JP2001158760A - Method of producing fumaric monoalkyl ester and sodium salt thereof - Google Patents
Method of producing fumaric monoalkyl ester and sodium salt thereofInfo
- Publication number
- JP2001158760A JP2001158760A JP34229599A JP34229599A JP2001158760A JP 2001158760 A JP2001158760 A JP 2001158760A JP 34229599 A JP34229599 A JP 34229599A JP 34229599 A JP34229599 A JP 34229599A JP 2001158760 A JP2001158760 A JP 2001158760A
- Authority
- JP
- Japan
- Prior art keywords
- monoalkyl
- fumarate
- sodium salt
- acid chloride
- monoalkyl fumarate
- 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.)
- Withdrawn
Links
- 159000000000 sodium salts Chemical class 0.000 title claims abstract description 10
- 238000000034 method Methods 0.000 title claims abstract description 9
- 150000002148 esters Chemical class 0.000 title abstract description 13
- YXFVVABEGXRONW-UHFFFAOYSA-N Toluene Chemical compound CC1=CC=CC=C1 YXFVVABEGXRONW-UHFFFAOYSA-N 0.000 claims abstract description 39
- 238000006317 isomerization reaction Methods 0.000 claims abstract description 16
- HEMHJVSKTPXQMS-UHFFFAOYSA-M Sodium hydroxide Chemical compound [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 claims abstract description 15
- 150000001732 carboxylic acid derivatives Chemical class 0.000 claims abstract description 10
- CTQNGGLPUBDAKN-UHFFFAOYSA-N O-Xylene Chemical compound CC1=CC=CC=C1C CTQNGGLPUBDAKN-UHFFFAOYSA-N 0.000 claims abstract description 9
- 239000008096 xylene Substances 0.000 claims abstract description 9
- 150000004945 aromatic hydrocarbons Chemical class 0.000 claims abstract description 8
- 238000004519 manufacturing process Methods 0.000 claims abstract description 4
- 230000003472 neutralizing effect Effects 0.000 claims abstract 2
- VZCYOOQTPOCHFL-UHFFFAOYSA-N trans-butenedioic acid Natural products OC(=O)C=CC(O)=O VZCYOOQTPOCHFL-UHFFFAOYSA-N 0.000 claims description 44
- VZCYOOQTPOCHFL-OWOJBTEDSA-N Fumaric acid Chemical compound OC(=O)\C=C\C(O)=O VZCYOOQTPOCHFL-OWOJBTEDSA-N 0.000 claims description 32
- VZCYOOQTPOCHFL-UPHRSURJSA-N maleic acid Chemical compound OC(=O)\C=C/C(O)=O VZCYOOQTPOCHFL-UPHRSURJSA-N 0.000 claims description 14
- FPYJFEHAWHCUMM-UHFFFAOYSA-N maleic anhydride Chemical compound O=C1OC(=O)C=C1 FPYJFEHAWHCUMM-UHFFFAOYSA-N 0.000 claims description 5
- -1 aromatic monocarboxylic acid Chemical class 0.000 claims description 4
- 125000004432 carbon atom Chemical group C* 0.000 claims description 3
- 230000032050 esterification Effects 0.000 claims description 3
- 238000005886 esterification reaction Methods 0.000 claims description 3
- 125000001931 aliphatic group Chemical group 0.000 claims 2
- 125000000217 alkyl group Chemical group 0.000 claims 2
- 239000002609 medium Substances 0.000 claims 2
- OFOBLEOULBTSOW-UHFFFAOYSA-N Malonic acid Chemical compound OC(=O)CC(O)=O OFOBLEOULBTSOW-UHFFFAOYSA-N 0.000 claims 1
- 239000012736 aqueous medium Substances 0.000 claims 1
- 239000000243 solution Substances 0.000 abstract description 4
- 239000007864 aqueous solution Substances 0.000 abstract description 2
- 239000002904 solvent Substances 0.000 description 15
- 238000006243 chemical reaction Methods 0.000 description 11
- ZLYYJUJDFKGVKB-OWOJBTEDSA-N (e)-but-2-enedioyl dichloride Chemical compound ClC(=O)\C=C\C(Cl)=O ZLYYJUJDFKGVKB-OWOJBTEDSA-N 0.000 description 6
- CSCPPACGZOOCGX-UHFFFAOYSA-N Acetone Chemical compound CC(C)=O CSCPPACGZOOCGX-UHFFFAOYSA-N 0.000 description 6
- 238000001914 filtration Methods 0.000 description 6
- MHQJUHSHQGQVTM-VHEBQXMUSA-N (e)-4-octadecoxy-4-oxobut-2-enoic acid Chemical compound CCCCCCCCCCCCCCCCCCOC(=O)\C=C\C(O)=O MHQJUHSHQGQVTM-VHEBQXMUSA-N 0.000 description 5
