYSA-M [Cl-].[PH4+].C(C1=CC=CC=C1)[N+](CC)(CC)CC.[Cl-] Chemical compound [Cl-].[PH4+].C(C1=CC=CC=C1)[N+](CC)(CC)CC.[Cl-] NPGKBLFMWGHJGI-UHFFFAOYSA-M 0.000 description 1
- 150000001252 acrylic acid derivatives Chemical class 0.000 description 1
- 125000003647 acryloyl group Chemical group O=C([*])C([H])=C([H])[H] 0.000 description 1
- 239000000853 adhesive Substances 0.000 description 1
- 230000001070 adhesive effect Effects 0.000 description 1
- 239000003513 alkali Substances 0.000 description 1
- 229910001854 alkali hydroxide Inorganic materials 0.000 description 1
- 150000008044 alkali metal hydroxides Chemical class 0.000 description 1
- 229910000272 alkali metal oxide Inorganic materials 0.000 description 1
- 125000002947 alkylene group Chemical group 0.000 description 1
- 235000019270 ammonium chloride Nutrition 0.000 description 1
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 1
- RZSJZEHKTBMMDZ-UHFFFAOYSA-N azanium;1,2,3-triethylbenzene;chloride Chemical compound [NH4+].[Cl-].CCC1=CC=CC(CC)=C1CC RZSJZEHKTBMMDZ-UHFFFAOYSA-N 0.000 description 1
- 238000010533 azeotropic distillation Methods 0.000 description 1
- RQPZNWPYLFFXCP-UHFFFAOYSA-L barium dihydroxide Chemical compound [OH-].[OH-].[Ba+2] RQPZNWPYLFFXCP-UHFFFAOYSA-L 0.000 description 1
- 229910001863 barium hydroxide Inorganic materials 0.000 description 1
- SRSXLGNVWSONIS-UHFFFAOYSA-N benzenesulfonic acid Chemical compound OS(=O)(=O)C1=CC=CC=C1 SRSXLGNVWSONIS-UHFFFAOYSA-N 0.000 description 1
- 229940092714 benzenesulfonic acid Drugs 0.000 description 1
- KXHPPCXNWTUNSB-UHFFFAOYSA-M benzyl(trimethyl)azanium;chloride Chemical compound [Cl-].C[N+](C)(C)CC1=CC=CC=C1 KXHPPCXNWTUNSB-UHFFFAOYSA-M 0.000 description 1
- TXXACRDXEHKXKD-UHFFFAOYSA-M benzyl(trimethyl)phosphanium;chloride Chemical compound [Cl-].C[P+](C)(C)CC1=CC=CC=C1 TXXACRDXEHKXKD-UHFFFAOYSA-M 0.000 description 1
- 229910000019 calcium carbonate Inorganic materials 0.000 description 1
- AXCZMVOFGPJBDE-UHFFFAOYSA-L calcium dihydroxide Chemical compound [OH-].[OH-].[Ca+2] AXCZMVOFGPJBDE-UHFFFAOYSA-L 0.000 description 1
- 239000000920 calcium hydroxide Substances 0.000 description 1
- 229910001861 calcium hydroxide Inorganic materials 0.000 description 1
- BRPQOXSCLDDYGP-UHFFFAOYSA-N calcium oxide Chemical compound [O-2].[Ca+2] BRPQOXSCLDDYGP-UHFFFAOYSA-N 0.000 description 1
- 239000000292 calcium oxide Substances 0.000 description 1
- ODINCKMPIJJUCX-UHFFFAOYSA-N calcium oxide Inorganic materials [Ca]=O ODINCKMPIJJUCX-UHFFFAOYSA-N 0.000 description 1
- 150000004649 carbonic acid derivatives Chemical class 0.000 description 1
- 150000001732 carboxylic acid derivatives Chemical class 0.000 description 1
- 239000003054 catalyst Substances 0.000 description 1
- 238000004587 chromatography analysis Methods 0.000 description 1
- 150000001875 compounds Chemical class 0.000 description 1
- 238000011109 contamination Methods 0.000 description 1
- 238000005260 corrosion Methods 0.000 description 1
- 230000007797 corrosion Effects 0.000 description 1
- 230000018044 dehydration Effects 0.000 description 1
- 238000006297 dehydration reaction Methods 0.000 description 1
- 239000002270 dispersing agent Substances 0.000 description 1
- 229940060296 dodecylbenzenesulfonic acid Drugs 0.000 description 1
- 230000005684 electric field Effects 0.000 description 1
- 125000003700 epoxy group Chemical group 0.000 description 1
- UXYBXUYUKHUNOM-UHFFFAOYSA-M ethyl(trimethyl)azanium;chloride Chemical compound [Cl-].CC[N+](C)(C)C UXYBXUYUKHUNOM-UHFFFAOYSA-M 0.000 description 1
- NCHUDIWSIORHHB-UHFFFAOYSA-M ethyl(trimethyl)phosphanium;chloride Chemical compound [Cl-].CC[P+](C)(C)C NCHUDIWSIORHHB-UHFFFAOYSA-M 0.000 description 1
- 239000000835 fiber Substances 0.000 description 1
- 238000004817 gas chromatography Methods 0.000 description 1
- 239000000383 hazardous chemical Substances 0.000 description 1
- 231100000206 health hazard Toxicity 0.000 description 1
- 230000002401 inhibitory effect Effects 0.000 description 1
- 238000002347 injection Methods 0.000 description 1
- 239000007924 injection Substances 0.000 description 1
- VTHJTEIRLNZDEV-UHFFFAOYSA-L magnesium dihydroxide Chemical compound [OH-].[OH-].[Mg+2] VTHJTEIRLNZDEV-UHFFFAOYSA-L 0.000 description 1
- 239000000347 magnesium hydroxide Substances 0.000 description 1
- 229910001862 magnesium hydroxide Inorganic materials 0.000 description 1
- 239000000395 magnesium oxide Substances 0.000 description 1
- CPLXHLVBOLITMK-UHFFFAOYSA-N magnesium oxide Inorganic materials [Mg]=O CPLXHLVBOLITMK-UHFFFAOYSA-N 0.000 description 1
- AXZKOIWUVFPNLO-UHFFFAOYSA-N magnesium;oxygen(2-) Chemical compound [O-2].[Mg+2] AXZKOIWUVFPNLO-UHFFFAOYSA-N 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 238000005259 measurement Methods 0.000 description 1
- 150000002739 metals Chemical class 0.000 description 1
- 229940098779 methanesulfonic acid Drugs 0.000 description 1
- 125000002496 methyl group Chemical group [H]C([H])([H])* 0.000 description 1
- 238000002156 mixing Methods 0.000 description 1
- 239000003607 modifier Substances 0.000 description 1
- 239000000178 monomer Substances 0.000 description 1
- 239000001301 oxygen Substances 0.000 description 1
- 229910052760 oxygen Inorganic materials 0.000 description 1
- 239000003973 paint Substances 0.000 description 1
- 235000021317 phosphate Nutrition 0.000 description 1
- 150000003013 phosphoric acid derivatives Chemical class 0.000 description 1
- 231100000614 poison Toxicity 0.000 description 1
- 239000002574 poison Substances 0.000 description 1
- 229910000160 potassium phosphate Inorganic materials 0.000 description 1
- 235000011009 potassium phosphates Nutrition 0.000 description 1
- 239000000843 powder Substances 0.000 description 1
