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JPH05125028A - Production of carbonic acid ester - Google Patents

Production of carbonic acid ester

Info

Publication number
JPH05125028A
JPH05125028A JP3311560A JP31156091A JPH05125028A JP H05125028 A JPH05125028 A JP H05125028A JP 3311560 A JP3311560 A JP 3311560A JP 31156091 A JP31156091 A JP 31156091A JP H05125028 A JPH05125028 A JP H05125028A
Authority
JP
Japan
Prior art keywords
acid
carboxylic acid
alkali metal
neutralizing
ester
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
Application number
JP3311560A
Other languages
Japanese (ja)
Inventor
Masahiko Kanda
昌彦 神田
Chuzo Watanabe
忠三 渡辺
Haruo Morita
治生 森田
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
YOTSUKAICHI GOSEI KK
Original Assignee
YOTSUKAICHI GOSEI KK
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by YOTSUKAICHI GOSEI KK filed Critical YOTSUKAICHI GOSEI KK
Priority to JP3311560A priority Critical patent/JPH05125028A/en
Publication of JPH05125028A publication Critical patent/JPH05125028A/en
Pending legal-status Critical Current

Links

Classifications

    • YGENERAL 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
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02PCLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P20/00Technologies relating to chemical industry
    • Y02P20/50Improvements relating to the production of bulk chemicals
    • Y02P20/52Improvements relating to the production of bulk chemicals using catalysts, e.g. selective catalysts

Landscapes

  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
  • Low-Molecular Organic Synthesis Reactions Using Catalysts (AREA)

Abstract

PURPOSE:To obtain the subject compound in improved workability while suppressing the foaming by reacting a lower aliphatic carboxylic acid with a specific aromatic-substituted alcohol in the presence of an acid catalyst, adding a specific alcohol to the reactional mixture and neutralizing the reactional liquid with an alkali metal carbonate, etc. CONSTITUTION:A carboxylic acid ester can be produced in high workability while suppressing the foaming caused by the carbon dioxide gas generated in neutralization reaction by esterifying a lower aliphatic carboxylic acid (e.g. propionic acid) or its acid anhydride with an aromatic-substituted alcohol of formula (X is carbamoyl, cyano or nitro) [e.g. 4-(2-hydroxyethoxy)benzamide] in the presence of an acid catalyst (e.g. p-toluenesulfonic acid) in a toluene solvent under refluxing the toluene for 5hr, adding a 6-12C aliphatic alcohol (e.g. 1-hexanol) to the reactional liquid containing the produced ester compound and neutralizing the mixture with an alkali metal carbonate or alkali metal bicarbonate (e.g. sodium carbonate).

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【産業上の利用分野】本発明は、カルボン酸エステルの
製造法に関し、特に酸触媒の存在下、低級脂肪族カルボ
ン酸又はその酸無水物と芳香族置換アルコールとのエス
テル化反応によって得られた反応液中に存在する酸性物
質の中和方法の改良されたカルボン酸エステルの製造法
に関するものである。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method for producing a carboxylic acid ester, which is obtained by an esterification reaction of a lower aliphatic carboxylic acid or an acid anhydride thereof with an aromatic substituted alcohol in the presence of an acid catalyst. The present invention relates to a method for producing a carboxylic acid ester having an improved method for neutralizing an acidic substance present in a reaction solution.

【0002】本発明で得られる製品エステルは、高沸点
及び高融点の物理的特性を有しており、特殊な溶媒とし
て用いることができる。
The product ester obtained in the present invention has physical properties of high boiling point and high melting point and can be used as a special solvent.

【0003】[0003]

【従来の技術】酸触媒の存在下で脂肪族カルボン酸又は
脂肪族カルボン酸無水物と芳香族置換アルコールとのエ
ステル化反応によって得られる反応液中には、酸性物質
として未反応カルボン酸と酸触媒とが共存している。こ
の酸性物質を除去するため、通常は廃水のpH調整の容易
なアルカリ金属の炭酸塩又は重炭酸塩の水溶液を用いて
中和処理をした後、エステル層と水層とに分液し、その
後再度エステル層を水を用いて水洗処理を行う。この場
合、中和反応により発生する二酸化炭素により激しく発
泡するため、中和操作は極めて煩雑となり、特に大規模
な工業生産の場合には大きな問題となる。
2. Description of the Related Art In a reaction solution obtained by an esterification reaction of an aliphatic carboxylic acid or an aliphatic carboxylic acid anhydride with an aromatic substituted alcohol in the presence of an acid catalyst, an unreacted carboxylic acid and an acid are added as acidic substances. Coexist with a catalyst. In order to remove this acidic substance, neutralization treatment is usually performed using an aqueous solution of an alkali metal carbonate or bicarbonate in which the pH of the wastewater is easily adjusted, and then liquid separation into an ester layer and a water layer is performed. The ester layer is washed again with water. In this case, since carbon dioxide generated by the neutralization reaction causes vigorous bubbling, the neutralization operation becomes extremely complicated and becomes a serious problem particularly in the case of large-scale industrial production.