- 239000003054 catalyst Substances 0.000 description 5
- 239000013078 crystal Substances 0.000 description 5
- DNIAPMSPPWPWGF-GSVOUGTGSA-N (R)-(-)-Propylene glycol Chemical compound C[C@@H](O)CO DNIAPMSPPWPWGF-GSVOUGTGSA-N 0.000 description 4
- 230000015572 biosynthetic process Effects 0.000 description 4
- 239000001530 fumaric acid Substances 0.000 description 4
- GLDOVTGHNKAZLK-UHFFFAOYSA-N octadecan-1-ol Chemical compound CCCCCCCCCCCCCCCCCCO GLDOVTGHNKAZLK-UHFFFAOYSA-N 0.000 description 4
- VZGDMQKNWNREIO-UHFFFAOYSA-N tetrachloromethane Chemical compound ClC(Cl)(Cl)Cl VZGDMQKNWNREIO-UHFFFAOYSA-N 0.000 description 4
- ZWEHNKRNPOVVGH-UHFFFAOYSA-N 2-Butanone Chemical compound CCC(C)=O ZWEHNKRNPOVVGH-UHFFFAOYSA-N 0.000 description 3
- UHOVQNZJYSORNB-UHFFFAOYSA-N Benzene Chemical compound C1=CC=CC=C1 UHOVQNZJYSORNB-UHFFFAOYSA-N 0.000 description 3
- MHQJUHSHQGQVTM-HNENSFHCSA-N Octadecyl fumarate Chemical compound CCCCCCCCCCCCCCCCCCOC(=O)\C=C/C(O)=O MHQJUHSHQGQVTM-HNENSFHCSA-N 0.000 description 3
- 150000008282 halocarbons Chemical class 0.000 description 3
- 239000000203 mixture Substances 0.000 description 3
- 238000006386 neutralization reaction Methods 0.000 description 3
- 239000002994 raw material Substances 0.000 description 3
- 238000003786 synthesis reaction Methods 0.000 description 3
- 238000001816 cooling Methods 0.000 description 2
- BXWNKGSJHAJOGX-UHFFFAOYSA-N hexadecan-1-ol Chemical compound CCCCCCCCCCCCCCCCO BXWNKGSJHAJOGX-UHFFFAOYSA-N 0.000 description 2
- 239000012535 impurity Substances 0.000 description 2
- GOQYKNQRPGWPLP-UHFFFAOYSA-N n-heptadecyl alcohol Natural products CCCCCCCCCCCCCCCCCO GOQYKNQRPGWPLP-UHFFFAOYSA-N 0.000 description 2
- CTSLXHKWHWQRSH-UHFFFAOYSA-N oxalyl chloride Chemical compound ClC(=O)C(Cl)=O CTSLXHKWHWQRSH-UHFFFAOYSA-N 0.000 description 2
- 239000002244 precipitate Substances 0.000 description 2
- 239000000047 product Substances 0.000 description 2
- HLZKNKRTKFSKGZ-UHFFFAOYSA-N tetradecan-1-ol Chemical compound CCCCCCCCCCCCCCO HLZKNKRTKFSKGZ-UHFFFAOYSA-N 0.000 description 2
- 238000005406 washing Methods 0.000 description 2
- NGNBDVOYPDDBFK-UHFFFAOYSA-N 2-[2,4-di(pentan-2-yl)phenoxy]acetyl chloride Chemical compound CCCC(C)C1=CC=C(OCC(Cl)=O)C(C(C)CCC)=C1 NGNBDVOYPDDBFK-UHFFFAOYSA-N 0.000 description 1
- 229920002472 Starch Polymers 0.000 description 1
- PWAXUOGZOSVGBO-UHFFFAOYSA-N adipoyl chloride Chemical compound ClC(=O)CCCCC(Cl)=O PWAXUOGZOSVGBO-UHFFFAOYSA-N 0.000 description 1
- 150000007933 aliphatic carboxylic acids Chemical class 0.000 description 1
- 239000003242 anti bacterial agent Substances 0.000 description 1
- WPYMKLBDIGXBTP-UHFFFAOYSA-N benzoic acid Chemical compound OC(=O)C1=CC=CC=C1 WPYMKLBDIGXBTP-UHFFFAOYSA-N 0.000 description 1
- PASDCCFISLVPSO-UHFFFAOYSA-N benzoyl chloride Chemical compound ClC(=O)C1=CC=CC=C1 PASDCCFISLVPSO-UHFFFAOYSA-N 0.000 description 1
- 229960000541 cetyl alcohol Drugs 0.000 description 1
- 150000001805 chlorine compounds Chemical group 0.000 description 1
- 230000000052 comparative effect Effects 0.000 description 1
- 150000001875 compounds Chemical class 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
- 229910052736 halogen Inorganic materials 0.000 description 1
- 150000002367 halogens Chemical class 0.000 description 1
- 239000000314 lubricant Substances 0.000 description 1
- 229910052751 metal Inorganic materials 0.000 description 1
- 239000002184 metal Substances 0.000 description 1
- 239000003607 modifier Substances 0.000 description 1