- 150000003864 primary ammonium salts Chemical class 0.000 description 1
- 230000000630 rising effect Effects 0.000 description 1
- 229920006395 saturated elastomer Polymers 0.000 description 1
- 229910001961 silver nitrate Inorganic materials 0.000 description 1
- 229940077386 sodium benzenesulfonate Drugs 0.000 description 1
- 229910000029 sodium carbonate Inorganic materials 0.000 description 1
- 239000001488 sodium phosphate Substances 0.000 description 1
- 229910000162 sodium phosphate Inorganic materials 0.000 description 1
- MZSDGDXXBZSFTG-UHFFFAOYSA-M sodium;benzenesulfonate Chemical compound [Na+].[O-]S(=O)(=O)C1=CC=CC=C1 MZSDGDXXBZSFTG-UHFFFAOYSA-M 0.000 description 1
- DAJSVUQLFFJUSX-UHFFFAOYSA-M sodium;dodecane-1-sulfonate Chemical compound [Na+].CCCCCCCCCCCCS([O-])(=O)=O DAJSVUQLFFJUSX-UHFFFAOYSA-M 0.000 description 1
- KKVTYAVXTDIPAP-UHFFFAOYSA-M sodium;methanesulfonate Chemical compound [Na+].CS([O-])(=O)=O KKVTYAVXTDIPAP-UHFFFAOYSA-M 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 229910021653 sulphate ion Inorganic materials 0.000 description 1
- IBWGNZVCJVLSHB-UHFFFAOYSA-M tetrabutylphosphanium;chloride Chemical compound [Cl-].CCCC[P+](CCCC)(CCCC)CCCC IBWGNZVCJVLSHB-UHFFFAOYSA-M 0.000 description 1
- HWCKGOZZJDHMNC-UHFFFAOYSA-M tetraethylammonium bromide Chemical compound [Br-].CC[N+](CC)(CC)CC HWCKGOZZJDHMNC-UHFFFAOYSA-M 0.000 description 1
- YMBCJWGVCUEGHA-UHFFFAOYSA-M tetraethylammonium chloride Chemical compound [Cl-].CC[N+](CC)(CC)CC YMBCJWGVCUEGHA-UHFFFAOYSA-M 0.000 description 1
- UQFSVBXCNGCBBW-UHFFFAOYSA-M tetraethylammonium iodide Chemical compound [I-].CC[N+](CC)(CC)CC UQFSVBXCNGCBBW-UHFFFAOYSA-M 0.000 description 1
- SZWHXXNVLACKBV-UHFFFAOYSA-N tetraethylphosphanium Chemical compound CC[P+](CC)(CC)CC SZWHXXNVLACKBV-UHFFFAOYSA-N 0.000 description 1
- LIXPXSXEKKHIRR-UHFFFAOYSA-M tetraethylphosphanium;bromide Chemical compound [Br-].CC[P+](CC)(CC)CC LIXPXSXEKKHIRR-UHFFFAOYSA-M 0.000 description 1
- FBOJNMRAZJRCNS-UHFFFAOYSA-M tetraethylphosphanium;chloride Chemical compound [Cl-].CC[P+](CC)(CC)CC FBOJNMRAZJRCNS-UHFFFAOYSA-M 0.000 description 1
- DDFYFBUWEBINLX-UHFFFAOYSA-M tetramethylammonium bromide Chemical compound [Br-].C[N+](C)(C)C DDFYFBUWEBINLX-UHFFFAOYSA-M 0.000 description 1
- RXMRGBVLCSYIBO-UHFFFAOYSA-M tetramethylazanium;iodide Chemical compound [I-].C[N+](C)(C)C RXMRGBVLCSYIBO-UHFFFAOYSA-M 0.000 description 1
- BXYHVFRRNNWPMB-UHFFFAOYSA-N tetramethylphosphanium Chemical compound C[P+](C)(C)C BXYHVFRRNNWPMB-UHFFFAOYSA-N 0.000 description 1
- ZTXFOCMYRCGSMU-UHFFFAOYSA-M tetramethylphosphanium;bromide Chemical compound [Br-].C[P+](C)(C)C ZTXFOCMYRCGSMU-UHFFFAOYSA-M 0.000 description 1
- NJFUXFRJVIXVSG-UHFFFAOYSA-M tetramethylphosphanium;chloride Chemical compound [Cl-].C[P+](C)(C)C NJFUXFRJVIXVSG-UHFFFAOYSA-M 0.000 description 1
- NIUZJTWSUGSWJI-UHFFFAOYSA-M triethyl(methyl)azanium;chloride Chemical compound [Cl-].CC[N+](C)(CC)CC NIUZJTWSUGSWJI-UHFFFAOYSA-M 0.000 description 1
- TVPZYULFHHZTQD-UHFFFAOYSA-M triethyl(methyl)phosphanium;chloride Chemical compound [Cl-].CC[P+](C)(CC)CC TVPZYULFHHZTQD-UHFFFAOYSA-M 0.000 description 1
- RYFMWSXOAZQYPI-UHFFFAOYSA-K trisodium phosphate Chemical compound [Na+].[Na+].[Na+].[O-]P([O-])([O-])=O RYFMWSXOAZQYPI-UHFFFAOYSA-K 0.000 description 1
Landscapes
- Epoxy Compounds (AREA)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
Abstract
Description
【0001】[0001]
【発明の属する技術分野】本発明は、エピクロルヒドリ
ンを反応原料として得られた粗(メタ)アクリル酸グリ
シジルの精製方法に関するものである。TECHNICAL FIELD The present invention relates to a method for purifying crude glycidyl (meth) acrylate obtained by using epichlorohydrin as a reaction raw material.
【0002】[0002]
【従来の技術】1分子中に重合性のアクリロイル基また
はメタクロイル基とエポキシ基を有する(メタ)アクリ
ル酸グリシジルは、その構造上の特徴から、反応性モノ
マ―として広い分野に使用されている。たとえば、塗
料、接着剤、粘着剤、繊維改質剤、分散剤、レジスト材
料などの多岐にわたつている。2. Description of the Related Art Glycidyl (meth) acrylate having a polymerizable acryloyl group or methacryloyl group and an epoxy group in one molecule is widely used as a reactive monomer due to its structural characteristics. For example, it is widely used in paints, adhesives, pressure sensitive adhesives, fiber modifiers, dispersants, resist materials, and the like.
【0003】(メタ)アクリル酸グリシジルを製造する
には、第一の方法として、(メタ)アクリル酸とエピク
ロルヒドリンを反応原料とする方法(特公昭37−74
54号公報)、第二の方法として、(メタ)アクリル酸
のアルカリ金属塩とエピクロルヒドリンを反応原料とす
る方法(特公昭45−28762号公報)、第三の方法
として、(メタ)アクリル酸メチルとグリシド―ルを反
応原料とする方法(特公昭47−38421号公報)
が、知られている。The first method for producing glycidyl (meth) acrylate is to use (meth) acrylic acid and epichlorohydrin as reaction raw materials (Japanese Patent Publication No. 37-74).
54), the second method is to use an alkali metal salt of (meth) acrylic acid and epichlorohydrin as reaction raw materials (Japanese Patent Publication No. 45-28762), and the third method is methyl (meth) acrylate. And glycidyl as reaction raw materials (JP-B-47-38421)
It has been known.
【0004】このうち、エピクロルヒドリンを反応原料
とする第一および第二の方法は、最も汎用的な方法とし
て知られるが、これらの方法によると、未反応のエピク
ロルヒドリンおよび反応で副生した塩素化合物の除去の
ために蒸留を行つても、得られる製品中に数千ppmの
エピクロルヒドリンおよび反応で副生した塩素化合物が
数%混入してくる。これらの混入は、作業者の健康阻
害、グル―プトランスフア―重合の触媒毒、電子・電気
分野で使用した際の金属の腐蝕などの問題を引き起こす
原因となり、製品の産業上の利用が制限される。Of these, the first and second methods using epichlorohydrin as a reaction raw material are known as the most general-purpose methods. According to these methods, unreacted epichlorohydrin and chlorine compounds by-produced in the reaction are used. Even if distillation is carried out for removal, several thousand ppm of epichlorohydrin and several% of chlorine compounds by-produced in the reaction are mixed in the obtained product. These contaminations cause problems such as health hazards for workers, catalyst poisons for group transfer polymerization, and corrosion of metals when used in the electronic and electrical fields, limiting the industrial use of products. .