【0004】この発泡問題を解決する方法として、例え
ば特開昭 59-127692号公報では、炭酸ナトリウム、重炭
酸ナトリウムなどの金属炭酸塩あるいは重炭酸塩に、0.
01重量%以上のシリコン系、鉱油系などの消泡剤を添加
して低発泡性中和剤を調製して酸性廃液の中和に用いる
という方法が提案されている。
As a method for solving this foaming problem, for example, in JP-A-59-127692, metal carbonates or bicarbonates such as sodium carbonate, sodium bicarbonate, etc.
A method has been proposed in which a low-foaming neutralizing agent is prepared by adding an antifoaming agent such as 01% by weight or more of a silicon-based or mineral oil-based anti-foaming agent and used for neutralizing an acidic waste liquid.

【0005】しかしながら、この方法を本発明のカルボ
ン酸エステルの製造の酸性物質の中和除去の方法に適用
しようとすると、これらの消泡剤は水にはほとんど溶解
しないため、エステルを含む有機層に消泡剤が混入し、
結果的には製品エステルに残留してカルボン酸エステル
の純度低下及び製品としての機能低下をもたらす。
However, when this method is applied to the method for neutralizing and removing the acidic substance in the production of the carboxylic acid ester of the present invention, since these antifoaming agents are hardly dissolved in water, the organic layer containing the ester is depleted. Defoamer mixed in,
As a result, it remains in the product ester, resulting in a decrease in the purity of the carboxylic acid ester and a decrease in the function of the product.

【0006】[0006]

【発明が解決しようとする課題】この様な状況下、工業
的に容易な方法にて、エステル化反応によって得られた
反応液中に存在する酸性物質の中和を行い、且つ目的物
のカルボン酸エステルの純度低下を防ぐことが課題とな
っていた。
Under such circumstances, the acidic substance present in the reaction solution obtained by the esterification reaction is neutralized by an industrially easy method, and the desired carvone is obtained. There has been a problem to prevent the purity of the acid ester from decreasing.

【0007】[0007]

【課題を解決するための手段】かかる課題を解決するた
め、本発明者らはカルボン酸エステルを製造するに際
し、該エステルを含む反応液の中和処理の方法について
鋭意研究した結果、反応液に脂肪族アルコール化合物を
添加した後、アルカリ金属炭酸塩又はアルカリ金属重炭
酸塩の水溶液で中和することにより、発泡量が大幅に減
少することを発見して本発明を完成した。
In order to solve the above problems, the inventors of the present invention have diligently studied a method of neutralizing a reaction solution containing a carboxylic acid ester when producing the carboxylic acid ester. The present invention has been completed by discovering that the amount of foaming is significantly reduced by neutralizing with an aqueous solution of an alkali metal carbonate or an alkali metal bicarbonate after adding an aliphatic alcohol compound.

【0008】すなわち本発明は、酸触媒の存在下に低級
脂肪族カルボン酸又はその酸無水物と下記の一般式で示
される芳香族置換アルコールとのエステル化反応におい
て、生成エステル化合物を含む反応液をアルカリ金属炭
酸塩又はアルカリ金属重炭酸塩の水溶液を用いて中和す
るに際して、中和前に炭素数が 6〜12の脂肪族アルコー
ル化合物を添加することを特徴とするカルボン酸エステ
ルの製造法である。
That is, the present invention relates to a reaction solution containing an ester compound produced in an esterification reaction of a lower aliphatic carboxylic acid or its acid anhydride with an aromatic substituted alcohol represented by the following general formula in the presence of an acid catalyst. A method for producing a carboxylic acid ester, which comprises adding an aliphatic alcohol compound having a carbon number of 6 to 12 before neutralization with an aqueous solution of an alkali metal carbonate or an alkali metal bicarbonate. Is.

