JPH0248559A - Production of unsaturated carboxylic acid amide - Google Patents
Production of unsaturated carboxylic acid amideInfo
- Publication number
- JPH0248559A JPH0248559A JP63198052A JP19805288A JPH0248559A JP H0248559 A JPH0248559 A JP H0248559A JP 63198052 A JP63198052 A JP 63198052A JP 19805288 A JP19805288 A JP 19805288A JP H0248559 A JPH0248559 A JP H0248559A
- Authority
- JP
- Japan
- Prior art keywords
- hydroxide
- carboxylic acid
- formula
- basic catalyst
- reaction
- 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
- 150000001732 carboxylic acid derivatives Chemical class 0.000 title claims abstract description 10
- 238000004519 manufacturing process Methods 0.000 title claims description 3
- 239000003054 catalyst Substances 0.000 claims abstract description 24
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 claims abstract description 21
- WMFOQBRAJBCJND-UHFFFAOYSA-M Lithium hydroxide Chemical compound [Li+].[OH-] WMFOQBRAJBCJND-UHFFFAOYSA-M 0.000 claims abstract description 12
- 238000000034 method Methods 0.000 claims abstract description 12
- 150000001733 carboxylic acid esters Chemical class 0.000 claims abstract description 11
- HEMHJVSKTPXQMS-UHFFFAOYSA-M Sodium hydroxide Chemical compound [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 claims abstract description 9
- 125000000217 alkyl group Chemical group 0.000 claims abstract description 6
- 239000000126 substance Substances 0.000 claims abstract description 5
- 125000002496 methyl group Chemical group [H]C([H])([H])* 0.000 claims abstract description 3
- 125000000467 secondary amino group Chemical class [H]N([*:1])[*:2] 0.000 claims abstract 3
- KWYUFKZDYYNOTN-UHFFFAOYSA-M Potassium hydroxide Chemical group [OH-].[K+] KWYUFKZDYYNOTN-UHFFFAOYSA-M 0.000 claims description 6
- CDBYLPFSWZWCQE-UHFFFAOYSA-L Sodium Carbonate Chemical group [Na+].[Na+].[O-]C([O-])=O CDBYLPFSWZWCQE-UHFFFAOYSA-L 0.000 claims description 4
- WQDUMFSSJAZKTM-UHFFFAOYSA-N Sodium methoxide Chemical group [Na+].[O-]C WQDUMFSSJAZKTM-UHFFFAOYSA-N 0.000 claims description 4
- QVQLCTNNEUAWMS-UHFFFAOYSA-N barium oxide Chemical compound [Ba]=O QVQLCTNNEUAWMS-UHFFFAOYSA-N 0.000 claims description 4
- 125000004432 carbon atom Chemical group C* 0.000 claims description 4
- BWHMMNNQKKPAPP-UHFFFAOYSA-L potassium carbonate Chemical compound [K+].[K+].[O-]C([O-])=O BWHMMNNQKKPAPP-UHFFFAOYSA-L 0.000 claims description 4
- CPRMKOQKXYSDML-UHFFFAOYSA-M rubidium hydroxide Chemical compound [OH-].[Rb+] CPRMKOQKXYSDML-UHFFFAOYSA-M 0.000 claims description 4
- 229910052783 alkali metal Inorganic materials 0.000 claims description 3
- 229910000288 alkali metal carbonate Inorganic materials 0.000 claims description 3
- 150000008041 alkali metal carbonates Chemical class 0.000 claims description 3
- 150000008044 alkali metal hydroxides Chemical class 0.000 claims description 3
- 150000001340 alkali metals Chemical group 0.000 claims description 3
- 229910001860 alkaline earth metal hydroxide Inorganic materials 0.000 claims description 3
- 229910000287 alkaline earth metal oxide Inorganic materials 0.000 claims description 3
- AXCZMVOFGPJBDE-UHFFFAOYSA-L calcium dihydroxide Chemical compound [OH-].[OH-].[Ca+2] AXCZMVOFGPJBDE-UHFFFAOYSA-L 0.000 claims description 3
- 239000000920 calcium hydroxide Substances 0.000 claims description 3
- 229910001861 calcium hydroxide Inorganic materials 0.000 claims description 3
- MFGOFGRYDNHJTA-UHFFFAOYSA-N 2-amino-1-(2-fluorophenyl)ethanol Chemical compound NCC(O)C1=CC=CC=C1F MFGOFGRYDNHJTA-UHFFFAOYSA-N 0.000 claims description 2
- GHVZOJONCUEWAV-UHFFFAOYSA-N [K].CCO Chemical compound [K].CCO GHVZOJONCUEWAV-UHFFFAOYSA-N 0.000 claims description 2
- RQPZNWPYLFFXCP-UHFFFAOYSA-L barium dihydroxide Chemical compound [OH-].[OH-].[Ba+2] RQPZNWPYLFFXCP-UHFFFAOYSA-L 0.000 claims description 2
- 229910001863 barium hydroxide Inorganic materials 0.000 claims description 2
- HUCVOHYBFXVBRW-UHFFFAOYSA-M caesium hydroxide Inorganic materials [OH-].[Cs+] HUCVOHYBFXVBRW-UHFFFAOYSA-M 0.000 claims description 2
- BRPQOXSCLDDYGP-UHFFFAOYSA-N calcium oxide Chemical compound [O-2].[Ca+2] BRPQOXSCLDDYGP-UHFFFAOYSA-N 0.000 claims description 2
- 239000000292 calcium oxide Substances 0.000 claims description 2
- ODINCKMPIJJUCX-UHFFFAOYSA-N calcium oxide Inorganic materials [Ca]=O ODINCKMPIJJUCX-UHFFFAOYSA-N 0.000 claims description 2
- 229910052739 hydrogen Inorganic materials 0.000 claims description 2
- 239000001257 hydrogen Substances 0.000 claims description 2
- VTHJTEIRLNZDEV-UHFFFAOYSA-L magnesium dihydroxide Chemical group [OH-].[OH-].[Mg+2] VTHJTEIRLNZDEV-UHFFFAOYSA-L 0.000 claims description 2
- 239000000347 magnesium hydroxide Substances 0.000 claims description 2