【0005】この問題を克服するため、特開昭48−3
6117号公報には、第4級アンモニウム塩の存在下、
飽和または不飽和カルボン酸にエピクロルヒドリンを加
えて反応させ、さらにエピクロルヒドリンまたはアルキ
レンオキシドを加えて第1工程のエポキシ交換反応を行
い、第2工程として反応液を水酸化アルカリまたはアル
カリ土類金属の水酸化物とともに混合し、副生するエピ
クロルヒドリンを閉環除去し、再び第4級アンモニウム
塩の存在下に加熱反応させて2回目のエポキシ交換反応
を行い、さらに前記の第2工程を繰り返すことにより、
高純度のカルボン酸グリシジルを高収率で得る方法が開
示されている。In order to overcome this problem, Japanese Patent Laid-Open No. 48-3
6117, in the presence of a quaternary ammonium salt,
Epichlorohydrin is added to saturated or unsaturated carboxylic acid to react, and epichlorohydrin or alkylene oxide is further added to carry out the epoxy exchange reaction in the first step. In the second step, the reaction solution is treated with alkali hydroxide or alkaline earth metal hydroxide. By mixing with a substance, the by-produced epichlorohydrin is ring-closed and removed, and the mixture is heated and reacted again in the presence of a quaternary ammonium salt to carry out a second epoxy exchange reaction, and by further repeating the second step,
A method for obtaining high-purity glycidyl carboxylate in high yield is disclosed.
【0006】しかし、この方法では、第4級アンモニウ
ム塩が残つているため、蒸留時に重合物が発生して作業
性が悪くなり、しかも、グリセリンジメタクリレ―ト、
グリセリントリメタクリレ―トなどが生成し、蒸留ピツ
チが増加するという問題がある。また、特開昭48−7
2115号公報には、反応後の粗(メタ)アクリル酸グ
リシジルにスルホン酸塩を添加して重合を防止する方法
が開示されているが、反応で副生した塩素化合物の除去
は十分ではない。However, in this method, since the quaternary ammonium salt remains, a polymerized product is generated during distillation and workability is deteriorated, and moreover, glycerin dimethacrylate,
Glycerin trimethacrylate and the like are generated, and there is a problem that distillation pitch increases. In addition, JP-A-48-7
Japanese Patent No. 2115 discloses a method in which a sulfonate is added to crude glycidyl (meth) acrylate after the reaction to prevent polymerization, but removal of chlorine compounds by-produced in the reaction is not sufficient.
【0007】特開平4−187682号公報には、第4
級アンモニウム塩の存在下に酸素含有ガスでストリツピ
ングしたのち、蒸留を行う方法が開示されている。しか
し、この方法では、蒸留時に第4級アンモニウム塩が存
在するため、蒸留中に副生するエピクロルヒドリンの発
生を抑えることができず、また、第4級アンモニウム塩
の存在下で蒸留を行うと、重合物が発生して作業性が悪
くなり、さらに、グリセリンジメタクリレ―ト、グリセ
リントリメタクリレ―トなどが多く生成して、蒸留ピツ
チが増加するなどの問題がある。Japanese Unexamined Patent Publication No. 4-187682 discloses a fourth method.
A method of stripping with an oxygen-containing gas in the presence of a primary ammonium salt and then performing distillation is disclosed. However, in this method, since the quaternary ammonium salt is present during the distillation, it is not possible to suppress the generation of epichlorohydrin, which is a by-product during the distillation, and when the distillation is performed in the presence of the quaternary ammonium salt, There is a problem that the workability is deteriorated due to the generation of a polymer, and more glycerin dimethacrylate, glycerin trimethacrylate and the like are produced, and the distillation pitch increases.
【0008】[0008]
【発明が解決しようとする課題】本発明は、このような
従来技術の問題点に鑑み、エピクロルヒドリンを反応原
料として得られた粗(メタ)アクリル酸グリシジルか
ら、エピクロルヒドリンおよび反応で副生した塩素化合
物をほとんど含まない、したがつて、塩素濃度が低い、
高純度の(メタ)アクリル酸グリシジルを収率良く得る
ことができる新規な精製方法を提供することを目的とし
ている。DISCLOSURE OF THE INVENTION In view of the above problems of the prior art, the present invention provides epichlorohydrin and a chlorine compound by-produced in the reaction from crude glycidyl (meth) acrylate obtained using epichlorohydrin as a reaction raw material. It contains almost no chlorine and therefore has a low chlorine concentration,
It is an object of the present invention to provide a novel purification method by which highly purified glycidyl (meth) acrylate can be obtained in good yield.
【0009】[0009]
【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、鋭意検討した結果、エピクロルヒド
リンを反応原料として得られた粗(メタ)アクリル酸グ
リシジルに対し、アルカリ金属またはアルカリ土類金属
の塩基性化合物と第4級オニウム塩を加えてエピクロル
ヒドリンを留去したのち、さらにスルホン酸またはスル
ホン酸塩を加えてろ過または水洗し、その後に蒸留を行
うようにすると、粗(メタ)アクリル酸グリシジル中の
エピクロルヒドリンおよび反応で副生した塩素化合物が
ほぼ除去されて、塩素濃度の低い高純度の(メタ)アク
リル酸グリシジルが高収率で得られることを見い出し、
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 object, and as a result, as a result of using crude glycidyl (meth) acrylate obtained using epichlorohydrin as a reaction raw material, alkali metal or alkali After adding a basic compound of an earth metal and a quaternary onium salt and distilling off epichlorohydrin, further adding a sulfonic acid or a sulfonate and filtering or washing with water, followed by distillation, a crude (meta) is obtained. ) It was found that epichlorohydrin in glycidyl acrylate and chlorine compounds by-produced in the reaction were almost removed, and high-purity glycidyl (meth) acrylate having a low chlorine concentration was obtained in high yield.
The present invention has been completed.
【0010】本発明は、(メタ)アクリル酸またはその
アルカリ金属塩とエピクロルヒドリンを第4級オニウム
塩の存在下で反応させて得られた粗(メタ)アクリル酸
グリシジルに、粗(メタ)アクリル酸グリシジルに対し
0.1〜20重量%のアルカリ金属またはアルカリ土類
金属の塩基性化合物と粗(メタ)アクリル酸グリシジル
に対し0.01〜5重量%の第4級オニウム塩を加え
て、エピクロルヒドリンを留去し、ついで第4級オニウ
ム塩に対し0.5〜10倍モルのスルホン酸またはスル
ホン酸塩を加えて、ろ過または水洗し、さらに蒸留を行
うことを特徴とする(メタ)アクリル酸グリシジルの精
製方法に係るものである。The present invention relates to a crude glycidyl (meth) acrylate obtained by reacting (meth) acrylic acid or an alkali metal salt thereof with epichlorohydrin in the presence of a quaternary onium salt. 0.1 to 20% by weight of a basic compound of an alkali metal or alkaline earth metal with respect to glycidyl and 0.01 to 5% by weight of a quaternary onium salt with respect to crude glycidyl (meth) acrylate are added to form epichlorohydrin. Is distilled off, and then 0.5 to 10 times mol of sulfonic acid or sulfonate is added to the quaternary onium salt, followed by filtration or washing with water, and further performing distillation (meth) acrylic acid. The present invention relates to a method for purifying glycidyl.