【0009】[0009]

【化1】[Chemical 1]

【0010】(式中Xはカルバモイル基、シアノ基、ニ
トロ基のいずれか一つを示す。)
(In the formula, X represents one of a carbamoyl group, a cyano group and a nitro group.)

【0011】本発明で用いられる低級脂肪族カルボン酸
は、酢酸、プロピオン酸、酪酸であり、酸無水物として
は無水酢酸、無水プロピオン酸、無水酪酸のいずれかが
用いられる。
The lower aliphatic carboxylic acids used in the present invention are acetic acid, propionic acid and butyric acid, and any of acetic anhydride, propionic anhydride and butyric anhydride can be used as the acid anhydride.

【0012】上記一般式で示される芳香族置換アルコー
ルは、例えば 4-(2-ヒドロキシエトキシ)ベンズアミ
ド、2-( 2-ヒドロキシエトキシ)ベンゾニトリル、2-(
3-ニトロフェニルオキシ)エタノールなどである。
The aromatic substituted alcohol represented by the above general formula is, for example, 4- (2-hydroxyethoxy) benzamide, 2- (2-hydroxyethoxy) benzonitrile, 2- (2-
3-nitrophenyloxy) ethanol and the like.

【0013】酸触媒は、p-トルエンスルホン酸、エタン
スルホン酸、ベンゼンスルホン酸などの有機スルホン酸
であるが、一般的にp-トルエンスルホン酸が用いられ
る。
The acid catalyst is an organic sulfonic acid such as p-toluenesulfonic acid, ethanesulfonic acid and benzenesulfonic acid, but p-toluenesulfonic acid is generally used.

【00014】反応方法は常法でよく、カルボン酸及び
/又はカルボン酸無水物と芳香族置換アルコールとを溶
媒の存在下で反応させる。ここで、反応溶媒としては、
一般的なエステル化反応で用いられるベンゼンやトルエ
ンなどが用いられる。
The reaction method may be a conventional method, in which a carboxylic acid and / or a carboxylic acid anhydride and an aromatic substituted alcohol are reacted in the presence of a solvent. Here, as the reaction solvent,
Benzene, toluene, etc. used in general esterification reaction are used.

【0015】エステル化反応で得られた反応液中には、
目的エステル化合物のほかに、酸触媒とカルボン酸又は
カルボン酸無水物が芳香族置換アルコールに対して過剰
当量数(ここで当量とは酸塩基当量をさす。以下同
じ。)使用された場合には、未反応のカルボン酸も含ま
れている。
In the reaction solution obtained by the esterification reaction,
In addition to the target ester compound, when an acid catalyst and a carboxylic acid or a carboxylic acid anhydride are used in excess equivalent numbers (here, equivalents refer to acid-base equivalents. The same applies hereinafter) with respect to the aromatic substituted alcohol. It also contains unreacted carboxylic acid.

【0016】反応液中に存在するこれらの酸性物質の除
去は、反応液に脂肪族アルコールを加えた後、塩基性中
和剤を含む水溶液で中和処理を行い、生成した中和塩は
水層に溶解して目的エステルを含む有機層から分離され
る。
The removal of these acidic substances present in the reaction solution is carried out by adding an aliphatic alcohol to the reaction solution and then neutralizing the solution with an aqueous solution containing a basic neutralizing agent. It is dissolved in the layer and separated from the organic layer containing the desired ester.

【0017】脂肪族アルコール化合物は、炭素数が 6〜
12のアルコールであり、1-ヘキサノール、1-ヘプタノー
ル、2-エチルヘキサノール、2-メチル- 1-ヘプタノー
ル、3-エチル- 2-ノナノールなどが例示できる。炭素数
が 5以下のアルコールでは水に対する溶解度が高く、消
泡作用が小さく、単素数が12を超えるアルコールでは融
点が高くなり中和温度でも粘性が高く、抑泡作用が期待
されない。
The aliphatic alcohol compound has 6 to 6 carbon atoms.
Examples of the 12 alcohols include 1-hexanol, 1-heptanol, 2-ethylhexanol, 2-methyl-1-heptanol, 3-ethyl-2-nonanol and the like. Alcohols having 5 or less carbon atoms have high solubility in water and a small defoaming effect, and alcohols having a number of carbon atoms greater than 12 have a high melting point and a high viscosity even at the neutralization temperature, and are not expected to have a foam suppressing effect.

