JPS5849329A - Preparation of cyclohexanone dimethyl acetal - Google Patents
Preparation of cyclohexanone dimethyl acetalInfo
- Publication number
- JPS5849329A JPS5849329A JP7013882A JP7013882A JPS5849329A JP S5849329 A JPS5849329 A JP S5849329A JP 7013882 A JP7013882 A JP 7013882A JP 7013882 A JP7013882 A JP 7013882A JP S5849329 A JPS5849329 A JP S5849329A
- Authority
- JP
- Japan
- Prior art keywords
- cyclohexanone
- calcium chloride
- parts
- methanol
- dimethyl acetal
- 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
Links
Landscapes
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
Abstract
Description
【発明の詳細な説明】
本発明は、医薬品原料として有用なシクロへキサノンジ
メチルアセタール(以下CD−ケタールと略す。)の製
法に係る。詳記すればシクロヘキサノンとメタノールと
を反応させる際、脱水剤として塩化カルシウム?使用し
、酸性にて反応させるCD−ケタールの製法並び椿当該
方法により得られた反応液に、ヒドラジン類ケ加え、蒸
留して精製する、高純度CD−ケタールの製法に関すム
従来この種化合物は、硫酸、塩酸等ケ触媒として、シク
ロヘキサノンとメタ/−ルとt反応させたり、シクロヘ
キサノンとメタノールとに酸触媒と硫酸鋼と金加えて1
反応させる方法等により製造されていた。しかしながら
この反応は平衡反応であり、反応中生成する水だけ?反
応系外に除去するのは困難でありζその為収率は低く、
分留による生成物の単離も、シクロヘキサノンとCD−
ケタールとの沸点差が少い為非常な困難倉伴b、高純度
品を工業的に製造するのは不可能視されていた。DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a method for producing cyclohexanone dimethyl acetal (hereinafter abbreviated as CD-ketal), which is useful as a raw material for pharmaceuticals. To be more specific, is calcium chloride used as a dehydrating agent when reacting cyclohexanone and methanol? A method for producing high-purity CD-ketal, which involves adding hydrazine to the reaction solution obtained by the method and distilling and purifying it. For example, cyclohexanone and methanol can be reacted with sulfuric acid, hydrochloric acid, etc. as a catalyst, or cyclohexanone and methanol can be reacted with an acid catalyst, sulfuric acid steel, and gold.
It was manufactured by a reaction method. However, this reaction is an equilibrium reaction, and only water is produced during the reaction. It is difficult to remove it from the reaction system, so the yield is low.
Isolation of the product by fractional distillation is also useful for cyclohexanone and CD-
Due to the small difference in boiling point from ketal, it was extremely difficult to industrially produce high-purity products.
本発明者等は、高純度CD−ケタールを工業的に高収率
で得る方法ケ見出すべく鋭意検討し、脱水剤とし5て塩
化カルシウムを使用して収率を飛躍的に上昇させると共
に、反応終了液にヒドラジン?Jj k加えて分留する
こきにより高純度品?提供すること紫可能とし、本発明
を達成した。The present inventors have made extensive studies to find a method for industrially obtaining high-purity CD-ketal at a high yield, and have dramatically increased the yield by using calcium chloride as a dehydrating agent. Hydrazine in the termination liquid? Is it a high purity product due to Jj k and fractional distillation? It has been made possible and achieved by the present invention to provide this.
