JPS5939842A - Preparation of acetals - Google Patents

Preparation of acetals

Info

Publication number
JPS5939842A
JPS5939842A JP57150056A JP15005682A JPS5939842A JP S5939842 A JPS5939842 A JP S5939842A JP 57150056 A JP57150056 A JP 57150056A JP 15005682 A JP15005682 A JP 15005682A JP S5939842 A JPS5939842 A JP S5939842A
Authority
JP
Japan
Prior art keywords
acid
alcohol
reaction
acid catalyst
hydrocarbon group
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
Application number
JP57150056A
Other languages
Japanese (ja)
Other versions
JPH0114889B2 (en
Inventor
Noriyuki Hirowatari
広渡 紀之
Junichi Imuda
淳一 伊牟田
Yoshiro Furuya
古屋 吉朗
Teijiro Morimoto
森本 悌次郎
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.)
Mitsui Petrochemical Industries Ltd
Original Assignee
Mitsui Petrochemical Industries Ltd
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 Mitsui Petrochemical Industries Ltd filed Critical Mitsui Petrochemical Industries Ltd
Priority to JP57150056A priority Critical patent/JPS5939842A/en
Publication of JPS5939842A publication Critical patent/JPS5939842A/en
Publication of JPH0114889B2 publication Critical patent/JPH0114889B2/ja
Granted 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

  • Catalysts (AREA)
  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
  • Low-Molecular Organic Synthesis Reactions Using Catalysts (AREA)
  • Heterocyclic Compounds That Contain Two Or More Ring Oxygen Atoms (AREA)

Abstract

PURPOSE:To prepare an acetal useful as a preparation raw material of 3-acylsalicylic acid, etc. which is an intermediate of pharmaceuticals, etc., easily, in high yield, by reacting a 2-cyanophenol compound with an alcohol in the presence of an acid catalyst in combination with a dehydration agent. CONSTITUTION:The acetal of formula II (R<2> and R<3> are hydrocarbon group or together form alkylene) is prepared by reacting the 2-acylphenol compound of formula I (R<1> is H or hydrocarbon group) with an alcohol such as 2-6C alkylene glycol (e.g. ethylene glycol) in an inert diluent (preferably benzene, etc.) in the presence of an acid catalyst and a dehydration agent at 30-200 deg.C under arbitrary pressure. The acid catalyst is, e.g. sulfuric acid, p-toluensulfonic acid, metasulfonic acid, boron trifluoride.ether complex, etc., and the dehydration agent is, e.g. methyl orthoformate, ethylene carbonate, HY-type zeolite, etc.

Description

【発明の詳細な説明】 本発明は、2−アシルフェノールとアルコールからアセ
タール類を製造する方法に関し、酸触媒と共に脱水剤を
使用して、アセタールを高収率で製造する方法に関する
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a method for producing acetals from 2-acylphenol and alcohol, and relates to a method for producing acetals in high yield by using a dehydrating agent together with an acid catalyst.

3−プロピルサリチル酸などの5−アシルサリチル酸は
、医薬品などの中間原料として有用であり、本発明者ら
は、2−アシルフェノールから6−アシルサリチル酸誘
導体を製造する方法として、2−アシルフェノールをア
セタール化してカルボニル基を保護した後、フェノラー
トの状態で炭酸ガスと反応させてカルボキシル化し、そ
の後アセタールを加水分解させる方法を見出した。
5-acylsalicylic acids such as 3-propyl salicylic acid are useful as intermediate raw materials for pharmaceuticals, etc., and the present inventors have developed a method for producing 6-acylsalicylic acid derivatives from 2-acylphenols by converting 2-acylphenols into acetals. We have discovered a method in which the phenolate is reacted with carbon dioxide gas to carboxylate the carbonyl group, and then the acetal is hydrolyzed.

この方法において、2−アシルフェノールのアセタール
化反応は硫酸、スルホン酸などの酸触媒の存在下にアル
コールなどを反応させて行われる。この場合反応は、通
常ベンゼンなどの溶媒で共沸脱水しながら行われるが、
この方法ではアセタール類の収率が充分に高いとは言え
ない。
In this method, the acetalization reaction of 2-acylphenol is carried out by reacting alcohol or the like in the presence of an acid catalyst such as sulfuric acid or sulfonic acid. In this case, the reaction is usually carried out with azeotropic dehydration in a solvent such as benzene,
This method cannot be said to provide a sufficiently high yield of acetals.

