[go: up one dir, main page]

JP2000178294A - Method for producing pentaacetyl-β-D-glucose - Google Patents

Method for producing pentaacetyl-β-D-glucose

Info

Publication number
JP2000178294A
JP2000178294A JP37559798A JP37559798A JP2000178294A JP 2000178294 A JP2000178294 A JP 2000178294A JP 37559798 A JP37559798 A JP 37559798A JP 37559798 A JP37559798 A JP 37559798A JP 2000178294 A JP2000178294 A JP 2000178294A
Authority
JP
Japan
Prior art keywords
glucose
producing
pentaacetyl
reaction
present
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
JP37559798A
Other languages
Japanese (ja)
Inventor
Masamichi Ito
雅通 伊藤
Daichi Oguro
大地 小黒
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.)
T Hasegawa Co Ltd
Original Assignee
T Hasegawa Co 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 T Hasegawa Co Ltd filed Critical T Hasegawa Co Ltd
Priority to JP37559798A priority Critical patent/JP2000178294A/en
Publication of JP2000178294A publication Critical patent/JP2000178294A/en
Pending legal-status Critical Current

Links

Landscapes

  • Saccharide Compounds (AREA)

Abstract

(57)【要約】 【課題】 ペンタアセチル−β−D−グルコースの工業
的に安全かつ安価な製造方法を提供する。 【解決手段】 グルコースを非プロトン性溶媒の存在
下、無水酢酸と反応させる新規なペンタアセチル−β−
D−グルコースの製造方法を提供する。
(57) [Problem] To provide an industrially safe and inexpensive method for producing pentaacetyl-β-D-glucose. SOLUTION: A novel pentaacetyl-β- reacting glucose with acetic anhydride in the presence of an aprotic solvent.
Provided is a method for producing D-glucose.

Description

【発明の詳細な説明】DETAILED DESCRIPTION OF THE INVENTION

【0001】[0001]

【発明の属する技術分野】本発明は、例えば、香粧品
類、飲食品類などに配合する香料前駆体としての香料配
糖体、両親媒性溶媒としてのゲル化剤、或いは、トコフ
ェロール配糖体などの医薬・保健衛生品に用いられる配
糖体類の合成中間体として有用な、ペンタアセチル−β
−D−グルコースの製造方法に関する。
The present invention relates to a fragrance glycoside as a fragrance precursor, a gelling agent as an amphipathic solvent, a tocopherol glycoside, etc., which are incorporated in cosmetics, foods and drinks, and the like. Pentaacetyl-β useful as a synthetic intermediate for glycosides used in pharmaceutical and health products
-A method for producing D-glucose.

【0002】[0002]

【従来の技術】糖類のアセチル誘導体は、アルキルグル
コシドをはじめ各種糖類誘導体を合成するための中間体
として重要な化合物である。中でも、グルコースのアセ
チル誘導体のうちβ−体である、ペンタアセチル−β−
D−グルコースは、例えば、上記したような香料配糖体
の中間体として用いられ、香料化合物のβ−D−グルコ
シドを得ることができるが、このβ−体はα−体のD−
グルコシドよりも加水分解性、微生物分解性に優れてい
るので、例えば、皮膚常在菌などにより容易に香料物質
を放出することができ、工業的にはより実用性があり重
要なものである。従って、β−体の配糖体を得るために
は、原料としてβ−体のアセチル化グルコースを用いる
方が有利であり、その製造方法も提案されている。例え
ば、酸性触媒の存在下、無水酢酸の還流下にグルコース
を添加して反応させるという、高温下での激しい反応に
よる製造方法である[Methods,Carbohy
dr.Chem.,211−215,(196
3)]。ただ、この製造方法では酢酸蒸気の排気は避け
られず、作業環境の悪化と排気洗浄設備の設置等の環境
対策が必要であり、また、反応温度を低下させるとα−
体の生成が増加し、目的とするβ−体の収率が低下す
る。一方、酢酸を反応溶媒として、100℃以下の温和
な反応温度で糖類のアセチル誘導体を得る方法(特開平
10−237084号公報)、或いは、酢酸エチル、酢
酸ブチル等の酢酸の低級アルキルエステルを溶媒にして
80〜120℃の温度で反応させる単糖乃至オリゴ糖の
完全アセチル化物の製造法(特開昭62−42996号
公報)などが提案されているが、いずれも発明の詳細な
説明にはα−体、β−体についての記載は無く、β−体
の製法とは言い難い。また、後者は、大量の酢酸廃水が
発生し工業的には問題である。
2. Description of the Related Art An acetyl derivative of a saccharide is an important compound as an intermediate for synthesizing various saccharide derivatives such as alkyl glucosides. Among them, pentaacetyl-β-, which is a β-form among acetyl derivatives of glucose,
D-glucose can be used, for example, as an intermediate of the perfume glycoside as described above to obtain a β-D-glucoside of a perfume compound, and the β-form is α-form D-glucoside.
Since it is superior in hydrolyzability and microbial degradability to glucoside, it can easily release fragrance substances due to, for example, resident bacteria, and is industrially more practical and important. Therefore, in order to obtain a β-glycoside, it is more advantageous to use β-acetylated glucose as a raw material, and a method for producing the same has been proposed. For example, it is a production method by vigorous reaction at high temperature, in which glucose is added under reflux of acetic anhydride in the presence of an acidic catalyst and reacted [Methods, Carbohy].
dr. Chem. 2 , 211-215, (196
3)]. However, exhaustion of acetic acid vapor is unavoidable in this production method, and environmental measures such as deterioration of the working environment and installation of exhaust cleaning equipment are required, and if the reaction temperature is lowered, α-
The formation of the isomer increases, and the yield of the desired β-isomer decreases. On the other hand, a method for obtaining an acetyl derivative of a saccharide at a mild reaction temperature of 100 ° C. or lower using acetic acid as a reaction solvent (JP-A-10-237084), or using a lower alkyl ester of acetic acid such as ethyl acetate or butyl acetate as a solvent A method for producing a fully acetylated monosaccharide or oligosaccharide in which the reaction is carried out at a temperature of 80 to 120 ° C. (JP-A-62-42996) has been proposed. There is no description about α-form and β-form, and it is hard to say that it is a production method of β-form. In the latter, a large amount of acetic acid wastewater is generated, which is industrially problematic.