【0011】[0011]
【発明の実施の形態】本発明において精製の対象となる
粗(メタ)アクリル酸グリシジルとしては、(1)(メ
タ)アクリル酸とエピクロルヒドリンを第4級オニウム
塩の存在下で反応させたのち、アルカリ金属またはアル
カリ土類金属の塩基性化合物と反応して得られた反応混
合物から、副生する塩をろ別、水洗などにより除去した
もの、(2)(メタ)アクリル酸のアルカリ金属塩とエ
ピクロルヒドリンを第4級オニウム塩の存在下で反応し
て得られた反応混合物から、副生する塩をろ別、水洗な
どにより除去したもの、(3)上記(1),(2)の粗
(メタ)アクリル酸グリシジルよりエピクロルヒドリン
を除去したもの、(4)上記(3)の粗(メタ)アクリ
ル酸グリシジルを蒸留したものなどが挙げられる。BEST MODE FOR CARRYING OUT THE INVENTION As crude glycidyl acrylate to be purified in the present invention, (1) (meth) acrylic acid and epichlorohydrin are reacted in the presence of a quaternary onium salt, A reaction mixture obtained by reacting with a basic compound of an alkali metal or an alkaline earth metal, from which a by-product salt is removed by filtration, washing with water, etc. (2) An alkali metal salt of (meth) acrylic acid A reaction mixture obtained by reacting epichlorohydrin in the presence of a quaternary onium salt, and removing a salt produced as a by-product by filtration, washing with water, or the like, (3) The crude (1) or (2) above. Examples thereof include those obtained by removing epichlorohydrin from glycidyl (meth) acrylate and (4) those obtained by distilling crude glycidyl (meth) acrylate of (3) above.
【0012】本発明の精製方法に用いられるアルカリ金
属またはアルカリ土類金属の塩基性化合物としては、ア
ルカリ金属もしくはアルカリ土類金属の水酸化物、酸化
物、炭酸塩または燐酸塩などがあり、たとえば、水酸化
ナトリウム、水酸化カリウム、水酸化リチウム、水酸化
マグネシウム、水酸化カルシウム、水酸化バリウム、酸
化マグネシウム、酸化カルシウム、炭酸ナトリウム、炭
酸カルシウム、燐酸ナトリウム、燐酸カリウムなどが挙
げられる。これらの塩基性化合物は、固形物、粉末また
は水溶液として使用することができる。The alkali metal or alkaline earth metal basic compound used in the purification method of the present invention includes alkali metal or alkaline earth metal hydroxides, oxides, carbonates or phosphates. , Sodium hydroxide, potassium hydroxide, lithium hydroxide, magnesium hydroxide, calcium hydroxide, barium hydroxide, magnesium oxide, calcium oxide, sodium carbonate, calcium carbonate, sodium phosphate, potassium phosphate and the like. These basic compounds can be used as solids, powders or aqueous solutions.
【0013】これらの塩基性化合物は、1種を単独でま
たは2種以上を組み合わせて使用してもよい。使用量と
しては、粗(メタ)アクリル酸グリシジルに対し、0.
1〜20重量%、好ましくは0.5〜10重量%であ
る。0.1重量%未満では塩素濃度を低くする効果が小
さく、20重量%を超えると副反応のため収率が低下す
るばかりでなく、経済性の面からも好ましくない。These basic compounds may be used alone or in combination of two or more. The amount of use is 0. 1 with respect to the crude glycidyl (meth) acrylate.
It is 1 to 20% by weight, preferably 0.5 to 10% by weight. If it is less than 0.1% by weight, the effect of lowering the chlorine concentration is small, and if it exceeds 20% by weight, not only the yield is lowered due to a side reaction, but it is also not economically preferable.
【0014】本発明の精製方法に用いられる第4級オニ
ウム塩としては、テトラメチルアンモニウムクロライ
ド、テトラエチルアンモニウムクロライド、テトラブチ
ルアンモニウムクロライド、トリメチルエチルアンモニ
ウムクロライド、トリメチルベンジルアンモニウムクロ
ライド、トリエチルメチルアンモニウムクロライド、ト
リエチルベンジルアンモニウムクロライド、テトラメチ
ルアンモニウムブロマイド、テトラエチルアンモニウム
ブロマイド、テトラメチルアンモニウムヨ―ダイド、テ
トラエチルアンモニウムヨ―ダイド、テトラメチルホス
ホニウムクロライド、テトラエチルホスホニウムクロラ
イド、テトラブチルホスホニウムクロライド、トリメチ
ルエチルホスホニウムクロライド、トリメチルベンジル
ホスホニウムクロライド、トリエチルメチルホスホニウ
ムクロライド、トリエチルベンジルホスホニウムクロラ
イド、テトラメチルホスホニウムブロマイド、テトラエ
チルホスホニウムブロマイド、テトラメチルホスホニウ
ムヨ―ダイド、テトラエチルホスホニウムヨ―ダイドな
どが挙げられる。Examples of the quaternary onium salt used in the purification method of the present invention include tetramethylammonium chloride, tetraethylammonium chloride, tetrabutylammonium chloride, trimethylethylammonium chloride, trimethylbenzylammonium chloride, triethylmethylammonium chloride and triethylbenzyl. Ammonium chloride, tetramethylammonium bromide, tetraethylammonium bromide, tetramethylammonium iodide, tetraethylammonium iodide, tetramethylphosphonium chloride, tetraethylphosphonium chloride, tetrabutylphosphonium chloride, trimethylethylphosphonium chloride, trimethylbenzylphosphonium chloride De, triethyl methyl phosphonium chloride, triethylbenzylammonium phosphonium chloride, tetramethyl phosphonium bromide, tetraethyl phosphonium bromide, tetramethyl phosphonium Yo - iodide, tetraethyl phosphonium Yo - iodide and the like.
【0015】これらの第4級オニウム塩は、1種を単独
でまたは2種以上を組み合わせて使用ししてもよい。使
用量としては、粗(メタ)アクリル酸グリシジルに対し
て、0.01〜5重量%、好ましくは0.05〜1重量
%である。0.01重量%未満では塩素濃度を低くする
効果が小さく、5重量%を超えると副反応のため収率が
低下するばかりでなく、経済性の面からも好ましくな
い。These quaternary onium salts may be used alone or in combination of two or more. The amount used is 0.01 to 5% by weight, preferably 0.05 to 1% by weight, based on the crude glycidyl (meth) acrylate. If it is less than 0.01% by weight, the effect of lowering the chlorine concentration is small, and if it exceeds 5% by weight, not only the yield is lowered due to a side reaction, but it is also not economically preferable.
【0016】本発明の精製方法においては、まず、前記
の粗(メタ)アクリル酸グリシジルに、上記の塩基性化
合物と第4級オニウム塩を上記割合で加えて、粗(メ
タ)アクリル酸グリシジル中に含まれるエピクロルヒド
リンを留去する。その際、水との共沸留去が効果的であ
り、また重合禁止の目的で空気を導入しながら行うのが
望ましい。処理時間は、粗(メタ)アクリル酸グリシジ
ルが前記(1)〜(4)のいずれであるかを勘案した上
で、処理温度、減圧度、空気吹き込み量などの処理条件
に応じて、適宜設定することができる。In the purification method of the present invention, first, the above-mentioned basic compound and quaternary onium salt are added to the above-mentioned crude glycidyl (meth) acrylate in the above-mentioned proportions to prepare the crude glycidyl (meth) acrylate. The epichlorohydrin contained in is distilled off. At that time, azeotropic distillation with water is effective, and it is desirable to carry out while introducing air for the purpose of inhibiting polymerization. The treatment time is appropriately set according to the treatment conditions such as the treatment temperature, the degree of pressure reduction, and the amount of air blown in consideration of which of the above (1) to (4) the crude (meth) acrylate glycidyl is. can do.
