JPH101453A - Production of benzyl acetate - Google Patents

Production of benzyl acetate

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Publication number
JPH101453A
JPH101453A JP17288696A JP17288696A JPH101453A JP H101453 A JPH101453 A JP H101453A JP 17288696 A JP17288696 A JP 17288696A JP 17288696 A JP17288696 A JP 17288696A JP H101453 A JPH101453 A JP H101453A
Authority
JP
Japan
Prior art keywords
acetic acid
mol
benzyl chloride
benzyl
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
Application number
JP17288696A
Other languages
Japanese (ja)
Inventor
Tamio Shirafuji
民雄 白藤
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.)
Sanken Kako KK
Original Assignee
Sanken Kako 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 Sanken Kako KK filed Critical Sanken Kako KK
Priority to JP17288696A priority Critical patent/JPH101453A/en
Publication of JPH101453A publication Critical patent/JPH101453A/en
Pending legal-status Critical Current

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

Abstract

PROBLEM TO BE SOLVED: To obtain benzyl acetate by using an inexpensive alkali, because conventional method for producing benzyl acetate, which needs to use expensive anhydrous potassium acetate, is not satisfactory as industrial manufacturing method. SOLUTION: When producing benzyl chloride by reacting benzyl chloride with an alkali in the presence of an excess amount of acetic acid in water- containing state, the reaction is carried out in the presence of acetic acid in an amount of >=1.1mol and <=3mol based on 1mol benzyl chloride and an alkali in an amount of >=1.0 equivalent based on 1mol benzyl chloride and in a smaller number of equivalent than the number of mol of coexisting acetic acid.

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、香料等として有用な酢
酸ベンジルの製造法に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method for producing benzyl acetate useful as a fragrance or the like.

【0002】[0002]

【従来の技術】従来、酢酸ベンジルの製造法は、例えば
ドイツ特許41507号に、大過剰の氷酢酸存在下に塩
化ベンジルと無水酢酸カリウムとを加熱還流にて反応さ
せる方法が記載されている。
2. Description of the Related Art Conventionally, as a method for producing benzyl acetate, for example, German Patent No. 41507 describes a method in which benzyl chloride and anhydrous potassium acetate are reacted under heating and reflux in the presence of a large excess of glacial acetic acid.

【0003】[0003]

【発明が解決しようとする課題】しかし、上記の方法に
おいては、高価な無水酢酸カリウムを使用する必要があ
り、工業的製造法としては十分なものとは言い難いもの
であった。
However, in the above-mentioned method, it is necessary to use expensive anhydrous potassium acetate, and it is hardly sufficient for an industrial production method.

【0004】[0004]

【問題点を解決するための手段】本発明者らは、酢酸ベ
ンジルの製造法として、工業的に入手可能であり、かつ
安価なアルカリと塩化ベンジルを含水状態にて反応させ
るものであり、その際に1モルの塩化ベンジルに対して
1.1モル以上3モル以下の酢酸及び1.0当量以上
で、かつ共存する酢酸のモル数より少ない当量数のアル
カリを存在させて反応することを特徴とする酢酸ベンジ
ルの製造法を提供するものである。
Means for Solving the Problems As a process for producing benzyl acetate, the present inventors have reacted industrially available and inexpensive alkali with benzyl chloride in a water-containing state. In this case, the reaction is performed in the presence of 1.1 to 3 mol of acetic acid and 1.0 or more equivalents of acetic acid to 1 mol of benzyl chloride and an equivalent number of alkalis smaller than the number of coexisting acetic acids. And a method for producing benzyl acetate.

【0005】以下、本発明を詳細に説明する。 本発明
は、塩化ベンジル1モルに対して酢酸を1.1モル以上
3モル以下とアルカリを1.0当量以上で、かつ共存す
る酢酸のモル数より少ない当量数での仕込比で含水状態
にて反応することにより酢酸ベンジルを製造する方法で
ある。
Hereinafter, the present invention will be described in detail. In the present invention, the hydrated state is prepared at a charge ratio of 1.1 mol or more and 3 mol or less of acetic acid and 1.0 equivalent or more of alkali to 1 mol of benzyl chloride and an equivalent number smaller than the number of moles of acetic acid coexisting. This is a method for producing benzyl acetate.