本発明は、2−アシルフェノールにアルコールを反応さ
せてアセタール類を製造する方法において、酸触媒と共
に脱水剤を使用することにより、アセタール類をより高
収率で製造する方法を提供するものである。
The present invention provides a method for producing acetals at a higher yield by using a dehydrating agent together with an acid catalyst in a method for producing acetals by reacting alcohol with 2-acylphenol. .

すなわち本発明は、一般式 (式中、R1は水素又は炭化水素基を示すンで示される
2−アシルフェノールとアルコールヲ反応させて、一般
式 (式中R1は前記と同じ、R2およびR3は炭化水素基
を示し、RとRは連結してアルキレン基を形成してもよ
い)で示されるアセタール類を製造する方法において、
酸触媒と共に脱水剤を使用して該反応を行うことを特徴
とするアセタール類の製造方法に関する。
That is, the present invention provides a method of reacting a 2-acylphenol represented by the general formula (wherein R1 represents hydrogen or a hydrocarbon group) with an alcohol to form a compound represented by the general formula (wherein R1 is the same as above, R2 and R3 are In a method for producing acetals represented by (representing a hydrocarbon group, R and R may be linked to form an alkylene group),
The present invention relates to a method for producing acetals, characterized in that the reaction is carried out using a dehydrating agent together with an acid catalyst.

本発明が適用される2−アシルフェノールは前記一般式
(1)で表わされる化合物であり、一般式中のR1ハ、
水素またはメチル、エチル、n−プロピル、1so−プ
ロピル等の直鎖状または分枝状アルギル基、シクロヘキ
シル等の環状アルキル基、フェニル、トリル等のアリー
ル基、ベンジル等のアラルギル基などを代表例とする炭
化水素基である。
The 2-acylphenol to which the present invention is applied is a compound represented by the above general formula (1), in which R1 c,
Representative examples include hydrogen or linear or branched argyl groups such as methyl, ethyl, n-propyl, and 1so-propyl, cyclic alkyl groups such as cyclohexyl, aryl groups such as phenyl and tolyl, and aralgyl groups such as benzyl. It is a hydrocarbon group that

またアルコールとしては、エチレングリコール、プロピ
レングリコール、ネオペンチルグリコール、ヘキシレン
グリコールなどの炭素数2ないしるのアルキレングリコ
ール、グリセリンなどの多価アルコールが例示される。
Examples of the alcohol include alkylene glycols having 2 or more carbon atoms such as ethylene glycol, propylene glycol, neopentyl glycol, and hexylene glycol, and polyhydric alcohols such as glycerin.

本発明で使用される酸触媒には、硫酸、塩酸、リン酸な
どの鉱酸、1)−)ルエンスルホン酸、メタスルホン酸
、トリフルオロメタンスルホン酸などのスルホン酸類、
陽イオン交換樹脂、三弗化硼素エーテル錯体などのルイ
ス酸などが例示される。
The acid catalyst used in the present invention includes mineral acids such as sulfuric acid, hydrochloric acid, and phosphoric acid; 1) sulfonic acids such as luenesulfonic acid, metasulfonic acid, and trifluoromethanesulfonic acid;
Examples include cation exchange resins and Lewis acids such as boron trifluoride ether complexes.

本発明で使用される脱水剤は、オルトギ酸アルキルエス
テルたとえばオルトギ酸メチル、オルトギ酸エチル、ア
ルキレンカーボネートたとえばエチレンカーボネート、
プロピレンカーボネート、プロレンカーボネート、各種
ゼオライトたとえばHYuゼオライト、モレキュラーシ
ーブ3A、4A。
Dehydrating agents used in the present invention include alkyl orthoformates such as methyl orthoformate, ethyl orthoformate, alkylene carbonates such as ethylene carbonate,
Propylene carbonate, propylene carbonate, various zeolites such as HYu zeolite, molecular sieves 3A, 4A.

リン化合物たとえば五酸化リン、オキシ塩化リン、三塩
化リン、イオウ化合物たとえば塩化チオニルから選ばれ
る少なくとも1種類以上の化合物である。
The compound is at least one compound selected from phosphorus compounds such as phosphorus pentoxide, phosphorus oxychloride, and phosphorus trichloride, and sulfur compounds such as thionyl chloride.

本発明の反応は、酸触媒と共に脱水剤の存在下、2−ア
シルフェノールとアルコールを反応させて行われる。
The reaction of the present invention is carried out by reacting 2-acylphenol and alcohol together with an acid catalyst in the presence of a dehydrating agent.