【0017】本発明においては、上記のエピクロルヒド
リンの留去後、さらにスルホン酸またはスルホン酸塩を
加えて、通常20〜70℃で20〜60分間の撹拌処理
を行つたのち、ろ過または水洗する。ろ過は、反応によ
り生成した塩および未反応のアルカリ金属またはアルカ
リ土類金属の塩基性化合物を、常圧ろ過、減圧ろ過、加
圧ろ過などにより除去するものである。また、水洗は、
反応により生成した塩および未反応のアルカリ金属また
はアルカリ土類金属の塩基性化合物を水に溶解させ、分
離した水層を除去するものである。In the present invention, after the above-mentioned epichlorohydrin is distilled off, sulfonic acid or sulfonate is further added, and the mixture is usually stirred at 20 to 70 ° C. for 20 to 60 minutes and then filtered or washed with water. The filtration removes the salt produced by the reaction and the unreacted basic compound of alkali metal or alkaline earth metal by atmospheric filtration, reduced pressure filtration, pressure filtration or the like. Also, washing with water
The salt produced by the reaction and the unreacted basic compound of alkali metal or alkaline earth metal are dissolved in water to remove the separated aqueous layer.
【0018】ここで用いられるスルホン酸またはスルホ
ン酸塩としては、メタンスルホン酸、ラウリルスルホン
酸、パラトルエンスルホン酸、ドデシルベンゼンスルホ
ン酸、ベンゼンスルホン酸、ポリオキシエチレンステア
リルサルフエ―トなどのスルホン酸や、メタンスルホン
酸ナトリウム、ラウリルスルホン酸ナトリウム、パラト
ルエンスルホン酸ナトリウム、ベンゼンスルホン酸ナト
リウム、ポリオキシステアリルサルフエ―トソ―ダなど
のスルホン酸塩が挙げられる。Examples of the sulfonic acid or sulfonate used here include methanesulfonic acid, laurylsulfonic acid, paratoluenesulfonic acid, dodecylbenzenesulfonic acid, benzenesulfonic acid, polyoxyethylene stearyl sulfate, and the like. And sulfonates such as sodium methanesulfonate, sodium laurylsulfonate, sodium paratoluenesulfonate, sodium benzenesulfonate, and polyoxystearyl sulphate soda.
【0019】これらのスルホン酸またはスルホン酸塩
は、1種を単独でまたは2種以上を組み合わせて使用し
てもよい。使用量としては、第4級オニウム塩に対し、
0.5〜10倍モル、好ましくは1〜5倍モルである。
0.5倍モル未満では重合物が生じて収率が低下しやす
く、10倍モルを超えて使用しても収率は変わらず、経
済性の面からも好ましくない。These sulfonic acids or sulfonates may be used alone or in combination of two or more. The amount used is based on the quaternary onium salt,
The amount is 0.5 to 10 times mol, preferably 1 to 5 times mol.
If it is less than 0.5 times by mole, a polymer is likely to be generated and the yield tends to be lowered. Even if it is used in excess of 10 times by mole, the yield does not change, which is not preferable from the economical aspect.
【0020】本発明において、このようにスルホン酸ま
たはスルホン酸塩を加えてろ過または水洗したのち、蒸
留することにより、塩素濃度の低い高純度の(メタ)ア
クリル酸グリシジルを高収率で得ることができる。粗
(メタ)アクリル酸グリシジルの種類により異なるが、
一般に、エピクロルヒドリンの量は0.002重量%以
下、塩素含量は1,000ppm以下、好ましくは50
0ppm以下に抑えることができ、純度99重量%以上
の(メタ)アクリル酸グリシジルを75重量%以上、好
ましくは80重量%前後の高い収率で得ることが可能で
ある。According to the present invention, high purity glycidyl (meth) acrylate having a low chlorine concentration can be obtained in a high yield by adding sulfonic acid or sulfonic acid salt, filtering or washing with water and then distilling. You can Depending on the type of crude (meth) acrylic acid glycidyl,
Generally, the amount of epichlorohydrin is 0.002% by weight or less and the chlorine content is 1,000 ppm or less, preferably 50%.
It can be suppressed to 0 ppm or less, and glycidyl (meth) acrylate having a purity of 99% by weight or more can be obtained in a high yield of 75% by weight or more, preferably around 80% by weight.
【0021】[0021]
【実施例】以下に、実施例および比較例により、本発明
を具体的に説明する。なお、実施例および比較例で使用
した粗(メタ)アクリル酸グリシジルA〜Eは、以下の
調製方法1〜5により得られたものである。EXAMPLES The present invention will be specifically described below with reference to Examples and Comparative Examples. The crude glycidyl (meth) acrylates A to E used in Examples and Comparative Examples were obtained by the following preparation methods 1 to 5.
【0022】<調製方法1>メタクリル酸とエピクロル
ヒドリン(対メタクリル酸6倍モル)を撹拌機、温度
計、還流冷却管を付したフラスコに仕込んだ。ついで、
テトラメチルアンモニウムクロライド(対メタクリル酸
3モル%)、フエノチアジン(総仕込量の0.02重量
%)を加え、90℃で5時間保つた。つぎに、90℃、
200mmHgで空気を吹き込みながら、50重量%水酸化
ナトリウム水溶液(対メタクリル酸1倍モル)を6時間
にわたつて滴下した。滴下終了後、水(総仕込量の50
重量%)で水洗し、粗メタクリル酸グリシジルAを得
た。<Preparation Method 1> Methacrylic acid and epichlorohydrin (6 times mol of methacrylic acid) were placed in a flask equipped with a stirrer, a thermometer, and a reflux condenser. Then
Tetramethylammonium chloride (based on methacrylic acid 3 mol%) and phenothiazine (0.02 wt% of the total amount charged) were added, and the mixture was kept at 90 ° C for 5 hours. Next, 90 ℃,
While blowing air at 200 mmHg, a 50 wt% sodium hydroxide aqueous solution (to 1-fold mol of methacrylic acid) was added dropwise over 6 hours. After the dropping, water (50% of the total amount charged)
It was washed with water to obtain crude glycidyl methacrylate A.
【0023】<調製方法2>調製方法1で得られた粗メ
タクリル酸グリシジルAに対し、60℃、50mmHgで空
気と水(対粗メタクリル酸グリシジルA5重量%/時
間)を吹き込みながら、6時間にわたつて未反応のエピ
クロルヒドリンを減圧留去することにより、粗メタクリ
ル酸グリシジルBを得た。<Preparation Method 2> The crude glycidyl methacrylate A obtained in Preparation Method 1 was blown with air and water (vs. crude glycidyl methacrylate A 5% by weight / hour) at 60 ° C. and 50 mmHg for 6 hours. Unreacted epichlorohydrin was distilled off under reduced pressure to obtain crude glycidyl methacrylate B.
【0024】<調製方法3>調製方法1で得られた粗メ
タクリル酸グリシジルA(1,062g)に、60℃、
50mmHgで空気と50ml/時間の水を吹き込みながら、
12時間にわたつて未反応のエピクロルヒドリンを減圧
留去し、その後、蒸留を行うことにより、粗メタクリル
酸グリシジルCを得た。<Preparation Method 3> The crude glycidyl methacrylate A (1,062 g) obtained in Preparation Method 1 was treated at 60 ° C.
While blowing air and 50 ml / hour of water at 50 mmHg,
Unreacted epichlorohydrin was distilled off under reduced pressure for 12 hours, and then distilled to obtain crude glycidyl methacrylate C.