- 229910001862 magnesium hydroxide Inorganic materials 0.000 claims description 2
- 239000000395 magnesium oxide Substances 0.000 claims description 2
- CPLXHLVBOLITMK-UHFFFAOYSA-N magnesium oxide Inorganic materials [Mg]=O CPLXHLVBOLITMK-UHFFFAOYSA-N 0.000 claims description 2
- AXZKOIWUVFPNLO-UHFFFAOYSA-N magnesium;oxygen(2-) Chemical compound [O-2].[Mg+2] AXZKOIWUVFPNLO-UHFFFAOYSA-N 0.000 claims description 2
- 229910000027 potassium carbonate Inorganic materials 0.000 claims description 2
- BDAWXSQJJCIFIK-UHFFFAOYSA-N potassium methoxide Chemical compound [K+].[O-]C BDAWXSQJJCIFIK-UHFFFAOYSA-N 0.000 claims description 2
- 229910000029 sodium carbonate Inorganic materials 0.000 claims description 2
- QDRKDTQENPPHOJ-UHFFFAOYSA-N sodium ethoxide Chemical compound [Na+].CC[O-] QDRKDTQENPPHOJ-UHFFFAOYSA-N 0.000 claims description 2
- UUCCCPNEFXQJEL-UHFFFAOYSA-L strontium dihydroxide Chemical compound [OH-].[OH-].[Sr+2] UUCCCPNEFXQJEL-UHFFFAOYSA-L 0.000 claims description 2
- 229910001866 strontium hydroxide Inorganic materials 0.000 claims description 2
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 claims 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-M hydroxide Chemical compound [OH-] XLYOFNOQVPJJNP-UHFFFAOYSA-M 0.000 claims 1
- 230000002194 synthesizing effect Effects 0.000 claims 1
- 239000006227 byproduct Substances 0.000 abstract description 11
- BDJSOPWXYLFTNW-UHFFFAOYSA-N methyl 3-methoxypropanoate Chemical compound COCCC(=O)OC BDJSOPWXYLFTNW-UHFFFAOYSA-N 0.000 abstract description 6
- 150000001875 compounds Chemical class 0.000 abstract description 3
- 229920000642 polymer Polymers 0.000 abstract description 3
- 229920006158 high molecular weight polymer Polymers 0.000 abstract description 2
- 239000000178 monomer Substances 0.000 abstract description 2
- 125000000391 vinyl group Chemical group [H]C([*])=C([H])[H] 0.000 abstract description 2
- 229920002554 vinyl polymer Polymers 0.000 abstract description 2
- 230000002745 absorbent Effects 0.000 abstract 1
- 239000002250 absorbent Substances 0.000 abstract 1
- 238000006243 chemical reaction Methods 0.000 description 53
- -1 N-substituted amides Chemical class 0.000 description 36
- 239000000047 product Substances 0.000 description 11
- 150000003335 secondary amines Chemical class 0.000 description 10
- 238000009835 boiling Methods 0.000 description 9
- ZSWFCLXCOIISFI-UHFFFAOYSA-N cyclopentadiene Chemical compound C1C=CC=C1 ZSWFCLXCOIISFI-UHFFFAOYSA-N 0.000 description 8
- OKKJLVBELUTLKV-UHFFFAOYSA-N Methanol Chemical compound OC OKKJLVBELUTLKV-UHFFFAOYSA-N 0.000 description 6
- 239000002994 raw material Substances 0.000 description 6
- 238000006116 polymerization reaction Methods 0.000 description 5
- 238000007086 side reaction Methods 0.000 description 5
- 239000003112 inhibitor Substances 0.000 description 4
- 239000002904 solvent Substances 0.000 description 4
- QTBSBXVTEAMEQO-UHFFFAOYSA-N Acetic acid Chemical compound CC(O)=O QTBSBXVTEAMEQO-UHFFFAOYSA-N 0.000 description 3
- ZMXDDKWLCZADIW-UHFFFAOYSA-N N,N-Dimethylformamide Chemical compound CN(C)C=O ZMXDDKWLCZADIW-UHFFFAOYSA-N 0.000 description 3
- YXFVVABEGXRONW-UHFFFAOYSA-N Toluene Chemical compound CC1=CC=CC=C1 YXFVVABEGXRONW-UHFFFAOYSA-N 0.000 description 3
- HPNMFZURTQLUMO-UHFFFAOYSA-N diethylamine Chemical compound CCNCC HPNMFZURTQLUMO-UHFFFAOYSA-N 0.000 description 3
- UAOMVDZJSHZZME-UHFFFAOYSA-N diisopropylamine Chemical compound CC(C)NC(C)C UAOMVDZJSHZZME-UHFFFAOYSA-N 0.000 description 3
- 239000012528 membrane Substances 0.000 description 3
- 238000000926 separation method Methods 0.000 description 3
- 238000005292 vacuum distillation Methods 0.000 description 3
- ROSDSFDQCJNGOL-UHFFFAOYSA-N Dimethylamine Chemical compound CNC ROSDSFDQCJNGOL-UHFFFAOYSA-N 0.000 description 2
- VEXZGXHMUGYJMC-UHFFFAOYSA-N Hydrochloric acid Chemical compound Cl VEXZGXHMUGYJMC-UHFFFAOYSA-N 0.000 description 2
- QIGBRXMKCJKVMJ-UHFFFAOYSA-N Hydroquinone Chemical compound OC1=CC=C(O)C=C1 QIGBRXMKCJKVMJ-UHFFFAOYSA-N 0.000 description 2
- 238000006845 Michael addition reaction Methods 0.000 description 2
- QAOWNCQODCNURD-UHFFFAOYSA-N Sulfuric acid Chemical compound OS(O)(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-N 0.000 description 2
- 150000001408 amides Chemical class 0.000 description 2
- 150000001412 amines Chemical class 0.000 description 2
- 230000015572 biosynthetic process Effects 0.000 description 2
- 239000003795 chemical substances by application Substances 0.000 description 2
- 230000007423 decrease Effects 0.000 description 2
- JQVDAXLFBXTEQA-UHFFFAOYSA-N dibutylamine Chemical compound CCCCNCCCC JQVDAXLFBXTEQA-UHFFFAOYSA-N 0.000 description 2
- WEHWNAOGRSTTBQ-UHFFFAOYSA-N dipropylamine Chemical compound CCCNCCC WEHWNAOGRSTTBQ-UHFFFAOYSA-N 0.000 description 2