- 125000001421 myristyl group Chemical group [H]C([*])([H])C([H])([H])C([H])([H])C([H])([H])C([H])([H])C([H])([H])C([H])([H])C([H])([H])C([H])([H])C([H])([H])C([H])([H])C([H])([H])C([H])([H])C([H])([H])[H] 0.000 description 1
- 235000016709 nutrition Nutrition 0.000 description 1
- 239000003960 organic solvent Substances 0.000 description 1
- 125000000913 palmityl group Chemical group [H]C([*])([H])C([H])([H])C([H])([H])C([H])([H])C([H])([H])C([H])([H])C([H])([H])C([H])([H])C([H])([H])C([H])([H])C([H])([H])C([H])([H])C([H])([H])C([H])([H])C([H])([H])C([H])([H])[H] 0.000 description 1
- 239000011541 reaction mixture Substances 0.000 description 1
- 230000035484 reaction time Effects 0.000 description 1
- 150000003839 salts Chemical class 0.000 description 1
- 238000007086 side reaction Methods 0.000 description 1
- 235000019698 starch Nutrition 0.000 description 1
- 239000008107 starch Substances 0.000 description 1
- 125000004079 stearyl group Chemical group [H]C([*])([H])C([H])([H])C([H])([H])C([H])([H])C([H])([H])C([H])([H])C([H])([H])C([H])([H])C([H])([H])C([H])([H])C([H])([H])C([H])([H])C([H])([H])C([H])([H])C([H])([H])C([H])([H])C([H])([H])C([H])([H])[H] 0.000 description 1
- 238000003756 stirring Methods 0.000 description 1
- LXEJRKJRKIFVNY-UHFFFAOYSA-N terephthaloyl chloride Chemical compound ClC(=O)C1=CC=C(C(Cl)=O)C=C1 LXEJRKJRKIFVNY-UHFFFAOYSA-N 0.000 description 1
Classifications
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P20/00—Technologies relating to chemical industry
- Y02P20/50—Improvements relating to the production of bulk chemicals
- Y02P20/52—Improvements relating to the production of bulk chemicals using catalysts, e.g. selective catalysts
Landscapes
- Low-Molecular Organic Synthesis Reactions Using Catalysts (AREA)
- 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、マレイン酸モノア
ルキルエステルを異性化して、高品質のフマル酸モノア
ルキルエステルおよびそのナトリウム塩を高収率で製造
する方法に関する。The present invention relates to a method for isomerizing a monoalkyl maleate to produce a high-quality monoalkyl fumarate and its sodium salt in high yield.
【0002】[0002]
【従来の技術】フマル酸モノアルキルエステルは、抗菌
剤および種々の化合物の中間体として有用である。殊に
その金属塩(例えばナトリウム塩)は、でん粉の改質
剤、医薬品や栄養剤の錠剤のための表面潤滑剤として有
用である。2. Description of the Related Art Monoalkyl fumarate is useful as an antibacterial agent and as an intermediate of various compounds. In particular, the metal salts (eg, sodium salts) are useful as starch modifiers, surface lubricants for pharmaceutical and nutritional tablets.
【0003】フマル酸モノアルキルエステルを製造する
には、脂肪族アルコールとフマル酸またはフマル酸クロ
ライドを反応させる方法が一般的である。しかしフマル
酸を使用する場合、反応が遅く低収率であり、モノアル
キルエステルを選択的に得ることは困難である。一方フ
マル酸クロライドを使用すると、反応は速やかに進行す
るが、ジアルキルエステルの生成が避けられず、モノア
ルキルエステルの選択率は低くなる。[0003] In order to produce monoalkyl fumarate, a method is generally used in which an aliphatic alcohol is reacted with fumaric acid or fumaric acid chloride. However, when fumaric acid is used, the reaction is slow and the yield is low, and it is difficult to selectively obtain a monoalkyl ester. On the other hand, when fumaric acid chloride is used, the reaction proceeds rapidly, but the formation of dialkyl esters is unavoidable, and the selectivity of monoalkyl esters is lowered.
【0004】またマレイン酸モノアルキルエステルを触
媒の存在下、異性化させることによって対応するフマル
酸モノアルキルエステルを得る方法が提案されている
(米国特許第3953616号明細書)。この原料とし
てのマレイン酸モノアルキルエステルは、無水マレイン
酸と脂肪族アルコールとの反応により比較的容易に製造
することができる。A method for obtaining the corresponding monoalkyl fumarate by isomerizing the monoalkyl maleate in the presence of a catalyst has been proposed (US Pat. No. 3,953,616). Monoalkyl maleate as this raw material can be produced relatively easily by reacting maleic anhydride with an aliphatic alcohol.