7 ル)−z+ztD使用割合Lt、2−アシルフェノ
ール1モルに対して、約1ないし約10モル、とくに約
1.1ないし約3モルとすることが望ましい。
7)-z+ztD Usage ratio Lt is desirably about 1 to about 10 mol, particularly about 1.1 to about 3 mol, per 1 mol of 2-acylphenol.

酸触媒の使用量は、2−アシルフェノール、アルコール
の種類に応じて適宜変えることができるが、通常は2−
アシルフェノール1モルに対して約0.001ないし約
0.2モル、とくに約o、o iないし0.1モルとす
ることが望ましい。
The amount of acid catalyst used can be changed as appropriate depending on the type of 2-acylphenol and alcohol, but usually 2-acylphenol and alcohol are used.
It is desirable that the amount is about 0.001 to about 0.2 mol, particularly about o, o i to 0.1 mol, per 1 mol of acylphenol.

脱水剤の使用量は任意であるが、2−アシルフェノール
1モルに対して通常0.1ないし約10モル、とくに約
0.3ないし約3モルの範囲が好適である。
The amount of the dehydrating agent to be used is arbitrary, but it is preferably in the range of usually 0.1 to about 10 moles, particularly about 0.3 to about 3 moles, per mole of 2-acylphenol.

これらの脱水剤は反応系に一時に添加してもよく、何回
かに分けて添加してもよい。脱水剤として各種ゼオライ
トを用いる場合には還流する水を含む溶媒を該脱水剤で
脱水して反応系内へ戻す方法が望ましい。
These dehydrating agents may be added to the reaction system all at once, or may be added in several portions. When using various zeolites as a dehydrating agent, it is desirable to dehydrate the refluxing water-containing solvent with the dehydrating agent and return it to the reaction system.

本発明の反応は、不活性希釈剤を用いずに行ってもよい
が、通常は不活性希釈剤、例えばヘギザン、ヘプタン、
灯油、シクロヘキサン、ベンゼン、トルエン、キシレン
のような炭化水素、クロロベンゼンのようなハロゲン化
炭化水素などの共存下に行われる。
The reactions of the present invention may be carried out without an inert diluent, but usually an inert diluent such as hegyzane, heptane,
It is carried out in the coexistence of hydrocarbons such as kerosene, cyclohexane, benzene, toluene, xylene, and halogenated hydrocarbons such as chlorobenzene.

反応は、任意の圧力下で行われ得る。反応温度は、通常
約30°Cないし約200°C1とくに好ましくは約5
0°Cないし約150°Cである。
The reaction can be carried out under any pressure. The reaction temperature is usually about 30°C to about 200°C, particularly preferably about 5°C.
0°C to about 150°C.

本発明の反応で得られるアセタール類は、前記一般式(
I)で示される化合物であり、一般式中R2およびR3
は、任意の炭化水素基であり、中でもR2とR3が連結
してアルキレン基例えばエチレン、プロピレン、アルキ
ル置換エチレンなどを形成した構造のものを好適例とし
て挙げることができる。
The acetals obtained by the reaction of the present invention have the general formula (
A compound represented by I), in which R2 and R3
is any hydrocarbon group, and preferred examples include those having a structure in which R2 and R3 are linked to form an alkylene group such as ethylene, propylene, alkyl-substituted ethylene, etc.

反応終了後は、慣用手段により、反応混合物からアセタ
ール類を分離することができる。またあるいはアセター
ル類を分離することなく、反応混合物をそのままあるい
は若干の後処理操作を施した復信の反応に供することが
可能である。
After the reaction is complete, acetals can be separated from the reaction mixture by conventional means. Alternatively, the reaction mixture can be subjected to a repeat reaction as it is or after some post-treatment without separating the acetals.

本発明によれば、アセタール類をより高収率で製造する
ことができる。
According to the present invention, acetals can be produced in higher yields.

以下に実施例を示す。Examples are shown below.