- 238000003379 elimination reaction Methods 0.000 description 2
- 239000003607 modifier Substances 0.000 description 2
- 230000001172 regenerating effect Effects 0.000 description 2
- 239000011347 resin Substances 0.000 description 2
- 229920005989 resin Polymers 0.000 description 2
- 238000005979 thermal decomposition reaction Methods 0.000 description 2
- SMZOUWXMTYCWNB-UHFFFAOYSA-N 2-(2-methoxy-5-methylphenyl)ethanamine Chemical compound COC1=CC=C(C)C=C1CCN SMZOUWXMTYCWNB-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
- NJBCRXCAPCODGX-UHFFFAOYSA-N 2-methyl-n-(2-methylpropyl)propan-1-amine Chemical compound CC(C)CNCC(C)C NJBCRXCAPCODGX-UHFFFAOYSA-N 0.000 description 1
- 238000005698 Diels-Alder reaction Methods 0.000 description 1
- JGFBQFKZKSSODQ-UHFFFAOYSA-N Isothiocyanatocyclopropane Chemical compound S=C=NC1CC1 JGFBQFKZKSSODQ-UHFFFAOYSA-N 0.000 description 1
- CERQOIWHTDAKMF-UHFFFAOYSA-N Methacrylic acid Chemical compound CC(=C)C(O)=O CERQOIWHTDAKMF-UHFFFAOYSA-N 0.000 description 1
- QCOGKXLOEWLIDC-UHFFFAOYSA-N N-methylbutylamine Chemical compound CCCCNC QCOGKXLOEWLIDC-UHFFFAOYSA-N 0.000 description 1
- CTQNGGLPUBDAKN-UHFFFAOYSA-N O-Xylene Chemical compound CC1=CC=CC=C1C CTQNGGLPUBDAKN-UHFFFAOYSA-N 0.000 description 1
- 239000006096 absorbing agent Substances 0.000 description 1
- 239000002253 acid Substances 0.000 description 1
- 125000005907 alkyl ester group Chemical group 0.000 description 1
- PWLNAUNEAKQYLH-UHFFFAOYSA-N butyric acid octyl ester Natural products CCCCCCCCOC(=O)CCC PWLNAUNEAKQYLH-UHFFFAOYSA-N 0.000 description 1
- 238000005119 centrifugation Methods 0.000 description 1
- 238000011109 contamination Methods 0.000 description 1
- 230000006866 deterioration Effects 0.000 description 1
- 229940043279 diisopropylamine Drugs 0.000 description 1
- 238000004821 distillation Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- BHXIWUJLHYHGSJ-UHFFFAOYSA-N ethyl 3-ethoxypropanoate Chemical compound CCOCCC(=O)OCC BHXIWUJLHYHGSJ-UHFFFAOYSA-N 0.000 description 1
- 125000001495 ethyl group Chemical group [H]C([H])([H])C([H])([H])* 0.000 description 1
- 238000000605 extraction Methods 0.000 description 1
- 239000011521 glass Substances 0.000 description 1
- 125000004435 hydrogen atom Chemical group [H]* 0.000 description 1
- 239000003230 hygroscopic agent Substances 0.000 description 1
- 239000012442 inert solvent Substances 0.000 description 1
- 229910052500 inorganic mineral Inorganic materials 0.000 description 1
- 125000001449 isopropyl group Chemical group [H]C([H])([H])C([H])(*)C([H])([H])[H] 0.000 description 1
- 239000011707 mineral Substances 0.000 description 1
- IGGPQQNWURZLDA-UHFFFAOYSA-N n,n-diethyl-3-methoxypropanamide Chemical compound CCN(CC)C(=O)CCOC IGGPQQNWURZLDA-UHFFFAOYSA-N 0.000 description 1
- OVHHHVAVHBHXAK-UHFFFAOYSA-N n,n-diethylprop-2-enamide Chemical compound CCN(CC)C(=O)C=C OVHHHVAVHBHXAK-UHFFFAOYSA-N 0.000 description 1
- RKSYJNCKPUDQET-UHFFFAOYSA-N n,n-dipropylprop-2-enamide Chemical compound CCCN(CCC)C(=O)C=C RKSYJNCKPUDQET-UHFFFAOYSA-N 0.000 description 1
- UUIQMZJEGPQKFD-UHFFFAOYSA-N n-butyric acid methyl ester Natural products CCCC(=O)OC UUIQMZJEGPQKFD-UHFFFAOYSA-N 0.000 description 1
- QHCCDDQKNUYGNC-UHFFFAOYSA-N n-ethylbutan-1-amine Chemical compound CCCCNCC QHCCDDQKNUYGNC-UHFFFAOYSA-N 0.000 description 1
- XCVNDBIXFPGMIW-UHFFFAOYSA-N n-ethylpropan-1-amine Chemical compound CCCNCC XCVNDBIXFPGMIW-UHFFFAOYSA-N 0.000 description 1
- 150000007524 organic acids Chemical class 0.000 description 1
- NWVVVBRKAWDGAB-UHFFFAOYSA-N p-methoxyphenol Chemical compound COC1=CC=C(O)C=C1 NWVVVBRKAWDGAB-UHFFFAOYSA-N 0.000 description 1
- 150000002990 phenothiazines Chemical class 0.000 description 1
- 125000002924 primary amino group Chemical group [H]N([H])* 0.000 description 1
- NMWCXUDFZWVKKJ-UHFFFAOYSA-N propan-2-yl 2-ethoxypropanoate Chemical compound CCOC(C)C(=O)OC(C)C NMWCXUDFZWVKKJ-UHFFFAOYSA-N 0.000 description 1
- 238000000746 purification Methods 0.000 description 1
- 238000011084 recovery Methods 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
- 238000003756 stirring Methods 0.000 description 1
- 239000002699 waste material Substances 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
Abstract
Description
【発明の詳細な説明】
〔産業上の利用分野〕
本発明は、−綴代(I[[)
(式中、R1は一般式(+)におけるR1に同じ、R4
゜RSは一般式(II)におけるR4.R5に同じ、)
で表されるN−置換不飽和カルボン酸アミド(以下、N
−置換アミドと略する。)の製造方法に関する。Detailed Description of the Invention [Industrial Application Field] The present invention relates to -binding margin (I[[) (wherein, R1 is the same as R1 in the general formula (+), R4
゜RS is R4. in general formula (II). Same as R5)
N-substituted unsaturated carboxylic acid amide represented by (hereinafter referred to as N
-Abbreviated as substituted amide. ).