【0005】前記提案方法において、異性化触媒として
カルボン酸クロライドまたはラジカル発生剤とハロゲン
が使用される。また異性化は無溶媒下あるいはハロゲン
化炭化水素溶媒を使用して行われる。無溶媒下では反応
をスムースに実施することは困難でありまた高純度のフ
マル酸モノアルキルエステルを得ることは容易ではな
い。ハロゲン化炭化水素を溶媒として使用した場合、環
境衛生上好ましくなく、その上目的とするフマル酸モノ
アルキルエステル中に溶媒が混入することは避けられ
ず、一方その除去には煩雑な手段を必要とする。In the above proposed method, carboxylic acid chloride or a radical generator and a halogen are used as the isomerization catalyst. The isomerization is carried out without a solvent or using a halogenated hydrocarbon solvent. It is difficult to carry out the reaction smoothly in the absence of a solvent, and it is not easy to obtain a high-purity monoalkyl fumarate. When a halogenated hydrocarbon is used as a solvent, it is not preferable from the viewpoint of environmental hygiene and, furthermore, it is inevitable that the solvent is mixed into the intended monoalkyl fumarate, while a complicated means is required for its removal. I do.
【0006】[0006]
【発明が解決しようとする課題】そこで本発明は、望ま
しくないハロゲン化炭化水素溶媒を使用しないで、高品
質のフマル酸モノアルキルエステルを高収率で得ること
を目的とする。The object of the present invention is therefore to obtain high-quality monoalkyl fumarate in high yields without using undesired halogenated hydrocarbon solvents.
【0007】[0007]
【課題を解決するための手段】本発明者らは、前記本発
明の目的を達成するため研究を進めたところ、触媒とし
てカルボン酸クロライドを使用し、溶媒として特定の芳
香族炭化水素を使用して異性化反応を行うと、反応が速
やかに進み、目的物を高収率で得ることができるばかり
でなく、未反応原料や他の不純物が溶媒中に溶解して除
去し易くなり、結果として高品質の目的物が得られるこ
とが見出され、本発明に到達した。Means for Solving the Problems The present inventors have conducted research to achieve the object of the present invention. As a result, the present inventors have used carboxylic acid chloride as a catalyst and specific aromatic hydrocarbons as a solvent. When the isomerization reaction is performed, the reaction proceeds promptly, and not only can the desired product be obtained in high yield, but also unreacted raw materials and other impurities are easily dissolved and removed in the solvent, and as a result, It has been found that a high quality object can be obtained, and the present invention has been achieved.
【0008】すなわち、本発明は、マレイン酸モノアル
キルエステルをカルボン酸クロライドの存在下で異性化
して対応するフマル酸モノアルキルエステルを製造する
方法において該異性化反応を、トルエンおよびキシレン
よりなる群から選ばれた少なくとも一種の芳香族炭化水
素媒体中で行うことを特徴とするフマル酸モノアルキル
エステルの製造法である。以下、さらに詳細に本発明を
説明する。Specifically, the present invention provides a method for producing a corresponding monoalkyl fumarate by isomerizing a monoalkyl maleate in the presence of a carboxylic acid chloride, wherein the isomerization reaction is carried out from the group consisting of toluene and xylene. A method for producing a monoalkyl fumarate, which is carried out in at least one selected aromatic hydrocarbon medium. Hereinafter, the present invention will be described in more detail.
【0009】本発明の異性化に使用されるマレイン酸モ
ノアルキルエステルは、炭素数10〜20の脂肪族アル
コール、好ましくは炭素数14〜18の脂肪族アルコー
ルと無水マレイン酸とのエステルである。具体的な態様
としては、テトラデシルアルコール、セチルアルコール
およびステアリルアルコールと無水マレイン酸とをほぼ
等モルの割合で反応させることによって得ることができ
る。The monoalkyl maleate used in the isomerization of the present invention is an ester of an aliphatic alcohol having 10 to 20 carbon atoms, preferably an aliphatic alcohol having 14 to 18 carbon atoms and maleic anhydride. As a specific embodiment, it can be obtained by reacting tetradecyl alcohol, cetyl alcohol, and stearyl alcohol with maleic anhydride in an approximately equimolar ratio.
【0010】このエステル化工程は、例えば、ベンゼ
ン、トルエンまたはキシレンのような芳香族炭化水素溶
媒中、無水の条件下で、40〜150℃、好ましくは5
0〜140℃の温度で実施される。好ましい溶媒は、ト
ルエンまたはキシレンである。This esterification step is carried out, for example, in an aromatic hydrocarbon solvent such as benzene, toluene or xylene under anhydrous conditions at 40 to 150 ° C., preferably 5 to 150 ° C.
It is carried out at a temperature of 0 to 140C. Preferred solvents are toluene or xylene.
【0011】前記エステル化工程により、高収率により
目的とするマレイン酸モノアルキルエステルが得られ
る。得られたマレイン酸モノアルキルエステルは、望ま
しくは反応混合液を冷却して濾過することにより、高純
度のエステルを得ることができる。[0011] By the esterification step, the desired monoalkyl maleate is obtained in high yield. The obtained monoalkyl maleate is desirably cooled and filtered to obtain a high-purity ester.