ンクロ′\キサノンとメタノールとの反応は、シクロヘ
キサノン、メタノール、塩化力ルンウムと?混合し、硫
酸、塩酸等の酸により反応液留酸性にし、常温付近にて
反応4行えばよい。使用するメタノールild、 /ク
ロヘキサノンに対し過剰蓋使用するのが好ましい。塩化
カルシウムの使用量ハ、シクロへキサノン1モルに対t
、、l/3〜2モル程度用いるのが好ましく、これ以上
用いてもさしたる効果はなく、これ以下にすると、若干
効果が減少する。反応終了液にヒドラジン類ケ加え、油
層ケ分留すれば、CD−ケタールとヒドラゾンとは容易
に分離出来、高純度のCD−ケタールが得られる。ヒド
ラジン類としては、例えば抱水ヒドラジン、メチルヒド
ラジン、フェニルヒドラジン等通常のもわが支障なく使
用出来、反応終了液にそのまま加えて中和1分液しても
、中和1分液後加えても一向に差し支えない。What is the reaction between xanone and methanol, cyclohexanone, methanol, and chloride? The mixture is mixed, the reaction mixture is made acidic with an acid such as sulfuric acid or hydrochloric acid, and the reaction is carried out at around room temperature. Preferably, an excess of methanol/chlorhexanone is used. The amount of calcium chloride used is t per 1 mole of cyclohexanone.
It is preferable to use about 1/3 to 2 mol. If it is used more than this, there will be no significant effect, and if it is less than this, the effect will be slightly reduced. By adding hydrazines to the reaction-completed liquid and fractionating the oil layer, CD-ketal and hydrazone can be easily separated and highly pure CD-ketal can be obtained. As the hydrazines, for example, hydrazine hydrate, methylhydrazine, phenylhydrazine, etc. can be used without any problem, and they can be added directly to the reaction completed solution and added for 1 portion of neutralization, or added after 1 portion of neutralization. There is absolutely no problem.
り上述べた如く1本発明方法は、工業的に高収率で高純
度のCD−ケタールを提供することを可能としたもので
あり、斯業に貢献する所極めて大である。As mentioned above, the method of the present invention makes it possible to industrially provide high-yield, high-purity CD-ketal, and thus makes an extremely large contribution to this industry.
以下に実施例を述べ本発明を更に説明する。実施例中数
量を表わす部は重量部である。The present invention will be further explained with reference to Examples below. In the examples, parts expressed are parts by weight.
参考例1゜
メタノール58一部とシクロヘキサノン35部、!:塩
化力ルンウム40部と濃硫酸15部とを混合する。20
〜30℃で8時間反応後、メタノール200部にカセイ
ソーダ12部を溶解した溶液で中和し、水90部を茄え
、水洗後分液して油層43部を得た。減圧蒸留により、
32mmHg、 70〜80℃の留分38部を得た
。ガスクロによるCD−ケタールの含量は88%であっ
た。比較の為。Reference example 1゜58 parts of methanol and 35 parts of cyclohexanone! : Mix 40 parts of chloride and 15 parts of concentrated sulfuric acid. 20
After reacting at ~30°C for 8 hours, the mixture was neutralized with a solution of 12 parts of caustic soda dissolved in 200 parts of methanol, boiled in 90 parts of water, washed with water, and then separated to obtain 43 parts of an oil layer. By vacuum distillation,
38 parts of a fraction at 32 mmHg and 70 to 80°C were obtained. The CD-ketal content by gas chromatography was 88%. For comparison.
同−条円で塩化カルシウムの替りに硫酸銅を用いて実験
を行うと、ガスクロ含量47%の生成物34部を得た。An experiment using copper sulfate instead of calcium chloride on the same strip gave 34 parts of a product with a gas chromatography content of 47%.
実施例1
メタノール25部とシクロへキサノン18部と塩化カル
シウム8部と濃塩酸5部とを混合する。Example 1 25 parts of methanol, 18 parts of cyclohexanone, 8 parts of calcium chloride, and 5 parts of concentrated hydrochloric acid are mixed.
10〜25℃で10時間反応後、メタノール40部にカ
セイソーダ2部を溶解した溶液で中和し。After reacting at 10 to 25°C for 10 hours, the mixture was neutralized with a solution of 2 parts of caustic soda dissolved in 40 parts of methanol.
水40部を加え、水洗後分液し、22部の油層を得た。40 parts of water was added, and after washing with water, the liquid was separated to obtain 22 parts of an oil layer.