本発明によって提供されるN−置換アミドは、吸湿剤、
防曇剤、分離膜、紙加工剤及び樹脂改質剤等の広い用途
を有する有用な化合物である。The N-substituted amides provided by the present invention are hygroscopic agents,
It is a useful compound that has a wide range of uses such as antifogging agents, separation membranes, paper processing agents, and resin modifiers.
〔従来の技術及び発明が解決しようとする課題〕本発明
のN−置換アミドは、一般に不飽和カルボン酸エステル
とアミノ化合物とのアミツリシスにより製造することが
できる。[Prior Art and Problems to be Solved by the Invention] The N-substituted amide of the present invention can generally be produced by amicilysis of an unsaturated carboxylic acid ester and an amino compound.
ところが、不飽和カルボン酸エステルとアミノ化合物と
のアミツリシスに際しては、アミノ化合物の二重結合へ
のマイケル付加が起こり反応における目的物の選択率が
低い。また、マイケル付加物から二重結合を再生するに
は、180〜300℃という高温で熱分解を行い付加し
たアミノ化合物を脱離させる工程が必要となるが、この
際、重合物の生成等の副反応が起こり、目的物の収率が
著しく低下する(特開昭50−111016号)、この
副反応を抑制するために、低級アルコールをまず二重結
合に付加させた後アミツリシスを行い、次いで、高温で
脱アルコールを行い二重結合を再生して目的物を得る方
法(特開昭49−66623号、 USP−25345
85゜USP−2702822)が開示されている。However, in the amitrilysis of an unsaturated carboxylic acid ester and an amino compound, Michael addition to the double bond of the amino compound occurs, resulting in a low selectivity of the target product in the reaction. In addition, in order to regenerate double bonds from Michael adducts, it is necessary to carry out thermal decomposition at a high temperature of 180 to 300°C to remove the added amino compound, but in this case, the formation of polymers, etc. A side reaction occurs and the yield of the target product decreases significantly (Japanese Patent Application Laid-Open No. 111016/1982). In order to suppress this side reaction, a lower alcohol is first added to the double bond, and then amithrisis is performed, and then , a method for obtaining the desired product by regenerating double bonds by dealcoholization at high temperatures (JP-A No. 49-66623, USP-25345)
85° USP-2702822) is disclosed.
この方法は、二重結合へのアミノ化合物のマイケル付加
を防ぐ目的からは有効な手段であるが、脱アルコール反
応により二重結合を再生する際に重合等の副反応が起こ
り、目的物の収率を低下させる重大な欠点を有する。ま
た、二重結合の保護法としてシクロペンタジェンを二重
結合へディールス・アルダ−反応で付加させ、アミツリ
シス終了後、熱分解によりシクロペンタジェンを脱離さ
せる方法(特開昭49−66625号他)も開示されて
いる。しかし、この方法においても、副生成物の生成は
免れず、脱離したシクロペンタジェンの目的物からの分
離・回収工程を要し、また、製品中へのシクロペンタジ
ェンの微量の混入が避けられず、製品の品質を低下させ
る等の欠点を有する。Although this method is effective for the purpose of preventing Michael addition of amino compounds to double bonds, side reactions such as polymerization occur when regenerating double bonds by dealcoholization, resulting in the yield of the target product. has serious drawbacks that reduce the rate. In addition, as a method for protecting double bonds, cyclopentadiene is added to the double bond by Diels-Alder reaction, and after completion of amitrilysis, cyclopentadiene is removed by thermal decomposition (JP-A-49-66625 et al. ) are also disclosed. However, even in this method, the formation of by-products is inevitable, a separation and recovery process is required for the desorbed cyclopentadiene from the target product, and the contamination of trace amounts of cyclopentadiene into the product is avoided. However, it has drawbacks such as deterioration of product quality.
(Li題を解決するための手段]
本発明者らは、N−置換アミドを副生成物を伴わずに収
率よく製造する方法について鋭意検討した結果、β−ア
ルコキシ1itaカルボン酸エステルと二級アミンと反
応させた後、触媒を用いて温和な条件でアルコールを脱
離させて二重結合を再生することにより、高収率で目的
物を製造することができることを見出し本発明を完成さ
せるに至った。(Means for Solving the Li Problem) As a result of intensive study on a method for producing N-substituted amides in good yield without producing by-products, the present inventors discovered that β-alkoxy 1ita carboxylic acid ester and secondary They discovered that the desired product could be produced in high yield by reacting it with an amine and then removing the alcohol under mild conditions using a catalyst to regenerate the double bond, thereby completing the present invention. It's arrived.
本発明は、−綴代(1)
%式%()
(式中、R1は水素またはメチル基を示し、pg、 R
。The present invention provides - binding allowance (1) % formula % () (in the formula, R1 represents hydrogen or a methyl group, pg, R
.
は炭素数1〜3のアルキル基を示す、)で表されるβ−
アルコキシ置換カルボン酸エステル(以下、β−アルコ
キシ置換カルボン酸エステルと略する。represents an alkyl group having 1 to 3 carbon atoms, β-
Alkoxy-substituted carboxylic ester (hereinafter abbreviated as β-alkoxy-substituted carboxylic ester).
)と−綴代(n)
HN−R4(It )
(式中、Ra、Rsは炭素数1〜5のアルキル基を示す
、)で表される二級アミン(以下、二級アミンと略する
。)とを反応させてβ−アルコキシ置換カルボン酸アミ
ドを合成し、次いで触媒として塩基性触媒を使用してア
ルコールを脱離させることにより不飽和基を形成せしめ
てN−i換アミドを製造する方法に関する。) and - binding allowance (n) HN-R4(It) (wherein, Ra and Rs represent an alkyl group having 1 to 5 carbon atoms) (hereinafter abbreviated as secondary amine) ) to synthesize a β-alkoxy-substituted carboxylic acid amide, and then remove the alcohol using a basic catalyst as a catalyst to form an unsaturated group to produce a N-i-substituted amide. Regarding the method.
以下、本発明の詳細な説明する。The present invention will be explained in detail below.