【0012】得られたマレイン酸モノアルキルエステル
は、次に異性化してフマル酸モノアルキルエステルとす
る。この異性化工程は、カルボン酸クロライドを触媒と
し、トルエンおよびキシレンよりなる群から選ばれた少
なくとも一種の芳香族炭化水素溶媒中で実施される。The obtained monoalkyl maleate is then isomerized to monoalkyl fumarate. This isomerization step is carried out in at least one aromatic hydrocarbon solvent selected from the group consisting of toluene and xylene, using carboxylic acid chloride as a catalyst.
【0013】異性化工程において、触媒としてのカルボ
ン酸クロライドは脂肪族または芳香族カルボン酸のクロ
ライドであり、具体的にはシュウ酸ジクロライド、フマ
ル酸ジクロライド、モノアルキル(例えばテトラデシ
ル、セチル、ステアリル)フマル酸クロライド、アジピ
ン酸ジクロライド、安息香酸クロライド、テレフタル酸
ジクロライド等が好適である。In the isomerization step, the carboxylic acid chloride as a catalyst is a chloride of an aliphatic or aromatic carboxylic acid, and specifically, oxalic acid dichloride, fumaric acid dichloride, monoalkyl (eg, tetradecyl, cetyl, stearyl) fumaric acid Acid chloride, adipic dichloride, benzoic chloride, terephthalic dichloride and the like are preferred.
【0014】カルボン酸クロライドは、マレイン酸モノ
アルキルエステル100重量部当たり、0.05〜5重
量部、好ましくは0.1〜3重量部の割合で使用するの
が適当である。The carboxylic acid chloride is used in an amount of 0.05 to 5 parts by weight, preferably 0.1 to 3 parts by weight, per 100 parts by weight of the monoalkyl maleate.
【0015】異性化工程において使用される溶媒は、ト
ルエンまたはキシレンであり、これらは混合物であって
もよく、この溶媒は、マレイン酸モノアルキルエステル
に対して1〜20重量倍、好ましくは1〜10重量倍使
用される。異性化反応は50〜150℃、好ましくは8
0〜120℃の温度で実施するのが有利であり、反応時
間は2〜20時間で充分である。The solvent used in the isomerization step is toluene or xylene, which may be a mixture, and the solvent is used in an amount of 1 to 20 times by weight, preferably 1 to 20 times by weight of the monoalkyl maleate. Used 10 times by weight. The isomerization reaction is carried out at 50-150 ° C., preferably 8
The reaction is advantageously carried out at a temperature of from 0 to 120 ° C., a reaction time of from 2 to 20 hours being sufficient.
【0016】異性化工程により得られた反応混合物は、
冷却することにより、フマル酸モノアルキルエステルを
析出させ、析出物の濾過により分離することができる。
かくして未反応原料や不純物は、溶媒中に除去されるこ
とになる。析出物は、芳香族炭化水素溶媒で洗浄するこ
とにより、より高純度のフマル酸モノアルキルエステル
とすることができる。The reaction mixture obtained by the isomerization step is
By cooling, the monoalkyl fumarate is precipitated, and the precipitate can be separated by filtration.
Thus, unreacted raw materials and impurities are removed in the solvent. The precipitate can be made into a higher purity monoalkyl fumarate by washing with an aromatic hydrocarbon solvent.
【0017】得られたフマル酸モノアルキルエステル
は、それ自体製品としてあるいは中間体として利用する
ことができる。また所望によりフマル酸モノアルキルエ
ステルは、中和してナトリウム塩とすることができる。The obtained monoalkyl fumarate can be used as a product per se or as an intermediate. If desired, the monoalkyl fumarate can be neutralized to a sodium salt.
【0018】この中和工程において水酸化ナトリウムを
水溶液として使用し、アセトン、メチルエチルケトンの
如き有機溶媒中で反応させることが望ましい。水酸化ナ
トリウムはフマル酸モノアルキルエステルとほぼ等モル
使用するのが有利である。過剰使用すると副反応が起こ
り望ましくない。中和反応は10〜60℃、好ましくは
15〜55℃の範囲で実施するのが適当である。反応終
了後、フマル酸モノアルキルエステルのナトリウム塩
は、濾過して分離することができる。In the neutralization step, it is desirable to use sodium hydroxide as an aqueous solution and to carry out the reaction in an organic solvent such as acetone or methyl ethyl ketone. The sodium hydroxide is advantageously used in approximately equimolar amounts with the monoalkyl fumarate. If used excessively, side reactions occur, which is not desirable. The neutralization reaction is suitably carried out at a temperature in the range of 10 to 60C, preferably 15 to 55C. After completion of the reaction, the sodium salt of fumaric acid monoalkyl ester can be separated by filtration.