実施例1 攪拌機、温度計、Dean−3tark装置を備えつけ
た200m1フラスコに2−プロピオニルフェノール7
.51 g (C1,05モル)、エチレングリコール
9.32g(0,i5モル)、エチレンカーボネート5
.29 g (0,06モル)、p−)ルエンスルホン
酸0.475 g (5モル%)およびベンゼン75m
4を入れ43hr加熱還流した。反応混合物を冷却した
のち氷を含む重曹水へ注ぎ、分液し、水層をベンゼンで
抽出し、有機層を合わせて水洗乾燥した。ガスクロマト
グラフィー分析した結果、2−7”ロヒ。
Example 1 2-Propionylphenol 7 was added to a 200ml flask equipped with a stirrer, thermometer, and Dean-3tark apparatus.
.. 51 g (C1.05 mol), ethylene glycol 9.32 g (0.i5 mol), ethylene carbonate 5
.. 29 g (0.06 mol), p-)luenesulfonic acid 0.475 g (5 mol%) and benzene 75 m
4 and heated under reflux for 43 hours. After the reaction mixture was cooled, it was poured into aqueous sodium bicarbonate containing ice to separate the layers, the aqueous layer was extracted with benzene, and the organic layers were combined, washed with water, and dried. As a result of gas chromatography analysis, it was 2-7" ROHI.

オニルフェノールの転化率ハ84%、エチレンアセター
ルの収率は83%、選択率は99%であった。
The conversion rate of onylphenol was 84%, the yield of ethylene acetal was 83%, and the selectivity was 99%.

実施例2 実施例1のエチレンカーボネートの量を8.81gに変
えた以外は実施例1と同様に反応を行ったところ、転化
率87%、収率86%、選択率99%であった。
Example 2 The reaction was carried out in the same manner as in Example 1 except that the amount of ethylene carbonate in Example 1 was changed to 8.81 g, and the conversion rate was 87%, the yield was 86%, and the selectivity was 99%.

実施例5 攪拌機、温度計、冷却器を備えつけた容量が200m1
フラスコに2−プロピオニルフェノール7(0.15モ
ル)、オルトギ酸メチル7、69 g ( 0.075
モル)、p−トルエンスルホン酸0.475g(5モル
%)およびベンゼン75Jを入れ8hr加熱還流したと
ころ、転化率97%、収率95%、選択率98%であっ
た。
Example 5 Capacity 200ml equipped with stirrer, thermometer, and cooler
In a flask, 2-propionylphenol 7 (0.15 mol), methyl orthoformate 7, 69 g (0.075
When 0.475 g (5 mol %) of p-toluenesulfonic acid and 75 J of benzene were added and heated under reflux for 8 hours, the conversion rate was 97%, the yield was 95%, and the selectivity was 98%.

実施例4〜6 実施例乙のオルトギ酸メチルの量を表1に示す量に変え
た以外、あるいはオルトギ酸メチルの代わりにオルトギ
酸エチルを表1に示す量用いた以外は実施例3と同様の
反応を行ったところ、表1に示す結果が得られた。
Examples 4 to 6 Same as Example 3 except that the amount of methyl orthoformate in Example B was changed to the amount shown in Table 1, or ethyl orthoformate was used in the amount shown in Table 1 instead of methyl orthoformate. When the reaction was carried out, the results shown in Table 1 were obtained.

表       1 実施例7 実施例1において48hr加熱還流する代りに12hr
共沸脱水したのちHY型ゼオライト(商品名SK−4 
1 )5.0 gを加えてさらに1 2 h.r加熱反
応させたところ、転化率70%、収率68%、選択率9
7%であった。
Table 1 Example 7 Instead of heating and refluxing for 48 hours in Example 1, heating was performed for 12 hours.
After azeotropic dehydration, HY type zeolite (product name SK-4
1) Add 5.0 g and continue for 12 h. When the reaction was carried out by heating, the conversion rate was 70%, the yield was 68%, and the selectivity was 9.
It was 7%.

実施例8〜9 実施例6のエチレングリコールの代りに表2に示すアル
コールを表2に示す量用いた以外は実施例3と同様に反
応を行い表2の結果を得た。
Examples 8 to 9 The reaction was carried out in the same manner as in Example 3, except that the alcohol shown in Table 2 was used in the amount shown in Table 2 instead of the ethylene glycol in Example 6, and the results shown in Table 2 were obtained.

表      2 実施例10〜12 実[IJlのp−)ルエンスルホン酸の代りに表6に示
す酸を表3に示す量用いた以外は実施例1と同様に反応
を行ったところ表3の結果が得られた。
Table 2 Examples 10 to 12 The reaction was carried out in the same manner as in Example 1, except that the acids shown in Table 6 were used in the amounts shown in Table 3 instead of real [IJl p-)luenesulfonic acid, and the results shown in Table 3 were obtained. was gotten.