【0018】また、脂肪族アルコール化合物の反応液へ
の添加量は、反応溶媒に対し、 0.1〜5.0 重量%の範囲
が好ましい。添加量が少なすぎると中和反応で生じた二
酸化炭素による大量の発泡が避けられず、添加量が過剰
になると中和処理後、水層と該エステルを含む有機層と
の分離が困難になる。
The amount of the aliphatic alcohol compound added to the reaction solution is preferably 0.1 to 5.0% by weight based on the reaction solvent. If the addition amount is too small, a large amount of foaming due to carbon dioxide generated in the neutralization reaction cannot be avoided, and if the addition amount is excessive, it becomes difficult to separate the aqueous layer and the organic layer containing the ester after the neutralization treatment. ..

【0019】塩基性中和剤は、アルカリ金属炭酸塩及び
アルカリ金属重炭酸塩であり、アルカリ金属炭酸塩とし
ては、炭酸ナトリウム、炭酸カリウムなど、アルカリ金
属重炭酸塩としては、炭酸水素ナトリウム、炭酸水素カ
リウムなどが例としてあげられる。
The basic neutralizing agents are alkali metal carbonates and alkali metal bicarbonates. The alkali metal carbonates include sodium carbonate and potassium carbonate, and the alkali metal bicarbonates include sodium hydrogen carbonate and carbonate. Examples include potassium hydrogen.

【0020】塩基性中和剤の添加量は、反応液中の酸に
対し 1〜3倍当量の範囲が好ましい。中和剤の量が少な
すぎると、反応液中の酸性物質が充分に中和されず、製
品エステル中に不純物として混入する。中和剤の量が上
記範囲よりも過剰になると、中和後の有機層にアルカリ
金属が残存し、中和後の水洗回数を多くする必要が生
じ、工程時間が延びる。
The amount of the basic neutralizing agent added is preferably in the range of 1 to 3 times the equivalent of the acid in the reaction solution. If the amount of the neutralizing agent is too small, the acidic substance in the reaction solution is not sufficiently neutralized and is mixed in the product ester as an impurity. If the amount of the neutralizing agent exceeds the above range, the alkali metal remains in the organic layer after neutralization, and it becomes necessary to increase the number of times of washing with water after neutralization, which extends the process time.

【0021】塩基性中和剤の水溶液の濃度は、特に制限
しないが、 5〜20重量%が好ましい。濃度が高すぎると
中和塩などが系内に析出し、一方、濃度が低すぎると廃
水量が大幅に増加する。
The concentration of the aqueous solution of the basic neutralizing agent is not particularly limited, but is preferably 5 to 20% by weight. If the concentration is too high, neutralized salts and the like will precipitate in the system, while if the concentration is too low, the amount of wastewater will increase significantly.

【0022】中和温度は、特に制限しないが80℃以下が
よく、80℃以上では溶媒の沸騰が起こり始める。
The neutralization temperature is not particularly limited, but is preferably 80 ° C. or lower, and boiling of the solvent begins to occur at 80 ° C. or higher.

【0023】[0023]

【作用】炭素数が 5以下の低級アルコールについては発
生した泡を消す破泡作用はあるが、泡の発生自体をを抑
制する作用はないことが知られている。本発明における
炭素数 6〜12の脂肪族アルコールの消泡作用又は抑泡作
用の機構については必ずしも明らかではないが、水相と
有機相のと界面にアルコールが存在することによって界
面張力が低下し、泡の発生が抑制されるものと考えられ
る。
[Function] It is known that lower alcohols having a carbon number of 5 or less have a foam-breaking action of eliminating bubbles, but do not suppress the generation of bubbles themselves. The mechanism of the antifoaming action or the foam suppressing action of the aliphatic alcohol having 6 to 12 carbon atoms in the present invention is not necessarily clear, but the presence of alcohol at the interface between the aqueous phase and the organic phase lowers the interfacial tension. It is considered that the generation of bubbles is suppressed.

【0024】[0024]

【実施例】以下、本発明を実施例によって具体的に説明
するが、本発明はこれらの実施例に限定されるものでは
ない。
EXAMPLES The present invention will be specifically described below with reference to examples, but the present invention is not limited to these examples.

【0025】実施例 4-( 2-ヒドロキシエトキシ) ベンズアミド 45g (0.25当
量) 、p-トルエンスルホン酸9.5g (0.05当量)、プロピ
オン酸22.2g (0.3当量)及びトルエン250gを同時に仕込
み、トルエン還流下 5時間反応(反応温度 110℃)を行
った。
Example 4- (2-hydroxyethoxy) benzamide 45 g (0.25 equivalent), p-toluenesulfonic acid 9.5 g (0.05 equivalent), propionic acid 22.2 g (0.3 equivalent) and toluene 250 g were charged at the same time under toluene reflux. The reaction was carried out for 5 hours (reaction temperature 110 ° C).