【0019】[0019]
【実施例】実施例の「部」とあるのは「重量部」を意味
する。 実施例1 冷却器、攪拌機を付した反応器にマレイン酸モノステア
リルエステル200部、トルエン300部、フマル酸ジ
クロライド2部を入れ、90〜100℃で5時間加熱し
た。その後室温まで冷却して析出した結晶を濾別し、ト
ルエン300部で洗浄した後減圧下50℃で3時間乾燥
した。得られたフマル酸モノステアリルエステルの収量
181部、収率90.5%、純度99.8%であった。EXAMPLES In the examples, "parts" means "parts by weight". Example 1 A reactor equipped with a condenser and a stirrer was charged with 200 parts of monostearyl maleate, 300 parts of toluene and 2 parts of fumaric acid dichloride, and heated at 90 to 100 ° C for 5 hours. After cooling to room temperature, the precipitated crystals were separated by filtration, washed with 300 parts of toluene, and dried under reduced pressure at 50 ° C. for 3 hours. The yield of the obtained monostearyl fumarate was 181 parts, the yield was 90.5%, and the purity was 99.8%.
【0020】比較例 実施例1と同じ反応器にマレイン酸モノステアリルエス
テル200部、フマル酸ジクロライド2部および四塩化
炭素800部を入れ、実施例1と同様、反応および処理
した。結晶を四塩化炭素300部で洗浄した後実施例1
と同様に乾燥し170部(収率85%)を得た。純度9
9.0%であった。Comparative Example 200 parts of monostearyl maleate, 2 parts of fumaric acid dichloride and 800 parts of carbon tetrachloride were placed in the same reactor as in Example 1, and the reaction and treatment were carried out in the same manner as in Example 1. Example 1 after washing the crystals with 300 parts of carbon tetrachloride
In the same manner as in the above, 170 parts (yield 85%) were obtained. Purity 9
It was 9.0%.
【0021】実施例2〜6 実施例1と同じ反応器に下記表に示すものマレイン酸モ
ノアルキルエステルおよびトルエンまたはキシレンを表
に示す重量入れ、温度90〜100℃で5時間加熱し
た。反応液を冷却し生成した結晶を濾別し、結晶を実施
例1と同様、乾燥して目的とするフマル酸モノアルキル
エステルを得た。その結果を表に示した。Examples 2 to 6 The same reactor as in Example 1 was charged with the monoalkyl maleate and toluene or xylene shown in the table below and heated at a temperature of 90 to 100 ° C. for 5 hours. The reaction solution was cooled, and the generated crystals were separated by filtration. The crystals were dried in the same manner as in Example 1 to obtain the desired monoalkyl fumarate. The results are shown in the table.
【0022】[0022]
【表1】 [Table 1]
【0023】実施例7 [マレイン酸モノステアリルエステルの合成]冷却器、
攪拌機を付した反応器に無水マレイン酸38部、ステア
リルアルコール105部およびトルエン175部を仕込
み、100℃で2時間攪拌下反応させた後、室温まで冷
却した。Example 7 [Synthesis of maleic acid monostearyl ester]
A reactor equipped with a stirrer was charged with 38 parts of maleic anhydride, 105 parts of stearyl alcohol, and 175 parts of toluene, reacted at 100 ° C. for 2 hours with stirring, and then cooled to room temperature.
【0024】[フマル酸モノステアリルエステルの合
成]上記の反応液にフマル酸ジクロライド1.3部を加
え90〜100℃で5時間加熱した。その後室温まで冷
却して析出した。結晶を濾別しトルエン190部で洗浄
した後、減圧下40℃で3時間乾燥した。得られたフマ
ル酸モノステアリルエステルの収量130部、収率91
%、純度99.8%であった。[Synthesis of Monostearyl Fumarate] 1.3 parts of fumaric acid dichloride was added to the above reaction solution, and the mixture was heated at 90 to 100 ° C. for 5 hours. Thereafter, the solution was cooled to room temperature and precipitated. The crystals were separated by filtration, washed with 190 parts of toluene, and dried under reduced pressure at 40 ° C. for 3 hours. The yield of the obtained monostearyl fumarate was 130 parts, and the yield was 91.
%, Purity 99.8%.
【0025】[フマル酸モノステアリルエステルのナト
リウム塩の合成]上記フマル酸モノステアリルエステル
130部とアセトン575部を攪拌機、冷却器を付した
反応器入れ、15%NaOH水94部を40℃で4時間
かけて添加して中和反応させた。反応後室温まで冷却し
て濾別し、アセトン100部で洗浄して80℃で5時間
減圧乾燥した。収量124部、収率90%、純度99.
5%であった。[Synthesis of sodium salt of monostearyl fumarate] 130 parts of the above monostearyl fumarate and 575 parts of acetone were placed in a reactor equipped with a stirrer and a cooler, and 94 parts of 15% aqueous NaOH were added at 40 ° C for 4 hours. It was added over time to perform a neutralization reaction. After the reaction, the mixture was cooled to room temperature, separated by filtration, washed with 100 parts of acetone, and dried under reduced pressure at 80 ° C. for 5 hours. Yield 124 parts, yield 90%, purity 99.
5%.
【0026】[0026]
【発明の効果】マレイン酸モノアルキルエステルの異性
化反応によって高品質、高収率の対応するフマル酸モノ
アルキルエステルが容易に得られる。According to the present invention, the corresponding monoalkyl fumarate of high quality and high yield can be easily obtained by the isomerization reaction of the monoalkyl maleate.