本発明で使用するβ−アルコキシ置換カルボン酸エステ
ルとしては、例えば、β−メトキシプロピオン酸メチル
、β−メトキシプロピオン酸エチル、β−メトキシプロ
ピオン酸n−プロピル、β−メトキシプロピオン酸イソ
プロピル、β−メトキシイソ酪酸メチル、β−メトキシ
イソ酪酸エチル、β−メトキシイソ酪酸n−プロピル、
β−メトキシイソ酪酸イソプロピル、β−エトキシプロ
ピオン酸メチル、β−エトキシプロピオン酸エチル、β
−エトキシプロピオン酸n−プロピル、β−エトキジプ
ロピオン酸イソプロピル、β−エトキシイソ酪酸メチル
、β−エトキシイソ酪酸エチル、βエトキシイソ醋酸ロ
ープロピル、β−エトキシイソ酪酸イソプロピル、β−
イソプロポキシプロピオン酸メチル、β−インプロポキ
シプロピオン酸エチル、β−イソプロポキシプロピオン
酸n−プロピル、β−イソプロポキシプロピオン酸イソ
プロピル、β−イソプロポキシイソ酪酸メチル、β−イ
ソプロポキシイソ酪酸エチル、β−イソプロポキシイソ
酪酸n−プロピル、β−イソプロポキシイソ酪酸イソプ
ロピル、β−n−プロポキシプロピオン酸メチル、β−
ロープロポキシプロピオン酸エチル、β−n−プロポキ
シプロピオン酸ロープロピル、β−nプロポキシプロビ
オン酸イソプロピル、β−n−プロポキシイソ酪酸エチ
ル、β−n−プロポキシイソ酪酸エチル、β−n−プロ
ポキシイソ酪酸n−プロピル、β−n−プロポキシイソ
酪酸イソプロピル等が挙げられる。Examples of the β-alkoxy-substituted carboxylic acid ester used in the present invention include methyl β-methoxypropionate, ethyl β-methoxypropionate, n-propyl β-methoxypropionate, isopropyl β-methoxypropionate, and β-methoxyisopropionate. Methyl butyrate, ethyl β-methoxyisobutyrate, n-propyl β-methoxyisobutyrate,
Isopropyl β-methoxyisobutyrate, Methyl β-ethoxypropionate, Ethyl β-ethoxypropionate, β
- n-propyl ethoxypropionate, isopropyl β-ethoxydipropionate, methyl β-ethoxyisobutyrate, ethyl β-ethoxyisobutyrate, rhopropyl β-ethoxyisoacetate, isopropyl β-ethoxyisobutyrate, β-
Methyl isopropoxypropionate, ethyl β-impropoxypropionate, n-propyl β-isopropoxypropionate, isopropyl β-isopropoxypropionate, methyl β-isopropoxyisobutyrate, ethyl β-isopropoxyisobutyrate, β- n-propyl isopropoxyisobutyrate, isopropyl β-isopropoxyisobutyrate, methyl β-n-propoxypropionate, β-
Ethyl low-propoxypropionate, low-propyl β-n-propoxypropionate, isopropyl β-n-propoxypropionate, ethyl β-n-propoxyisobutyrate, ethyl β-n-propoxyisobutyrate, β-n-propoxyisobutyric acid n-propyl, isopropyl β-n-propoxyisobutyrate, and the like.
これらのアルコキシ置換カルボン酸アルキルエステルは
、アクリル酸またはメタクリル酸のアルキルエステルの
二重結合へアルコールを付加させることにより得ること
ができる。These alkoxy-substituted carboxylic acid alkyl esters can be obtained by adding an alcohol to the double bond of an alkyl ester of acrylic acid or methacrylic acid.
二級アミンとしては、ジメチルアミン、ジエチルアミン
、N、N−エチルプロピルアミン、N、N−メチルブチ
ルアミン、ジ−n−プロピルアミン、ジイソプロピルア
ミン、N、N−エチルブチルアミン、ジ−n−ブチルア
ミン、ジイソブチルアミン、ジベンチルアミン等を挙げ
ることができる。Examples of secondary amines include dimethylamine, diethylamine, N,N-ethylpropylamine, N,N-methylbutylamine, di-n-propylamine, diisopropylamine, N,N-ethylbutylamine, di-n-butylamine, and diisobutylamine. Examples include amines, dibentylamines, and the like.
本発明においては、まず、前記β−アルコキシ置換カル
ボン酸エステルと二級アミンとのアミツリシスによりβ
−アルコキシ置換カルボン酸アミドを得る。In the present invention, first, β-alkoxy-substituted carboxylic acid ester and secondary amine are subjected to amithrilysis to obtain β-
-Alkoxy-substituted carboxylic acid amide is obtained.
β−アルコキシ置換カルボン酸エステルに対する二級ア
ミンの仕込モル比は、0.3〜3の範囲が好ましい。The molar ratio of the secondary amine to the β-alkoxy substituted carboxylic acid ester is preferably in the range of 0.3 to 3.
使用する二級アミンの沸点が、アミツリシスで副生ずる
アルコールの沸点より高い場合、反応圧力は、大気圧下
または減圧下がよく、望ましい反応圧力は50〜760
smHgである。When the boiling point of the secondary amine used is higher than the boiling point of the alcohol by-produced in amitrilysis, the reaction pressure is preferably atmospheric pressure or reduced pressure, and the preferred reaction pressure is 50 to 760.
smHg.
反応温度は、副生ずるアルコールの沸点以上で行うこと
が好ましく、反応圧力、使用する二級アミンの沸点によ
っても異なるが、40〜180°Cが望ましい。この場
合、副生ず、るアルコールを反応系から留去しながら反
応を進める方法が反応速度を高め、転化率を上げるのに
有利である。The reaction temperature is preferably higher than the boiling point of the alcohol produced as a by-product, and is preferably 40 to 180°C, although it varies depending on the reaction pressure and the boiling point of the secondary amine used. In this case, it is advantageous to proceed with the reaction while distilling the alcohol by-produced from the reaction system to increase the reaction rate and conversion rate.
また、使用する二級アミンの沸点がアミツリシスで副生
ずるアルコールの沸点より低い場合、副生アルコールを
留去させようとすると、原料の二級アミンが先に系外に
出てしまう、そのためにオートクレーブのような加圧可
能な密閉反応素装置を用いる必要がある。このときの反
応圧力は、反応温度により変わるが自発的に発生した圧
力で十分であり、1〜10atm位になる。この場合、
副生ずるアルコールを反応系から留去できないため、反
応温度をより高温にする必要があり、望ましい反応温度
は、使用する原料により異なるが、100〜180℃が
望ましい。In addition, if the boiling point of the secondary amine used is lower than the boiling point of the alcohol by-produced during amitrilysis, when attempting to distill off the by-product alcohol, the raw material secondary amine will come out of the system first. It is necessary to use a closed reactor that can be pressurized, such as The reaction pressure at this time varies depending on the reaction temperature, but the spontaneously generated pressure is sufficient and is about 1 to 10 atm. in this case,
Since the by-product alcohol cannot be distilled off from the reaction system, the reaction temperature must be raised to a higher temperature, and the desired reaction temperature varies depending on the raw materials used, but is preferably 100 to 180°C.