【0025】<調製方法4>メタクリル酸430.5g
(5モル)と水酸化ナトリウム200g(5モル)との
中和反応によりメタクリル酸ナトリウムを合成し、これ
を脱水して得たメタクリル酸ナトリウム540.5gと
エピクロルヒドリン2,775.9g(30モル)を撹
拌機、温度計、還流冷却管を付したフラスコに仕込ん
だ。ついで、トリエチルベンジルアンモニウムクロライ
ド24.0g(対メタクリル酸ナトリウム2モル%)、
フエノチアジン0.55gを加えて、90℃、200mm
Hgで空気を吹き込みながら5時間反応した。反応終了
後、1,500gの水で水洗したのち、60℃、50mm
Hgで空気と50ml/時間の水を吹き込みながら、6時間
にわたつて未反応のエピクロルヒドリンを減圧留去する
ことにより、粗メタクリル酸グリシジルDを得た。<Preparation Method 4> Methacrylic acid 430.5 g
(5 mol) and 200 g (5 mol) of sodium hydroxide were neutralized to synthesize sodium methacrylate, which was dehydrated to give 540.5 g of sodium methacrylate and epichlorohydrin 2,775.9 g (30 mol). Was charged into a flask equipped with a stirrer, a thermometer, and a reflux condenser. Then, 24.0 g of triethylbenzylammonium chloride (based on sodium methacrylate 2 mol%),
Add 0.55g of phenothiazine, 90 ℃, 200mm
The mixture was reacted for 5 hours while blowing air with Hg. After completion of the reaction, wash with 1,500 g of water and then 60 ℃, 50 mm
Crude glycidyl methacrylate D was obtained by distilling off unreacted epichlorohydrin under reduced pressure for 6 hours while blowing air and 50 ml / hour of water with Hg.
【0026】<調製方法5>調製方法1と同様の方法に
より、アクリル酸360.2g(5モル)、エピクロル
ヒドリン2,775.9g(30モル)、トリブチルベ
ンジルホスホニウムクロライド65.6g(0.20モ
ル、メタクリル酸に対して4モル%)、フエノチアジン
0.55g、50重量%水酸化ナトリウム480g(6
モル)を用いて、粗アクリル酸グリシジルEを得た。<Preparation Method 5> By the same method as in Preparation Method 1, 360.2 g (5 mol) of acrylic acid, 2,775.9 g (30 mol) of epichlorohydrin, and 65.6 g (0.20 mol of tributylbenzylphosphonium chloride). , Methacrylic acid (4 mol%), phenothiazine 0.55 g, 50% by weight sodium hydroxide 480 g (6
Mol) was used to obtain crude glycidyl acrylate E.
【0027】実施例1 粗メタクリル酸グリシジルA2,933gに、水酸化ナ
トリウム29.3g(対粗メタクリル酸グリシジルA
1.0重量%)とテトラメチルアンモニウムクロライド
1.5g(対粗メタクリル酸グリシジルA0.05重量
%)を加えて、60℃、50mmHgで空気と50ml/時間
の水を吹き込みながら、12時間にわたつて未反応のエ
ピクロルヒドリンを減圧留去した。ついで、パラトルエ
ンスルホン酸4.7g(対テトラメチルアンモニウムク
ロライド2倍モル)を加えて、60℃で20分間攪拌
後、水150gで水洗し、減圧下で脱水したのち、ろ過
した。最後に、蒸留を行い、精製メタクリル酸グリシジ
ルを得た。Example 1 2,933 g of crude glycidyl methacrylate A was added to 29.3 g of sodium hydroxide (vs. crude glycidyl methacrylate A).
1.0% by weight) and 1.5 g of tetramethylammonium chloride (0.05% by weight of crude glycidyl methacrylate A) were added, and the mixture was blown with air and 50 ml / hour of water at 60 ° C. and 50 mmHg for 12 hours. Then, unreacted epichlorohydrin was distilled off under reduced pressure. Then, 4.7 g of paratoluenesulfonic acid (2 times mol of tetramethylammonium chloride) was added, and the mixture was stirred at 60 ° C. for 20 minutes, washed with 150 g of water, dehydrated under reduced pressure, and then filtered. Finally, distillation was performed to obtain purified glycidyl methacrylate.
【0028】実施例2 粗メタクリル酸グリシジルB766gに、水酸化ナトリ
ウム38.3g(対粗メタクリル酸グリシジルB5重量
%)とテトラメチルアンモニウムクロライド3.8g
(対粗メタクリル酸グリシジルB0.5重量%)を加え
て、60℃、50mmHgで空気と50ml/時間の水を吹き
込みながら、6時間にわたつて未反応のエピクロルヒド
リンを減圧留去した。ついで、パラトルエンスルホン酸
7.6g(対テトラメチルアンモニウムクロライド2倍
モル)を加えて、40℃で30分間撹拌後、減圧下で脱
水したのち、ろ過した。最後に、蒸留を行い、精製メタ
クリル酸グリシジルを得た。Example 2 To 766 g of crude glycidyl methacrylate B was added 38.3 g of sodium hydroxide (5% by weight of crude glycidyl methacrylate B) and 3.8 g of tetramethylammonium chloride.
(0.5% by weight of crude glycidyl methacrylate B) was added, and unreacted epichlorohydrin was distilled off under reduced pressure over 6 hours while blowing air and 50 ml / hour of water at 60 ° C. and 50 mmHg. Then, 7.6 g of paratoluenesulfonic acid (2 times mol of tetramethylammonium chloride) was added, and the mixture was stirred at 40 ° C. for 30 minutes, dehydrated under reduced pressure, and then filtered. Finally, distillation was performed to obtain purified glycidyl methacrylate.
【0029】実施例3〜7 粗メタクリル酸グリシジルBに対し、後記の表1に記載
のアルカリ金属またはアルカリ土類金属の塩基性化合
物、第4級オニウム塩ならびにスルホン酸またはスルホ
ン酸塩を用いて、実施例2と同様の方法で精製処理し
て、精製メタクリル酸グリシジルを得た。なお、表1に
は、本実施例3〜7のほかに、前記の実施例1,2、後
記の実施例8〜10および比較例1〜5で用いた上記化
合物についても、その種類および量を併記した。Examples 3 to 7 Using a basic compound of an alkali metal or an alkaline earth metal, a quaternary onium salt, and a sulfonic acid or a sulfonate as shown in Table 1 below, with respect to the crude glycidyl methacrylate B. Purification treatment was performed in the same manner as in Example 2 to obtain purified glycidyl methacrylate. In addition to the present Examples 3 to 7, Table 1 also shows the types and amounts of the above-mentioned compounds used in Examples 1 and 2 and Examples 8 to 10 and Comparative Examples 1 to 5 described later. Was also written.
【0030】表1中の各符号は、下記のとおりである。 50%NaOH:50重量%水酸化ナトリウム水溶液 TMAC:テトラメチルアンモニウムクロライド TEBzAC:トリエチルベンジルアンモニウムクロラ
イド TBuBzPC:トリブチルベンジルホスホニウムクロ
ライド PTS:パラトルエンスルホン酸 PTSNa:パラトルエンスルホン酸ナトリウムThe symbols in Table 1 are as follows. 50% NaOH: 50% by weight aqueous sodium hydroxide solution TMAC: Tetramethylammonium chloride TEBzAC: Triethylbenzylammonium chloride TBuBzPC: Tributylbenzylphosphonium chloride PTS: Paratoluenesulfonic acid PTSNa: Sodium paratoluenesulfonate
【0031】実施例8 粗メタクリル酸グリシジルC530.3gに、表1に記
載の水酸化ナトリウムとトリエチルベンゼンアンモニウ
ムクロライドを加えて、60℃、50mmHgで空気と50
ml/時間の水を吹き込みながら、3時間にわたつて未反
応のエピクロルヒドリンを減圧留去した。ついで、パラ
トルエンスルホン酸ナトリウムを加えて、20℃で60
分間撹拌後、水220gで水洗し、減圧下で脱水したの
ち、ろ過した。最後に、蒸留を行い、精製メタクリル酸
グリシジルを得た。Example 8 To 530.3 g of crude glycidyl methacrylate C, sodium hydroxide and triethylbenzene ammonium chloride shown in Table 1 were added, and the mixture was mixed with air at 60 ° C. and 50 mmHg and 50%.