【0006】反応温度は加熱還流下で実施され、通常1
00〜140℃範囲であり、好ましくは105〜120
℃の範囲である。 反応時間は通常1〜30時間で目的
を達する事ができる。
[0006] The reaction temperature is carried out under heating to reflux, usually 1
In the range of 00 to 140 ° C, preferably 105 to 120 ° C.
It is in the range of ° C. The reaction can be carried out usually for 1 to 30 hours.

【0007】使用されるアルカリとしては、例えば水酸
化ナトリウム、炭酸ナトリウム、重炭酸ナトリウム、水
酸化カリウム、炭酸カリウム及び重炭酸カリウムなどが
適当である。
As the alkali used, for example, sodium hydroxide, sodium carbonate, sodium bicarbonate, potassium hydroxide, potassium carbonate and potassium bicarbonate are suitable.

【0008】本反応系は含水状態にて酢酸ベンジルが良
好な反応収率で得られる。 反応系の含水率については
特に制限はないが、通常1〜30%の範囲である。 例
えば、酢酸とアルカリの中和水のみが存在する系であっ
てもよい。
In this reaction system, benzyl acetate can be obtained with a good reaction yield in a water-containing state. The water content of the reaction system is not particularly limited, but is usually in the range of 1 to 30%. For example, a system in which only acetic acid and neutralized water of alkali exist.

【0009】本反応により得られた反応液を分液、中和
及び濃縮することにより酢酸ベンジルが得られるが、そ
の際少量のベンジルアルコ−ルが含有される。 副生ベ
ンジルアルコ−ルは当該反応液に硫酸存在下に少量の無
水酢酸と反応させる等の通常の方法により、より高純度
の酢酸ベンジルとすることができる。
The reaction solution obtained by this reaction is separated, neutralized and concentrated to obtain benzyl acetate, which contains a small amount of benzyl alcohol. By-product benzyl alcohol can be converted to higher purity benzyl acetate by an ordinary method such as a reaction of the reaction solution with a small amount of acetic anhydride in the presence of sulfuric acid.

【0010】本発明の反応仕込モル比の検討を酢酸につ
いて実施した。
[0010] The reaction molar ratio of the present invention was examined for acetic acid.

【0011】塩化ベンジル1モルに対して50%水酸化
ナトリウム水溶液を1.1モルとして酢酸のモル数を種
々変えて反応を実施した。 結果を表−1に示した。
塩化ベンジル1モルに対して酢酸1.1〜3.0と過剰
モル数存在すれば、塩化ベンジル反応率及び酢酸ベンジ
ル反応収率ともに良好な結果が得られた。
The reaction was carried out by varying the number of moles of acetic acid with 1.1 mole of 50% aqueous sodium hydroxide solution per mole of benzyl chloride. The results are shown in Table 1.
If there is an excess mole number of 1.1 to 3.0 acetic acid relative to 1 mole of benzyl chloride, good results were obtained for both the benzyl chloride reaction rate and the benzyl acetate reaction yield.

【0012】塩化ベンジル1モルに対して酢酸が1モル
しか存在しない場合には、塩化ベンジル反応率及び酢酸
ベンジル反応収率ともに顕著に低下する。
When only 1 mol of acetic acid is present per 1 mol of benzyl chloride, both the benzyl chloride reaction rate and the benzyl acetate reaction yield decrease remarkably.

【0013】一方、塩化ベンジル1モルに対して酢酸が
3モルを越えて存在しても、塩化ベンジル反応率及び酢
酸ベンジル反応収率ともに向上することはない。
On the other hand, even if acetic acid is present in an amount exceeding 3 moles per mole of benzyl chloride, neither the benzyl chloride reaction rate nor the benzyl acetate reaction yield is improved.