Claims (4)
ボン酸クロライドの存在下で異性化して対応するフマル
酸モノアルキルエステルを製造する方法において該異性
化反応を、トルエンおよびキシレンよりなる群から選ば
れた少なくとも一種の芳香族炭化水素媒体中で行うこと
を特徴とするフマル酸モノアルキルエステルの製造法。1. A method for producing a corresponding monoalkyl fumarate by isomerizing a monoalkyl maleate in the presence of a carboxylic acid chloride, wherein the isomerization reaction is performed by at least one selected from the group consisting of toluene and xylene. A process for producing a monoalkyl fumarate, which is carried out in a kind of aromatic hydrocarbon medium.
フマル酸モノアルキルエステルにおけるアルキル基が、
炭素数14〜18のアルキル基である請求項1記載の製
造法。2. An alkyl group in a monoalkyl maleate and a monoalkyl fumarate is:
The method according to claim 1, wherein the alkyl group has 14 to 18 carbon atoms.
芳香族のモノカルボン酸あるいはジカルボン酸のクロラ
イドである請求項1記載の製造法。3. The process according to claim 1, wherein the carboxylic acid chloride is an aliphatic or aromatic monocarboxylic acid or dicarboxylic acid chloride.
等モルの割合で反応させてマレイン酸モノアルキルエス
テルを得るエステル化工程 (2)得られたマレイン酸モノアルキルエステルを、カ
ルボン酸クロライドの存在下、トルエンおよびキシレン
よりなる群から選ばれた少なくとも一種の芳香族炭化水
素媒体中、異性化させてフマル酸モノアルキルエステル
を得る異性化工程および (3)次いで得られたフマル酸モノアルキルエステルを
水酸化ナトリウム含有水性媒体中で中和させて、フマル
酸モノアルキルエステルのナトリウム塩を得る中和工程 よりなることを特徴とするフマル酸モノアルキルエステ
ルのナトリウム塩の製造法。4. The following step (1) Esterification step of reacting maleic anhydride with an aliphatic monoalcohol in a substantially equimolar ratio to obtain a monoalkyl maleate ester. (2) Obtained monoalkyl maleate ester. Isomerization in the presence of a carboxylic acid chloride in at least one aromatic hydrocarbon medium selected from the group consisting of toluene and xylene to obtain a monoalkyl fumarate; and (3) Producing a sodium salt of a monoalkyl fumarate by neutralizing the monoalkyl fumarate in an aqueous medium containing sodium hydroxide to obtain a sodium salt of the monoalkyl fumarate. Law.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP34229599A JP2001158760A (en) | 1999-12-01 | 1999-12-01 | Method of producing fumaric monoalkyl ester and sodium salt thereof |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP34229599A JP2001158760A (en) | 1999-12-01 | 1999-12-01 | Method of producing fumaric monoalkyl ester and sodium salt thereof |
Publications (1)
Publication Number | Publication Date |
---|---|
JP2001158760A true JP2001158760A (en) | 2001-06-12 |
Family
ID=18352633
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP34229599A Withdrawn JP2001158760A (en) | 1999-12-01 | 1999-12-01 | Method of producing fumaric monoalkyl ester and sodium salt thereof |
Country Status (1)
Country | Link |
---|---|
JP (1) | JP2001158760A (en) |
Cited By (8)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO2014197860A1 (en) * | 2013-06-07 | 2014-12-11 | Xenoport, Inc. | Method of making monomethyl fumarate |
US9416096B2 (en) | 2013-09-06 | 2016-08-16 | Xenoport, Inc. | Crystalline forms of (N,N-Diethylcarbamoyl)methyl methyl (2E)but-2-ene-1,4-dioate, methods of synthesis and use |
US9421182B2 (en) | 2013-06-21 | 2016-08-23 | Xenoport, Inc. | Cocrystals of dimethyl fumarate |
US9452972B2 (en) | 2008-08-19 | 2016-09-27 | Xenoport, Inc. | Methods of using prodrugs of methyl hydrogen fumarate and pharmaceutical compositions thereof |
US9597292B2 (en) | 2012-08-22 | 2017-03-21 | Xenoport, Inc. | Oral dosage forms of methyl hydrogen fumarate and prodrugs thereof |
US9999672B2 (en) | 2014-03-24 | 2018-06-19 | Xenoport, Inc. | Pharmaceutical compositions of fumaric acid esters |
US10179118B2 (en) | 2013-03-24 | 2019-01-15 | Arbor Pharmaceuticals, Llc | Pharmaceutical compositions of dimethyl fumarate |
US10945984B2 (en) | 2012-08-22 | 2021-03-16 | Arbor Pharmaceuticals, Llc | Methods of administering monomethyl fumarate and prodrugs thereof having reduced side effects |
-
1999
- 1999-12-01 JP JP34229599A patent/JP2001158760A/en not_active Withdrawn
Cited By (13)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US9452972B2 (en) | 2008-08-19 | 2016-09-27 | Xenoport, Inc. | Methods of using prodrugs of methyl hydrogen fumarate and pharmaceutical compositions thereof |