表       5 実施例13 実m例1の2−プロピオニルフェノールの代すに2−ア
セチルフェノールを6.81g用いた以外は実施例1と
同様に反応を行ったととろ、2−アセチルフェノールの
転化率は89%、エチレンアセタールの収率は88%、
選択率は99%であった。
Table 5 Example 13 The reaction was carried out in the same manner as in Example 1 except that 6.81 g of 2-acetylphenol was used instead of 2-propionylphenol in Example 1. The conversion rate of 2-acetylphenol was as follows. 89%, the yield of ethylene acetal is 88%,
The selectivity was 99%.

実施例14〜15 実施例1のベンゼンの代わりに表4に示した溶媒を用い
た以外は実施例1と同様に反応を行ったところ表4に示
す結果が得られた。
Examples 14-15 The reaction was carried out in the same manner as in Example 1, except that the solvent shown in Table 4 was used instead of benzene in Example 1, and the results shown in Table 4 were obtained.

表       4 比較例1 実施例1においてエチレンカーボネートを用いずに実施
例1と同様に反応を行ったところ2−プロピオニルフェ
ノールの転化率は55%、エチレンケタールの収率は5
4%、選択率は98%であった 出願人  三井石油化学工業株式会社 代理人  山  口     和
Table 4 Comparative Example 1 When a reaction was carried out in the same manner as in Example 1 without using ethylene carbonate, the conversion rate of 2-propionylphenol was 55% and the yield of ethylene ketal was 55%.
4%, and the selection rate was 98%.Applicant: Mitsui Petrochemical Industries Co., Ltd. Agent Kazu Yamaguchi

Claims (1)

【特許請求の範囲】[Claims] (1)一般式 (式中、Rは水素又は炭化水素基を示す)で示される2
−アシルフェノール類とアルコールを反応させて、一般
式 (式中、R1は前記と同じ、R2およびR3は炭化水素
基を示し、RとRは連結してアルキレン基を形成してい
てもよい)で表わされるアセタール類を製造する方法に
おいて、酸触媒と共に脱水剤の存在下に該反応を行うこ
とを特徴とするアセタール類の製造方法。
(1) 2 represented by the general formula (wherein R represents hydrogen or a hydrocarbon group)
-By reacting acylphenols with alcohol, the general formula (wherein R1 is the same as above, R2 and R3 represent a hydrocarbon group, and R and R may be connected to form an alkylene group) A method for producing acetals represented by the following, characterized in that the reaction is carried out in the presence of a dehydrating agent together with an acid catalyst.
JP57150056A 1982-08-31 1982-08-31 Preparation of acetals Granted JPS5939842A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP57150056A JPS5939842A (en) 1982-08-31 1982-08-31 Preparation of acetals

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP57150056A JPS5939842A (en) 1982-08-31 1982-08-31 Preparation of acetals

Publications (2)

Publication Number Publication Date
JPS5939842A true JPS5939842A (en) 1984-03-05
JPH0114889B2 JPH0114889B2 (en) 1989-03-14

Family

ID=15488538

Family Applications (1)

Application Number Title Priority Date Filing Date
JP57150056A Granted JPS5939842A (en) 1982-08-31 1982-08-31 Preparation of acetals

Country Status (1)

Country Link
JP (1) JPS5939842A (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS61117402U (en) * 1985-01-09 1986-07-24
GB2369361A (en) * 1997-12-22 2002-05-29 Inst Francais Du Petrole Efficient synthesis of an acetal from a non-cyclic ketone or aldehyde starting materials
JP2006289158A (en) * 2005-04-05 2006-10-26 Mitsubishi Heavy Ind Ltd Catalyst for synthesis of acetal and method of manufacturing acetal

Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5632427A (en) * 1979-08-22 1981-04-01 Bayer Ag Novel 44fluoroo33phenoxyybenzaldehydeacetal* its manufacture* novel intermediate therefor and its manufacture

Patent Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5632427A (en) * 1979-08-22 1981-04-01 Bayer Ag Novel 44fluoroo33phenoxyybenzaldehydeacetal* its manufacture* novel intermediate therefor and its manufacture

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS61117402U (en) * 1985-01-09 1986-07-24
GB2369361A (en) * 1997-12-22 2002-05-29 Inst Francais Du Petrole Efficient synthesis of an acetal from a non-cyclic ketone or aldehyde starting materials
GB2369361B (en) * 1997-12-22 2002-08-07 Inst Francais Du Petrole Synthesis of an acetal from non-cyclic ketone or aldehyde starting material
JP2006289158A (en) * 2005-04-05 2006-10-26 Mitsubishi Heavy Ind Ltd Catalyst for synthesis of acetal and method of manufacturing acetal

Also Published As

Publication number Publication date
JPH0114889B2 (en) 1989-03-14

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