【0014】表1の結果から酢酸の仕込モル比は塩化ベ
ンジル1モルに対して1.1〜3.0モルの範囲が好ま
しく、かつその範囲内で仕込モル比が多いほうが塩化ベ
ンジル反応率及び酢酸ベンジル反応収率ともに向上す
る。
From the results shown in Table 1, the molar ratio of acetic acid to be charged is preferably in the range of 1.1 to 3.0 mol per mol of benzyl chloride. Both benzyl acetate reaction yields are improved.

【0015】水酸化ナトリウムは水溶液として塩化ベン
ジル1モルに対して1.0モル以上あれば十分である。
塩化ベンジル1モルに対して水酸化ナトリウム仕込量
が1モルを下回ると、結果として生成する一方の反応原
料である酢酸ナトリウムが1.0モルを下回ることにな
り、塩化ベンジル反応率が低下することになり適当でな
い。 また表1の実施例1、実施例2及び比較例1に例
示したように水酸化ナトリウムの仕込モル比は共存する
酢酸のモル数以下になるようにすることが好ましい。
比較例1に例示したように水酸化ナトリウム仕込みモル
比が共存する酢酸のモル比より大きくなると塩化ベンジ
ル反応率及び酢酸ベンジル反応収率は大きく低下した。
It is sufficient that the amount of sodium hydroxide is 1.0 mol or more per 1 mol of benzyl chloride as an aqueous solution.
If the amount of sodium hydroxide charged is less than 1 mole per mole of benzyl chloride, one of the resulting reaction materials, sodium acetate, will be less than 1.0 mole, and the benzyl chloride conversion will decrease. It is not appropriate. Further, as exemplified in Example 1, Example 2 and Comparative Example 1 in Table 1, the charged molar ratio of sodium hydroxide is preferably set to be equal to or less than the number of moles of coexisting acetic acid.
As exemplified in Comparative Example 1, when the molar ratio of sodium hydroxide charged was larger than the molar ratio of coexisting acetic acid, the benzyl chloride reaction rate and the benzyl acetate reaction yield were significantly reduced.

【0016】表−2にアルカリとして重炭酸ナトリウ
ム、炭酸ナトリウム、、水酸化カリウム、重炭酸カリウ
ム及び炭酸カリウムを使用した結果を示した。
Table 2 shows the results obtained when sodium bicarbonate, sodium carbonate, potassium hydroxide, potassium bicarbonate and potassium carbonate were used as alkalis.

【0017】[0017]

【発明の効果】本発明によれば、塩化ベンジルに過剰量
の酢酸の存在下、アルカリと含水状態にて反応させて酢
酸ベンジルを製造する際に、1モルの塩化ベンジルに対
して1.1モル以上3モル以下の酢酸及び1.0当量以
上で、かつ共存する酢酸のモル数より少ない当量数のア
ルカリを存在させて反応することにより酢酸ベンジルを
良好な収率で得ることができる。 又工業的に入手可能
であり、かつ安価なアルカリ水溶液を使用可能とした点
で有利な方法である。
According to the present invention, when producing benzyl acetate by reacting benzyl chloride with an alkali in the presence of an excess amount of acetic acid in the presence of water, 1.1 mole of benzyl chloride is added to 1 mole of benzyl chloride. Benzyl acetate can be obtained in good yield by reacting in the presence of at least 3 moles of acetic acid and at least 1.0 equivalent of an alkali and an equivalent number of alkalis smaller than the number of moles of acetic acid coexisting. Further, this method is advantageous in that it is industrially available and an inexpensive alkaline aqueous solution can be used.

【0018】[0018]

【実施例】以下実施例により本発明を更に詳細に説明す
るが本発明はこれに限定されるものではない。
The present invention will be described in more detail with reference to the following Examples, but it should not be construed that the present invention is limited thereto.