US9597292B2 (en) | 2012-08-22 | 2017-03-21 | Xenoport, Inc. | Oral dosage forms of methyl hydrogen fumarate and prodrugs thereof |
US10945984B2 (en) | 2012-08-22 | 2021-03-16 | Arbor Pharmaceuticals, Llc | Methods of administering monomethyl fumarate and prodrugs thereof having reduced side effects |
US10716760B2 (en) | 2012-08-22 | 2020-07-21 | Arbor Pharmaceuticals, Llc | Oral dosage forms of methyl hydrogen fumarate and prodrugs thereof |
US10179118B2 (en) | 2013-03-24 | 2019-01-15 | Arbor Pharmaceuticals, Llc | Pharmaceutical compositions of dimethyl fumarate |
US11938111B2 (en) | 2013-03-24 | 2024-03-26 | Arbor Pharmaceuticals, Llc | Pharmaceutical compositions of dimethyl fumarate |
US9302977B2 (en) | 2013-06-07 | 2016-04-05 | Xenoport, Inc. | Method of making monomethyl fumarate |
WO2014197860A1 (en) * | 2013-06-07 | 2014-12-11 | Xenoport, Inc. | Method of making monomethyl fumarate |
US9421182B2 (en) | 2013-06-21 | 2016-08-23 | Xenoport, Inc. | Cocrystals of dimethyl fumarate |
US9682057B2 (en) | 2013-09-06 | 2017-06-20 | Xenoport, Inc. | Crystalline forms of (N,N-Diethylcarbamoyl)methyl methyl (2E)but-2-ene-1,4-dioate, methods of synthesis and use |
US9416096B2 (en) | 2013-09-06 | 2016-08-16 | Xenoport, Inc. | Crystalline forms of (N,N-Diethylcarbamoyl)methyl methyl (2E)but-2-ene-1,4-dioate, methods of synthesis and use |
US9999672B2 (en) | 2014-03-24 | 2018-06-19 | Xenoport, Inc. | Pharmaceutical compositions of fumaric acid esters |
US11135296B2 (en) | 2014-03-24 | 2021-10-05 | Arbor Pharmaceuticals, Llc | Pharmaceutical compositions of fumaric acid esters |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
JP2001158760A (en) | Method of producing fumaric monoalkyl ester and sodium salt thereof | |
JPH0649009A (en) | Production of 2,5-diphenylaminoterephthalic acid and its derivative | |
SK8997A3 (en) | Process for the preparation of 5-amino-2,4,6-triiodine-1,3- -benzenedicarboxylic acid | |
WO1992018449A1 (en) | Selective hydroxylation of phenol or phenolic ethers | |
JPS6241662B2 (en) | ||
TWI333944B (en) | Process for preparing (s)-(+)-2-(substituted phenyl)-2-hydroxy-ethyl carbamates | |
JP3909094B2 (en) | Process for producing 1-aminocyclopropanecarboxylic acid hydrochloride | |
US2763683A (en) | Preparation of salicylanilide | |
KR100301756B1 (en) | Manufacturing method of 0,0'- diacyl tartaric anhydride and manufacturing method of 0,0'- diacyl tartaric acid | |
JP4213244B2 (en) | Purification method of keto acid | |
JP4126729B2 (en) | Method for producing phthalides | |
JP3199618B2 (en) | Method for producing 1,4-dihydroxy-2-naphthoic acid | |
JP3945610B2 (en) | Process for producing fumaric acid monoesters and alkali metal salts thereof | |
JP2747780B2 (en) | Method for producing asymmetric diester | |
JP2896797B2 (en) | Method for producing α-bromoisovalerylurea | |
JPH0276836A (en) | Production of metal ether carboxylate | |
EP0563986A2 (en) | Process for selective hydrodefluorination | |
JPH11279121A (en) | Production of alkyl beta-alkoxypropionate | |
US2623065A (en) | Methods for producing alkoxynaphthoylalkanoic acids | |
US4434104A (en) | Preparation of high purity di-lower alkyl naphthalenedisulfonates | |
JPH06172257A (en) | Production of bis@(3754/24)p-hydroxyphenyl)acetic acid | |
JPS645017B2 (en) | ||
JPH06107599A (en) | Production of aromatic dicarboxlic acid monoester compounds | |
JPH11292824A (en) | Production of alpha-hydroxycarboxylate | |
CN113045381A (en) | Preparation method of fluorine-containing dihydric alcohol |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
A711 | Notification of change in applicant |
Free format text: JAPANESE INTERMEDIATE CODE: A712 Effective date: 20050826 |
|
A521 | Written amendment |
Free format text: JAPANESE INTERMEDIATE CODE: A821 Effective date: 20050826 |
|
A300 | Withdrawal of application because of no request for examination |
Free format text: JAPANESE INTERMEDIATE CODE: A300 Effective date: 20070206 |