Unreacted epichlorohydrin was distilled off under reduced pressure over 3 hours while blowing water at a rate of ml / hour. Then add sodium paratoluene sulfonate and add 60 at 20 ° C.
After stirring for a minute, the mixture was washed with 220 g of water, dehydrated under reduced pressure, and filtered. Finally, distillation was performed to obtain purified glycidyl methacrylate.
【0032】実施例9 粗メタクリル酸グリシジルD748gに、表1に記載の
水酸化ナトリウムとテトラメチルアンモニウムクロライ
ドを加えて、実施例2と同様の方法によりエピクロルヒ
ドリンを減圧留去した。ついで、パラトルエンスルホン
酸を加え、70℃で20分間撹拌後、減圧下で脱水した
のち、ろ過した。最後に、蒸留を行い、精製メタクリル
酸グリシジルを得た。Example 9 Sodium hydroxide and tetramethylammonium chloride described in Table 1 were added to 748 g of crude glycidyl methacrylate D, and epichlorohydrin was distilled off under reduced pressure in the same manner as in Example 2. Then, paratoluenesulfonic acid was added, and the mixture was stirred at 70 ° C. for 20 minutes, dehydrated under reduced pressure, and then filtered. Finally, distillation was performed to obtain purified glycidyl methacrylate.
【0033】実施例10 粗アクリル酸グリシジルE2,864gに、表1に記載
の50重量%水酸化ナトリウム水溶液とテトラメチルア
ンモニウムクロライドを加えて、実施例1と同様の方法
によりエピクロルヒドリンを減圧留去した。ついで、パ
ラトルエンスルホン酸ナトリウムを加えて、40℃で6
0分間撹拌後、減圧下で脱水したのち、ろ過した。最後
に、蒸留を行い、精製メタクリル酸グリシジルを得た。Example 10 To 2,864 g of crude glycidyl acrylate E was added 50% by weight aqueous sodium hydroxide solution and tetramethylammonium chloride shown in Table 1, and epichlorohydrin was distilled off under reduced pressure in the same manner as in Example 1. . Then add sodium paratoluenesulfonate and add 6 at 40 ° C.
After stirring for 0 minutes, the mixture was dehydrated under reduced pressure and then filtered. Finally, distillation was performed to obtain purified glycidyl methacrylate.
【0034】比較例1 粗メタクリル酸グリシジルB766gに、60℃で、5
0mmHgで空気と50ml/時間の水を吹き込みながら、6
時間にわたつて未反応のエピクロルヒドリンを減圧留去
した。ついで、減圧下で脱水したのち、ろ過した。最後
に、蒸留を行い、精製メタクリル酸グリシジルを得た。Comparative Example 1 766 g of crude glycidyl methacrylate B was added at 60 ° C. to 5
While blowing air and 50 ml / hour of water at 0 mmHg, 6
Unreacted epichlorohydrin was distilled off under reduced pressure over time. Then, it was dehydrated under reduced pressure and then filtered. Finally, distillation was performed to obtain purified glycidyl methacrylate.
【0035】比較例2 粗メタクリル酸グリシジルB766gに、表1に記載の
水酸化ナトリウムを加えて、60℃、50mmHgで空気と
50ml/時間の水を吹き込みながら、6時間にわたつて
未反応のエピクロルヒドリンを減圧留去した。減圧下で
脱水したのち、ろ過した。最後に、蒸留を行い、精製メ
タクリル酸グリシジルを得た。Comparative Example 2 To 766 g of crude glycidyl methacrylate B was added the sodium hydroxide shown in Table 1, and air and 50 ml / hour of water were blown at 60 ° C. and 50 mmHg for 6 hours while unreacted epichlorohydrin was added. Was distilled off under reduced pressure. After dehydration under reduced pressure, it was filtered. Finally, distillation was performed to obtain purified glycidyl methacrylate.
【0036】比較例3 粗メタクリル酸グリシジルB766gに、表1に記載の
トリブチルベンジルホスホニウムクロライドを加えて、
60℃、50mmHgで空気と50ml/時間の水を吹き込み
ながら、6時間にわたり未反応のエピクロルヒドリンを
減圧留去した。ついで、減圧下で脱水したのち、ろ過し
た。最後に、蒸留を行うことにより、精製メタクリル酸
グリシジルを得た。Comparative Example 3 To 766 g of crude glycidyl methacrylate B was added tributylbenzylphosphonium chloride shown in Table 1,
Unreacted epichlorohydrin was distilled off under reduced pressure for 6 hours while blowing air and 50 ml / hour of water at 60 ° C. and 50 mmHg. Then, it was dehydrated under reduced pressure and then filtered. Finally, distillation was performed to obtain purified glycidyl methacrylate.
【0037】比較例4 粗メタクリル酸グリシジルB766gに、60℃、50
mmHgで空気と50ml/時間の水を吹き込みながら、表1
に記載のパラトルエンスルホン酸を加えて、6時間にわ
たり未反応のエピクロルヒドリンを減圧留去した。最後
に、蒸留を行い、精製メタクリル酸グリシジルを得た。Comparative Example 4 766 g of crude glycidyl methacrylate B was added at 60 ° C. and 50
While blowing air and 50 ml / hour of water with mmHg,
Paratoluenesulfonic acid described in 1) was added, and unreacted epichlorohydrin was distilled off under reduced pressure for 6 hours. Finally, distillation was performed to obtain purified glycidyl methacrylate.
【0038】比較例5 粗メタクリル酸グリシジルB766gに、表1に記載の
水酸化ナトリウムとトリブチルベンジルホスホニウムク
ロライドを加えて、60℃、50mmHgで空気と50ml/
時間の水を吹き込みながら、6時間にわたつて未反応の
エピクロルヒドリンを減圧留去した。ついで、減圧下で
脱水したのち、ろ過した。最後に、蒸留を行い、精製メ
タクリル酸グリシジルを得た。Comparative Example 5 Sodium hydroxide and tributylbenzylphosphonium chloride shown in Table 1 were added to 766 g of crude glycidyl methacrylate B, and 50 ml / air of air was added at 60 ° C. and 50 mmHg.
The unreacted epichlorohydrin was distilled off under reduced pressure over 6 hours while blowing water for a period of time. Then, it was dehydrated under reduced pressure and then filtered. Finally, distillation was performed to obtain purified glycidyl methacrylate.
【0039】以上の実施例1〜10および比較例1〜5
で得た精製(メタ)アクリル酸グリシジルについて、そ
の収率と、蒸留時の初留カツト分およびピツチ(蒸留残
渣)の収率を、後記の表2に示した。また、精製(メ
タ)アクリル酸グリシジルの純度、エピクロルヒドリン
の濃度および塩素濃度を調べ、表2に示した。純度とエ
ピクロルヒドリンの濃度は下記のガスクロマトグラフイ
―分析で測定し、塩素濃度はアルカリ水溶液で処理した
のち硝酸銀で滴定する方法で測定した。表2中、エピク
ロルヒドリンの濃度の欄における「ND」は、上記分析
で検知できなかつた(0.002重量%以下であつた)
ことを示している。The above Examples 1 to 10 and Comparative Examples 1 to 5
The yields of the purified (meth) acrylic acid glycidyl obtained in 1. and the yields of the initial cut fraction and the pitch (distillation residue) at the time of distillation are shown in Table 2 below. Further, the purity of purified glycidyl (meth) acrylate, the concentration of epichlorohydrin and the concentration of chlorine were examined, and shown in Table 2. The purity and the concentration of epichlorohydrin were measured by the following gas chromatography analysis, and the chlorine concentration was measured by a method of treating with an alkaline aqueous solution and then titrating with silver nitrate. In Table 2, "ND" in the column of the concentration of epichlorohydrin could not be detected by the above analysis (it was 0.002% by weight or less).