【0019】[0019]

【実施例1】50%水酸化ナトリウム水溶液253.4
0g(3.17モル)に酢酸224.60g(3.74
モル)及び塩化ベンジル368.00g(2.91モ
ル)を加えて内温105〜110℃にて15時間加熱還
流下に攪拌した。 反応液を分液して下層の水層を除
き、上層の有機層を減圧下に濃縮した。 得られた濃縮
液をサンプリングしてガスクロ分析したところ塩化ベン
ジル反応率95%、酢酸ベンジル反応収率78%及びベ
ンジルアルコ−ル反応収率15%であった。
Example 1 50% aqueous sodium hydroxide solution 253.4
224.60 g (3.74) of acetic acid was added to 0 g (3.17 mol) of acetic acid.
Mol) and 368.00 g (2.91 mol) of benzyl chloride, and the mixture was stirred at an internal temperature of 105 to 110 ° C for 15 hours while heating under reflux. The reaction solution was separated to remove the lower aqueous layer, and the upper organic layer was concentrated under reduced pressure. The resulting concentrated solution was sampled and subjected to gas chromatographic analysis to find that the benzyl chloride reaction rate was 95%, the benzyl acetate reaction yield was 78%, and the benzyl alcohol reaction yield was 15%.

【0020】[0020]

【実施例2】実施例1の仕込酢酸量を209.52g
(3.49モル)に変更し、その他は実施例1と同様に
行った。結果を表−1に示した。
Example 2 The amount of acetic acid charged in Example 1 was 209.52 g.
(3.49 mol), and the others were the same as in Example 1. The results are shown in Table 1.

【0021】[0021]

【実施例3】実施例1の仕込酢酸量を192.06g
(3.20モル)に変更し、その他は実施例1と同様に
行った。結果を表−1に示した。
Example 3 The amount of acetic acid used in Example 1 was changed to 192.06 g.
(3.20 mol), and the others were the same as in Example 1. The results are shown in Table 1.

【0022】[0022]

【実施例4】実施例1の仕込酢酸量を523.80g
(8.73モル)に変更し、その他は実施例1と同様に
行った。結果を表−1に示した。
Example 4 The amount of acetic acid charged in Example 1 was 523.80 g.
(8.73 mol), and the others were the same as in Example 1. The results are shown in Table 1.

【0023】[0023]

【比較例1】実施例1の仕込酢酸量を174.60g
(2.91モル)に変更し、その他は実施例1と同様に
行った。結果を表−1に示した。
Comparative Example 1 The amount of acetic acid charged in Example 1 was 174.60 g.
(2.91 mol), and the others were the same as in Example 1. The results are shown in Table 1.

【0024】[0024]

【比較例2】実施例1の仕込酢酸量を576.18g
(9.60モル)に変更し、その他は実施例1と同様に
行った。結果を表−1に示した。
Comparative Example 2 The amount of acetic acid charged in Example 1 was 576.18 g.
(9.60 mol), and the others were the same as in Example 1. The results are shown in Table 1.

【0025】[0025]

【表1】 [Table 1]

【0026】[0026]

【実施例5】実施例3においてNaOHの代りに、Na
HCO3266.28g(3.17モル)を使用した他
は実施例3と同様に行った。結果を表−2に示した。
Embodiment 5 In Embodiment 3, NaOH is used instead of NaOH.
Example 3 was repeated except that 266.28 g (3.17 mol) of HCO 3 was used. The results are shown in Table-2.

【0027】[0027]

【実施例6】実施例4においてNaOHの代りに、Na
HCO3266.28g(3.17モル)を使用した他
は実施例4と同様に行った。結果を表−2に示した。
EXAMPLE 6 In Example 4, NaOH was used instead of NaOH.
The same operation as in Example 4 was performed except that 266.28 g (3.17 mol) of HCO 3 was used. The results are shown in Table-2.

【0028】[0028]

【実施例7】実施例3においてNaOHの代りに、Na
2CO3167.48g(1.58モル)を使用した他は
実施例3と同様に行った。結果を表−2に示した。
Embodiment 7 In Embodiment 3, NaOH is used instead of NaOH.
The same operation as in Example 3 was performed except that 167.48 g (1.58 mol) of 2 CO 3 was used. The results are shown in Table-2.