このように加圧下の場合は、副生ずるアルコールを反応
系から留去することが不可能なため、平衡を移動させる
ことができず、転化率をある一定以上あげることができ
ない、この転化率の限界は原料の二級アミン、β−アル
コキシ置換カルボン酸エステルによって異なるが50〜
60%である。Under pressure, it is impossible to distill off the by-product alcohol from the reaction system, so the equilibrium cannot be shifted and the conversion rate cannot be increased beyond a certain level. The limit varies depending on the raw material secondary amine and β-alkoxy-substituted carboxylic acid ester, but is 50~
It is 60%.
また、この反応は、二級アミンが塩基性であるので無触
媒でも進行するが、公知の塩基性のアミツリシス触媒を
添加することも可能である。Further, since the secondary amine is basic, this reaction proceeds even without a catalyst, but it is also possible to add a known basic amitrisis catalyst.
得られたβ−アルコキシ置換カルボン酸アミドは、減圧
蒸留により精製して次の工程に使用してもよいが、反応
終了後、未反応の原料及び低沸副生成物を留去するのみ
で次の反応に使用可能である。The obtained β-alkoxy-substituted carboxylic acid amide may be purified by vacuum distillation and used in the next step, but after the reaction is completed, unreacted raw materials and low-boiling byproducts are simply distilled off. It can be used for this reaction.
次と、β−アルコキシ置換カルボン酸アミドよリアルコ
ールを脱離させてN−置換アミドを合成するが、この際
、従来行われている高温でのクラッキングにより目的物
を製造した場合には重合物等の好ましくない副生成物を
多量に生じ、目的物の精製を煩雑にし、また、収率を著
しく低下させる、このため本発明においては、触媒を使
用して温和な条件でアルコールを脱離させることが肝要
であり、触媒としては塩基性触媒を使用する。Next, an N-substituted amide is synthesized by eliminating the real alcohol from a β-alkoxy-substituted carboxylic acid amide. A large amount of undesirable by-products such as This is important, and a basic catalyst is used as the catalyst.
本発明の塩基性触媒としては、アルカリ金属アルコラー
ト、アルカリ金属水酸化物、アルカリ土類金属水酸化物
または酸化物、アルカリ金属炭酸塩等が挙げられる。Examples of the basic catalyst of the present invention include alkali metal alcoholates, alkali metal hydroxides, alkaline earth metal hydroxides or oxides, and alkali metal carbonates.
アルカリ金属アルコラートとしては、ナトリウムメチラ
ート、ナトリウムエチラート、カリウムメチラート、カ
リウムエチラート等が挙げられる。Examples of the alkali metal alcoholate include sodium methylate, sodium ethylate, potassium methylate, potassium ethylate, and the like.
アルカリ金属水酸化物としては、水酸化リチウム、水酸
化ナトリウム、水酸化カリウム、水酸化ルビジウム、水
酸化セシウム等が挙げられる。Examples of the alkali metal hydroxide include lithium hydroxide, sodium hydroxide, potassium hydroxide, rubidium hydroxide, and cesium hydroxide.
アルカリ土類金属水酸化物または酸化物としては、水酸
化マグネシウム、水酸化カルシウム、水酸化ストロンチ
ウム、水酸化バリウム、酸化マグネシウム、酸化カルシ
ウム、酸化バリウム等が挙げられる。また、アルカリ金
属炭酸塩としては、炭酸ナトリウムシ炭酸カリウムが挙
げられる。Examples of alkaline earth metal hydroxides or oxides include magnesium hydroxide, calcium hydroxide, strontium hydroxide, barium hydroxide, magnesium oxide, calcium oxide, barium oxide, and the like. Further, examples of the alkali metal carbonate include sodium carbonate and potassium carbonate.
これら塩基性触媒の添加は、不活性な溶剤に溶かして反
応系へ添加することも固体のまま添加することも可能で
ある。These basic catalysts can be added to the reaction system after being dissolved in an inert solvent, or they can be added in solid form.
副反応を抑えるため反応は低温で行うことが好ましく、
反応温度は50〜170″Cの範囲が好ましい。It is preferable to carry out the reaction at low temperature to suppress side reactions.
The reaction temperature is preferably in the range of 50 to 170''C.
反応圧力は50〜760+*mHgが適当で、生成する
アルコールを留去しつつ反応を進めることが反応速度を
高める点から望ましい。A suitable reaction pressure is 50 to 760+*mHg, and it is desirable to proceed with the reaction while distilling off the alcohol produced, from the viewpoint of increasing the reaction rate.
副反応を防ぐもう一つの手段として溶剤を使用すること
も可能である0本発明においては溶剤を使用しないでも
よいが、溶剤を使用した場合でも生成物の収率の低下を
まねくことはなく、良好な収率を維持することができる
。It is also possible to use a solvent as another means of preventing side reactions.Although it is not necessary to use a solvent in the present invention, even if a solvent is used, it will not result in a decrease in the yield of the product, A good yield can be maintained.
溶剤としては、N、N−ジメチルホルムアミド、N。As a solvent, N,N-dimethylformamide, N.
N−ジメチルスルホキシド、トルエン、キシレン等が挙
げられる。Examples include N-dimethylsulfoxide, toluene, xylene, and the like.
反応終了後、反応液は塩酸、硫酸等の鉱酸または酢酸等
の有機酸で塩基性触媒を中和するか、あるいは、抽出操
作により廃触媒を除去するか、あるいは、不溶の触媒を
濾過もしくは、遠心分離により除去した後、目的物を蒸
留等により精製する。After the reaction is completed, the basic catalyst in the reaction solution is neutralized with a mineral acid such as hydrochloric acid or sulfuric acid, or an organic acid such as acetic acid, or the waste catalyst is removed by an extraction operation, or the undissolved catalyst is filtered or removed. , and then removed by centrifugation, the target product is purified by distillation or the like.