It is shown that.
【0040】 <ガスクロマトグラフイ―分析> 機種:(株)島津製作所製の「GC14−A」 測定条件:カラム;PEG−HT5%、内径3mm、長さ2m 注入温度;280℃ カラム温度;80〜260℃、7.5℃/分の昇温速度<Gas Chromatography-Analysis> Model: “GC14-A” manufactured by Shimadzu Corporation Measurement conditions: column; PEG-HT 5%, inner diameter 3 mm, length 2 m Injection temperature; 280 ° C. Column temperature; 80- 260 ° C, temperature rising rate of 7.5 ° C / min
【0041】 (注)※1:対粗(メタ)アクリル酸グリシジル(単位:重量%) ※2:対粗(メタ)アクリル酸グリシジル(単位:重量%) ※3:対第4級オニウム塩(単位:倍モル)[0041] (Note) * 1: To crude glycidyl acrylate (unit: wt%) * 2: To crude glycidyl acrylate (unit: wt%) * 3: To quaternary onium salt (unit: double) Mol)
【0042】 (注)※4,5:収率は重量を蒸留前の重量で除した百分率である ※6:収率は重量を蒸留前の重量で除した百分率であり、ECH濃度は 製品中のエピクロルヒドリンの濃度であり、塩素濃度は製品中の 塩素の濃度である[0042] (Note) * 4, 5: Yield is the percentage obtained by dividing the weight by the weight before distillation. * 6: Yield is the percentage obtained by dividing the weight by the weight before distillation. The ECH concentration is the percentage of epichlorohydrin in the product. Concentration, chlorine concentration is the concentration of chlorine in the product
【0043】上記の表2の結果から明らかなように、本
発明の実施例1〜10の精製方法では、蒸留時の初留カ
ツト分が約6重量%以下、ピツチ(蒸留残渣)が約17
重量%以下で、約77重量%以上の高い収率が得られて
おり、しかも、この製品(メタ)アクリル酸グリシジル
にはエピクロルヒドリンがほとんど含まれておらず、塩
素濃度は約350ppm以下の低い値を示しており、9
9重量%以上の高純度の(メタ)アクリル酸グリシジル
が得られていることがわかる。これに対して、比較例1
〜5の精製方法では、収率および純度ともに、本発明の
実施例1〜10の方法に比べて、大分劣つていることが
明らかである。As is clear from the results of Table 2 above, in the purification methods of Examples 1 to 10 of the present invention, the initial cut content during distillation was about 6% by weight or less, and the pitch (distillation residue) was about 17%.
A high yield of about 77% by weight or less was obtained at a weight% or less, and moreover, this product glycidyl (meth) acrylate contained almost no epichlorohydrin, and the chlorine concentration was a low value of about 350 ppm or less. Shows 9
It can be seen that 9% by weight or more of high-purity glycidyl (meth) acrylate was obtained. On the other hand, Comparative Example 1
It is apparent that the purification methods of ~ 5 are much inferior to the methods of Examples 1 to 10 of the present invention in yield and purity.
【0044】[0044]
【発明の効果】以上のように、本発明の精製方法によれ
ば、エピクロルヒドリンを反応原料として得られた粗
(メタ)アクリル酸グリシジルから、エピクロルヒドリ
ンおよび反応で副生した塩素化合物をほとんど含まな
い、したがつて、塩素濃度が低い、高純度の(メタ)ア
クリル酸グリシジルを高収率で得ることができる。As described above, according to the purification method of the present invention, from crude glycidyl (meth) acrylate obtained using epichlorohydrin as a reaction raw material, epichlorohydrin and chlorine compounds by-produced in the reaction are scarcely contained. Therefore, highly pure glycidyl (meth) acrylate having a low chlorine concentration can be obtained in a high yield.
Claims (1)
金属塩とエピクロルヒドリンを第4級オニウム塩の存在
下で反応させて得られた粗(メタ)アクリル酸グリシジ
ルに、粗(メタ)アクリル酸グリシジルに対し0.1〜
20重量%のアルカリ金属またはアルカリ土類金属の塩
基性化合物と粗(メタ)アクリル酸グリシジルに対し
0.01〜5重量%の第4級オニウム塩を加えて、エピ
クロルヒドリンを留去し、ついで第4級オニウム塩に対
し0.5〜10倍モルのスルホン酸またはスルホン酸塩
を加えて、ろ過または水洗し、さらに蒸留を行うことを
特徴とする(メタ)アクリル酸グリシジルの精製方法。1. A crude glycidyl (meth) acrylate obtained by reacting (meth) acrylic acid or an alkali metal salt thereof with epichlorohydrin in the presence of a quaternary onium salt to give a crude glycidyl (meth) acrylate. To 0.1
0.01 to 5% by weight of a quaternary onium salt is added to 20% by weight of a basic compound of an alkali metal or an alkaline earth metal and crude glycidyl (meth) acrylate, and epichlorohydrin is distilled off. A method for purifying glycidyl (meth) acrylate, which comprises adding 0.5 to 10 moles of a sulfonic acid or a sulfonate to a quaternary onium salt, filtering or washing with water, and further performing distillation.
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JP05560896A JP3885249B2 (en) | 1996-03-13 | 1996-03-13 | Purification method of glycidyl (meth) acrylate |
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JPH09249657A true JPH09249657A (en) | 1997-09-22 |
JP3885249B2 JP3885249B2 (en) | 2007-02-21 |
Family
ID=13003492
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Cited By (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2006143629A (en) * | 2004-11-18 | 2006-06-08 | Mitsubishi Gas Chem Co Inc | Method for preparing glycidyl methacrylate |
JP2006193449A (en) * | 2005-01-12 | 2006-07-27 | Mitsubishi Gas Chem Co Inc | Purification method of glycidyl methacrylate |
JP2010126453A (en) * | 2008-11-25 | 2010-06-10 | Nippon Shokubai Co Ltd | Method for producing epoxy group-containing acrylic esters |
JP2011184373A (en) * | 2010-03-09 | 2011-09-22 | Nippon Shokubai Co Ltd | Method for producing glycidyl acrylate |
WO2022158463A1 (en) * | 2021-01-20 | 2022-07-28 | 三菱瓦斯化学株式会社 | Glycidyl (meth)acrylate composition |
-
1996
- 1996-03-13 JP JP05560896A patent/JP3885249B2/en not_active Expired - Fee Related
Cited By (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2006143629A (en) * | 2004-11-18 | 2006-06-08 | Mitsubishi Gas Chem Co Inc | Method for preparing glycidyl methacrylate |
JP2006193449A (en) * | 2005-01-12 | 2006-07-27 | Mitsubishi Gas Chem Co Inc | Purification method of glycidyl methacrylate |
JP2010126453A (en) * | 2008-11-25 | 2010-06-10 | Nippon Shokubai Co Ltd | Method for producing epoxy group-containing acrylic esters |
JP2011184373A (en) * | 2010-03-09 | 2011-09-22 | Nippon Shokubai Co Ltd | Method for producing glycidyl acrylate |
WO2022158463A1 (en) * | 2021-01-20 | 2022-07-28 | 三菱瓦斯化学株式会社 | Glycidyl (meth)acrylate composition |
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Publication number | Publication date |
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JP3885249B2 (en) | 2007-02-21 |
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