【0026】反応液を 500mlのメスシリンダーに移し、
表1に示す添加剤を加え、70℃に保って攪拌しながら、
炭酸ナトリウム10.6g(0.2 当量)を水 90gに溶かした水
溶液で中和処理を行い、そのときの発泡量を測定した。
結果を表1に示す。
The reaction solution was transferred to a 500 ml measuring cylinder,
Add the additives shown in Table 1 and maintain at 70 ° C with stirring,
Neutralization treatment was carried out with an aqueous solution prepared by dissolving 10.6 g (0.2 equivalent) of sodium carbonate in 90 g of water, and the amount of foaming at that time was measured.
The results are shown in Table 1.

【0027】[0027]

【発明の効果】以上詳述したように、本発明は酸触媒の
存在下脂肪族カルボン酸又はその酸無水物と芳香族置換
アルコールからエステル化反応によってカルボン酸エス
テル製造するに際し、該エステル化合物を含む反応液を
アルカリ金属炭酸塩又はアルカリ金属重炭酸塩で中和す
る前に、反応液に脂肪族アルコール化合物を少量加える
ことにより、中和反応での二酸化炭素の発生による発泡
が抑制され、大幅な作業性の向上が達成できる。
As described above in detail, the present invention provides a method for producing a carboxylic acid ester by an esterification reaction from an aliphatic carboxylic acid or its acid anhydride and an aromatic substituted alcohol in the presence of an acid catalyst. Before neutralizing the reaction solution containing it with an alkali metal carbonate or an alkali metal bicarbonate, by adding a small amount of an aliphatic alcohol compound to the reaction solution, foaming due to the generation of carbon dioxide in the neutralization reaction is suppressed, It is possible to improve the workability.

【表1】 [Table 1]

───────────────────────────────────────────────────── フロントページの続き (51)Int.Cl.5 識別記号 庁内整理番号 FI 技術表示箇所 C07C 255/54 6917−4H // C07B 61/00 300 ─────────────────────────────────────────────────── ─── Continuation of the front page (51) Int.Cl. 5 Identification number Office reference number FI technical display location C07C 255/54 6917-4H // C07B 61/00 300

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】 酸触媒の存在下に低級脂肪族カルボン酸
又はその酸無水物と一般式 【化1】 (式中Xはカルバモイル基、シアノ基、ニトロ基のいず
れか一つを示す。)で示される芳香族置換アルコールと
のエステル化反応において、生成エステル化合物を含む
反応液をアルカリ金属炭酸塩又はアルカリ金属重炭酸塩
の水溶液を用いて中和するに際して、中和前に炭素数が
6〜12の脂肪族アルコール化合物を添加することを特徴
とするカルボン酸エステルの製造法。
1. A lower aliphatic carboxylic acid or an acid anhydride thereof in the presence of an acid catalyst and a general formula: (In the formula, X represents one of a carbamoyl group, a cyano group and a nitro group.) In an esterification reaction with an aromatic substituted alcohol represented by the formula, the reaction solution containing the produced ester compound is treated with an alkali metal carbonate or an alkali. When neutralizing with an aqueous solution of metal bicarbonate,
A method for producing a carboxylic acid ester, which comprises adding 6 to 12 aliphatic alcohol compounds.
JP3311560A 1991-10-31 1991-10-31 Production of carbonic acid ester Pending JPH05125028A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP3311560A JPH05125028A (en) 1991-10-31 1991-10-31 Production of carbonic acid ester

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP3311560A JPH05125028A (en) 1991-10-31 1991-10-31 Production of carbonic acid ester

Publications (1)

Publication Number Publication Date
JPH05125028A true JPH05125028A (en) 1993-05-21

Family

ID=18018704

Family Applications (1)

Application Number Title Priority Date Filing Date
JP3311560A Pending JPH05125028A (en) 1991-10-31 1991-10-31 Production of carbonic acid ester

Country Status (1)

Country Link
JP (1) JPH05125028A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5812105A (en) * 1996-06-10 1998-09-22 Cree Research, Inc. Led dot matrix drive method and apparatus
US7385574B1 (en) 1995-12-29 2008-06-10 Cree, Inc. True color flat panel display module

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US7385574B1 (en) 1995-12-29 2008-06-10 Cree, Inc. True color flat panel display module
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