なお、反応中及び目的物の精製中には、重合禁止剤を添
加することが好ましく、重合禁止剤としては、例えば、
ハイドロキノン、ハイドロキノンモノメチルエーテル、
フェノチアジン、クペロン等が適当である。In addition, it is preferable to add a polymerization inhibitor during the reaction and purification of the target product, and examples of the polymerization inhibitor include:
hydroquinone, hydroquinone monomethyl ether,
Phenothiazines, cuperone, etc. are suitable.
[実施例] 以下、実施例により本発明を具体的に説明する。[Example] Hereinafter, the present invention will be specifically explained with reference to Examples.
実施例1
[アミツリシス]
攪拌機及び塔頂に分留装置をつけて、ガラス製うッシヒ
リングを充填した塔を有する四ツロフラスコにβ−メト
キシプロピオン酸メチル118.1g(1,0モル)及
びジ−n−プロピルアミン202.3g(2,0モル)
を入れ、125℃で生成するメタノールを留去しながら
反応を進めた。Example 1 [Amitrisis] 118.1 g (1.0 mol) of methyl β-methoxypropionate and di-n were placed in a four-cylinder flask equipped with a stirrer and a column equipped with a fractionator at the top and filled with a glass Uschig ring. -Propylamine 202.3g (2.0 mol)
was added, and the reaction proceeded while distilling off the methanol produced at 125°C.
反応は16時間で終了し、反応終了後、未反応のジ−n
−プロピルアミンを減圧下で留去した。さらに低沸分留
去後150.6gの反応液を得た0反応液のN、N−シ
ートプロピル−β−メトキシプロピオアミドの含有率は
、90%であった。The reaction was completed in 16 hours, and after the reaction, unreacted di-n
-Propylamine was distilled off under reduced pressure. Furthermore, the content of N,N-sheet propyl-β-methoxypropioamide in 150.6 g of the reaction solution obtained after distilling off the low-boiling fraction was 90%.
[アルコール脱ml]
前記アミツリシスで得られた反応液を前記アミツリシス
と同様に反応器に入れ、触媒として水酸化カルシウム4
.0g、重合禁止剤としてクペロン0゜6gを添加して
、125°C,150mmHgで反応させた。[Alcohol deml] The reaction solution obtained in the above amithrisis was put into a reactor in the same manner as in the above amithrisis, and calcium hydroxide 4 was added as a catalyst.
.. 0g of cuperone was added as a polymerization inhibitor, and the reaction was carried out at 125°C and 150mmHg.
反応に際して副生ずるアルコールは、反応系から留去し
ながら反応を進めた0反応は4時間で終了し、得られた
反応液を減圧蒸留で精製してN、N−ジ−n−プロピル
アクリルアミド109.3gを得た。純度は99.5%
で、収率は70.5%(反応に供与したβ−メトキシブ
ロピオン酸メチル基準)であった。The reaction proceeded while the alcohol by-produced during the reaction was distilled off from the reaction system. The reaction was completed in 4 hours, and the resulting reaction solution was purified by vacuum distillation to obtain N,N-di-n-propylacrylamide 109 .3g was obtained. Purity is 99.5%
The yield was 70.5% (based on methyl β-methoxypropionate donated to the reaction).
実施例2〜8
実施例1と同様の反応装置を用い、表1の原料及び触媒
を使用して、実施例1と同様のアミツリシス及びアルコ
ール脱離反応を行い、相当するN−置換アミドを合成し
表1の結果を得た。Examples 2 to 8 Using the same reaction apparatus as in Example 1 and the raw materials and catalysts in Table 1, the same amicilysis and alcohol elimination reactions as in Example 1 were carried out to synthesize the corresponding N-substituted amides. The results shown in Table 1 were obtained.
(以下、余白)
実施例9
[アミツリシス]
攪拌機のついた12オートクレーブにβ−メトキシプロ
ピオン酸メチル236.2g(2,0モル)及びジエチ
ルアミン292.5g(4,0モル)を仕込み、蓋をし
て、撹拌しながら昇温し、100°Cにした。10時間
後、反応を止め冷却し、反応液を取り出して未反応のジ
エチルアミンを留去した。さらに低沸分留去後、111
10.0gの反応液を得た0反応後のN、N−ジエチル
−β−メトキシプロピオアミドの含有率は92゜0%で
あった。(The following is a blank space) Example 9 [Amiturisis] 236.2 g (2.0 mol) of methyl β-methoxypropionate and 292.5 g (4.0 mol) of diethylamine were placed in a 12 autoclave equipped with a stirrer, and the lid was closed. The temperature was raised to 100°C while stirring. After 10 hours, the reaction was stopped and cooled, and the reaction solution was taken out and unreacted diethylamine was distilled off. After further distilling off the low boiling fraction, 111
The content of N,N-diethyl-β-methoxypropioamide after the 0-reaction yielding 10.0 g of reaction solution was 92.0%.
[アルコール脱M]
前記アミツリシスで得られた反応液180.0gを実施
例1と同様の反応器に入れ、触媒として水酸化リチウム
4.0g、重合禁止剤としてクペロン1.0gを添加し
て、125°C1L50ff1m)Igで反応させた0
反応に際して副生ずるメタノールは反応系から留去しな
がら反応を進めた0反応は4時間で終了し、得られた反
応液を減圧蒸留で精製して、N、N−ジエチルアクリル
アミド127.7gを得た。純度は99.6%で収率は
50%(反応に供与したβ−メトキシプロピオン酸メチ
ル基準)であった。[Alcohol DeMization] 180.0 g of the reaction solution obtained in the above amithrisis was placed in the same reactor as in Example 1, 4.0 g of lithium hydroxide was added as a catalyst, and 1.0 g of cuperone was added as a polymerization inhibitor. 125°C1L50ff1m)0 reacted with Ig
The reaction proceeded while the methanol by-produced during the reaction was distilled off from the reaction system. The reaction was completed in 4 hours, and the resulting reaction solution was purified by vacuum distillation to obtain 127.7 g of N,N-diethylacrylamide. Ta. The purity was 99.6% and the yield was 50% (based on methyl β-methoxypropionate donated to the reaction).