【0029】[0029]

【実施例8】実施例4においてNaOHの代りに、Na
2CO3167.48g(1.58モル)を使用した他は
実施例4と同様に行った。結果を表−2に示した。
Example 8 In Example 4, NaOH was used instead of NaOH.
The procedure was performed in the same manner as in Example 4 except that 167.48 g (1.58 mol) of 2 CO 3 was used. The results are shown in Table-2.

【0030】[0030]

【実施例9】実施例3においてNaOHの代りに、KO
H177.52g(3.17モル)を使用した他は実施
例3と同様に行った。結果を表−2に示した。
Embodiment 9 In Embodiment 3, KO was used instead of NaOH.
The same procedures as in Example 3 were carried out except for using 177.52 g (3.17 mol) of H. The results are shown in Table-2.

【0031】[0031]

【実施例10】実施例4においてNaOHの代りに、K
OH177.52g(3.17モル)を使用した他は実
施例4と同様に行った。結果を表−2に示した。
Example 10 In Example 4, K was used instead of NaOH.
Example 4 was repeated except that 177.52 g (3.17 mol) of OH was used. The results are shown in Table-2.

【0032】[0032]

【実施例11】実施例3においてNaOHの代りに、K
HCO3317.00g(3.17モル)を使用した他
は実施例3と同様に行った。結果を表−2に示した。
Example 11 In Example 3, K was used instead of NaOH.
The same operation as in Example 3 was carried out except that 317.00 g (3.17 mol) of HCO 3 was used. The results are shown in Table-2.

【0033】[0033]

【実施例12】実施例4においてNaOHの代りに、K
HCO3317.00g(3.17モル)を使用した他
は実施例4と同様に行った。結果を表−2に示した。
Example 12 In Example 4, K was used instead of NaOH.
The same operation as in Example 4 was performed except that 317.00 g (3.17 mol) of HCO 3 was used. The results are shown in Table-2.

【0034】[0034]

【実施例13】実施例3においてNaOHの代りに、K
2CO3218.04g(1.58モル)を使用した他は
実施例3と同様に行った。結果を表−2に示した。
Example 13 In Example 3, K was used instead of NaOH.
The same operation as in Example 3 was carried out except that 218.04 g (1.58 mol) of 2 CO 3 was used. The results are shown in Table-2.

【0035】[0035]

【実施例14】実施例4においてNaOHの代りに、K
2CO3218.04g(1.58モル)を使用した他は
実施例4と同様に行った。結果を表−2に示した。
Embodiment 14 In Embodiment 4, K is replaced by NaOH.
Example 4 was repeated except that 218.04 g (1.58 mol) of 2 CO 3 was used. The results are shown in Table-2.

【0036】[0036]

【表2】 [Table 2]

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】塩化ベンジルに過剰量の酢酸の存在下、ア
ルカリと含水状態にて反応させて酢酸ベンジルを製造す
る際に、1モルの塩化ベンジルに対して1.1モル以上
3モル以下の酢酸及び1.0当量以上で、かつ共存する
酢酸のモル数より少ない当量数のアルカリを存在させて
反応することを特徴とする酢酸ベンジルの製造法。
(1) When producing benzyl acetate by reacting benzyl chloride with an alkali in the presence of an excess amount of acetic acid in the presence of water, 1.1 to 3 mol of benzyl chloride is added to 1 mol of benzyl chloride. A process for producing benzyl acetate, characterized in that the reaction is carried out in the presence of acetic acid and at least 1.0 equivalent of an alkali which is less than the number of moles of acetic acid coexisting.
JP17288696A 1996-06-11 1996-06-11 Production of benzyl acetate Pending JPH101453A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP17288696A JPH101453A (en) 1996-06-11 1996-06-11 Production of benzyl acetate

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP17288696A JPH101453A (en) 1996-06-11 1996-06-11 Production of benzyl acetate

Publications (1)

Publication Number Publication Date
JPH101453A true JPH101453A (en) 1998-01-06

Family

ID=15950153

Family Applications (1)

Application Number Title Priority Date Filing Date
JP17288696A Pending JPH101453A (en) 1996-06-11 1996-06-11 Production of benzyl acetate

Country Status (1)

Country Link
JP (1) JPH101453A (en)

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