80%抱水ヒドラジン4部を加え分液後、油層を減圧蒸
留する。30mmHg、69〜72℃の留分15部を得
た。ガスクロによる含量は99゜3%であった。After adding 4 parts of 80% hydrazine hydrate and separating the liquid, the oil layer is distilled under reduced pressure. 15 parts of a fraction at 30 mmHg and 69 to 72°C were obtained. The content determined by gas chromatography was 99.3%.
特許出願人 和光純薬工業株式、会社
5−
手続補正書
昭和57年 5月24日
特許庁長官 殿
1、事件の表示
昭和57年4月26日提出の特許願(3)2 発明の名
称
シクロへキサノンジメチルアセタールの製法1 補正を
する者
事件との関係 特許出願人
郵便番号 54に
連絡先 特許!!(東京) 置 03−270−8
5715、 補正の対象
明細書の発明の詳細な説明の欄。Patent Applicant: Wako Pure Chemical Industries, Ltd., Company 5 - Procedural Amendment May 24, 1980 Commissioner of the Patent Office 1. Indication of the Case Patent Application (3) filed on April 26, 1980 2. Name of the invention Cyclo Process for producing hexanone dimethyl acetal 1 Relationship with the case of the person making the amendment Patent applicant zip code 54 Contact information Patent! ! (Tokyo) 03-270-8
5715, Detailed description of the invention in the specification subject to amendment.
6、 補正の内容
明細書3頁15行目に記載の「が得られる。」の次に次
の文章を加入する。6. Add the following sentence after "is obtained." written on page 3, line 15 of the specification of contents of the amendment.
「これは、結果としてCD−ケタールが問題となるヒド
ラゾンとの共沸もなく容易に高純度で分離されるに到っ
たこと金量味する。尚、この場合ノ蒸留装置としては、
取り立てて精密な分留装置は必要とせず、既存の単蒸留
装置で充分である。又ここで用いる。」
以上``As a result, CD-ketal was easily separated with high purity without azeotrope with hydrazone, which is a problem.In this case, as a distillation apparatus,
No particularly precise fractionation equipment is required; an existing simple distillation equipment is sufficient. Also used here. "that's all
Claims (1)
にて/クロヘキサノンとメタノールと金反応させて得ら
れたシクロヘキサノンジメチルアセクールに、ヒドラジ
ン類?加え、蒸留して精製すること全特徴とする、高純
度シクロヘキサノンジメチルアセクールの製法。(1) Calcium chloride as a dehydrating agent? Cyclohexanone dimethyl acecool obtained by reacting clohexanone, methanol, and gold in an acidic environment, and hydrazines? In addition, the method for producing high-purity cyclohexanone dimethyl acecool is characterized by distillation and purification.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP7013882A JPS5849533B2 (en) | 1982-04-26 | 1982-04-26 | Production method of cyclohexanone dimethyl acetal |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP7013882A JPS5849533B2 (en) | 1982-04-26 | 1982-04-26 | Production method of cyclohexanone dimethyl acetal |
Related Parent Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP1801174A Division JPS5848527B2 (en) | 1974-02-14 | 1974-02-14 | Cyclohexanone dimethyl acetal noseiho |
Publications (2)
Publication Number | Publication Date |
---|---|
JPS5849329A true JPS5849329A (en) | 1983-03-23 |
JPS5849533B2 JPS5849533B2 (en) | 1983-11-05 |
Family
ID=13422905
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP7013882A Expired JPS5849533B2 (en) | 1982-04-26 | 1982-04-26 | Production method of cyclohexanone dimethyl acetal |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS5849533B2 (en) |
Families Citing this family (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS6351526U (en) * | 1986-09-19 | 1988-04-07 |
-
1982
- 1982-04-26 JP JP7013882A patent/JPS5849533B2/en not_active Expired
Also Published As
Publication number | Publication date |
---|---|
JPS5849533B2 (en) | 1983-11-05 |
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