実施例10〜12
実施例9と同様の反応装置を用い、表2の原料及び触媒
を使用して、実施例9と同様のアミツリシス及びアルコ
ール脱離反応を行い、相当するN−置換アミドを合成し
表2の結果を得た。Examples 10 to 12 Using the same reaction apparatus as in Example 9 and the raw materials and catalysts in Table 2, the same amicilysis and alcohol elimination reactions as in Example 9 were carried out to synthesize the corresponding N-substituted amides. The results shown in Table 2 were obtained.
(以下、余白)
[発明の効果]
本発明の方法によれば、重合物等の副生成物が少なく高
収率でN−置換アミドを製造することができる。得られ
たN−置換アミドは単独重合あるいは、他のビニル系モ
ノマーと共重合させて、吸湿剤、防曇膜、分離膜及び樹
脂改質剤等の用途に好適な高分子量の重合体を製造する
ことができる。(Hereinafter, blank spaces) [Effects of the Invention] According to the method of the present invention, an N-substituted amide can be produced in high yield with few by-products such as polymers. The obtained N-substituted amide is homopolymerized or copolymerized with other vinyl monomers to produce high molecular weight polymers suitable for uses such as moisture absorbers, antifogging membranes, separation membranes, and resin modifiers. can do.
特許出願人 三井東圧化学化学会社Patent applicant: Mitsui Toatsu Chemical Company
Claims (1)
R_3は炭素数1〜3のアルキル基を示す。)で表され
るβ−アルコキシ置換カルボン酸エステルと一般式(I
I) ▲数式、化学式、表等があります▼(II) (式中、R_1、R_5は炭素数1〜5のアルキル基を
示す。)で表される二級アミンとを反応させてβ−アル
コキシ置換カルボン酸アミドを合成し、次いで塩基性触
媒を使用してアルコールを脱離させることにより不飽和
基を形成せしめることを特徴とする一般式(III) ▲数式、化学式、表等があります▼(III) (式中、R_1は式( I )におけるR_1に同じ。R
_4、R_5は式(II)におけるR_4、R_5に同じ
。)で表されるN−置換不飽和カルボン酸アミドの製造
方法。 2、塩基性触媒がアルカリ金属アルコラート、アルカリ
金属水酸化物、アルカリ土類金属水酸化物、アルカリ土
類金属酸化物またはアルカリ金属炭酸塩である請求項1
記載の方法。 3、塩基性触媒がナトリウムメチラート、ナトリウムエ
チラート、カリウムメチラートまたはカリウムエチラー
トである請求項1記載の方法。 4、塩基性触媒が水酸化リチウム、水酸化ナトリウム、
水酸化カリウム、水酸化ルビジウムまたは水酸化セシウ
ムである請求項1記載の方法。 5、塩基性触媒が水酸化マグネシウム、水酸化カルシウ
ム、水酸化ストロンチウム、水酸化バリウム、酸化マグ
ネシウム、酸化カルシウムまたは酸化バリウムである請
求項1記載の方法。 6、塩基性触媒が炭酸ナトリウムまたは炭酸カリウムで
ある請求項1記載の方法。[Claims] 1. General formula (I) ▲There are mathematical formulas, chemical formulas, tables, etc.▼(I) (In the formula, R_1 represents hydrogen or a methyl group, R_2,
R_3 represents an alkyl group having 1 to 3 carbon atoms. ) and the β-alkoxy-substituted carboxylic acid ester represented by the general formula (I
I) ▲There are mathematical formulas, chemical formulas, tables, etc.▼ (II) (In the formula, R_1 and R_5 represent an alkyl group having 1 to 5 carbon atoms.) By reacting with a secondary amine represented by General formula (III), which is characterized by forming an unsaturated group by synthesizing a substituted carboxylic acid amide and then eliminating the alcohol using a basic catalyst ▲There are mathematical formulas, chemical formulas, tables, etc.▼ ( III) (In the formula, R_1 is the same as R_1 in formula (I).
_4 and R_5 are the same as R_4 and R_5 in formula (II). ) A method for producing an N-substituted unsaturated carboxylic acid amide. 2. Claim 1, wherein the basic catalyst is an alkali metal alcoholate, an alkali metal hydroxide, an alkaline earth metal hydroxide, an alkaline earth metal oxide or an alkali metal carbonate.
Method described. 3. The method according to claim 1, wherein the basic catalyst is sodium methylate, sodium ethylate, potassium methylate or potassium ethylate. 4. The basic catalyst is lithium hydroxide, sodium hydroxide,
2. The method according to claim 1, wherein the hydroxide is potassium hydroxide, rubidium hydroxide or cesium hydroxide. 5. The method according to claim 1, wherein the basic catalyst is magnesium hydroxide, calcium hydroxide, strontium hydroxide, barium hydroxide, magnesium oxide, calcium oxide or barium oxide. 6. The method according to claim 1, wherein the basic catalyst is sodium carbonate or potassium carbonate.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP63198052A JPH0248559A (en) | 1988-08-10 | 1988-08-10 | Production of unsaturated carboxylic acid amide |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP63198052A JPH0248559A (en) | 1988-08-10 | 1988-08-10 | Production of unsaturated carboxylic acid amide |
Publications (1)
Publication Number | Publication Date |
---|---|
JPH0248559A true JPH0248559A (en) | 1990-02-19 |
Family
ID=16384733
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP63198052A Pending JPH0248559A (en) | 1988-08-10 | 1988-08-10 | Production of unsaturated carboxylic acid amide |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH0248559A (en) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP2123631A1 (en) * | 2007-02-20 | 2009-11-25 | Idemitsu Kosan Co., Ltd. | Process for producing -alkoxypropionamide |
JP2011168514A (en) * | 2010-02-17 | 2011-09-01 | Kohjin Co Ltd | Method for producing high-quality n(n, n)-mono(di)alkyl acrylamide |
-
1988
- 1988-08-10 JP JP63198052A patent/JPH0248559A/en active Pending
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP2123631A1 (en) * | 2007-02-20 | 2009-11-25 | Idemitsu Kosan Co., Ltd. | Process for producing -alkoxypropionamide |
EP2123631A4 (en) * | 2007-02-20 | 2010-06-23 | Idemitsu Kosan Co | Process for producing -alkoxypropionamide |
US8338645B2 (en) | 2007-02-20 | 2012-12-25 | Idemitsu Kosan Co., Ltd. | Method for producing a β-alkoxypropionamide |
JP2011168514A (en) * | 2010-02-17 | 2011-09-01 | Kohjin Co Ltd | Method for producing high-quality n(n, n)-mono(di)alkyl acrylamide |
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