【0003】[0003]

【発明が解決しようとする課題】上記のように、ペンタ
アセチル−β−D−グルコース(以下、PAGと略称す
ることがある)が各種配糖体の合成中間原料として需要
が大きくなっている現状から、工業的に安全で安価なP
AGを高収率且つ高純度で得ることができる製造方法が
求められていた。
As described above, there is a growing demand for pentaacetyl-β-D-glucose (hereinafter sometimes abbreviated as PAG) as an intermediate material for synthesizing various glycosides. From industrially safe and cheap P
There has been a demand for a production method capable of obtaining AG with high yield and high purity.

【0004】[0004]

【課題を解決するための手段】そこで本発明者らは上記
課題を解決するため、安全性、経済性にも考慮しつつ、
高純度かつ高収率でPAGを製造することができる方法
を鋭意研究した結果、従来の製造方法においては衛生安
全面で問題のある苛酷な条件で製造されていたβ−体ア
セチル化グルコースを、工業的に有利に製造する方法を
見出し本発明を完成した。即ち、本発明は、グルコース
を非プロトン性溶媒の存在下、無水酢酸と反応させるこ
とにより、温和な反応でPAGを高純度かつ高収率で製
造する方法である。
Means for Solving the Problems In order to solve the above-mentioned problems, the present inventors have considered safety and economic efficiency,
As a result of intensive research on a method capable of producing PAG with high purity and high yield, β-form acetylated glucose produced under severe conditions having problems in terms of hygiene and safety in the conventional production method is The present invention has been completed by finding a method for producing it industrially advantageously. That is, the present invention is a method for producing PAG with high purity and high yield by a mild reaction by reacting glucose with acetic anhydride in the presence of an aprotic solvent.

【0005】[0005]

【発明の実施の形態】以下、本発明の実施態様について
詳細に説明する。
DESCRIPTION OF THE PREFERRED EMBODIMENTS Hereinafter, embodiments of the present invention will be described in detail.

【0006】本発明は、非プロトン性溶媒にグルコース
及び無水酢酸を添加して130℃以下で加熱し、ペンタ
アセチル−β−D−グルコースを得る方法である。
The present invention is a method for obtaining pentaacetyl-β-D-glucose by adding glucose and acetic anhydride to an aprotic solvent and heating at 130 ° C. or lower.

【0007】本発明で用いるグルコースは、特に純度は
問わないが、好ましくは無水ブドウ糖が望ましい。ま
た、無水酢酸も工業用に用いられるものであれば、特に
純度は問わない。
[0007] The glucose used in the present invention may be of any purity, but is preferably anhydrous glucose. Also, the purity of acetic anhydride is not particularly limited as long as it is used for industrial purposes.

【0008】また、本発明で用いる非プロトン性溶媒と
しては、炭化水素、好ましくは、芳香族炭化水素、より
好ましくは、トルエン、キシレン、トリメチルベンゼン
を挙げることができる。これら非プロトン性溶媒は、反
応温度を制御できる反応溶媒として優れているばかりで
なく、生成したPAGの抽出溶媒として、また、再結晶
溶媒としても使用でき、本発明が工業的に有利である所
以である。
The aprotic solvent used in the present invention includes hydrocarbons, preferably aromatic hydrocarbons, more preferably toluene, xylene and trimethylbenzene. These aprotic solvents are not only excellent as reaction solvents capable of controlling the reaction temperature, but also can be used as an extraction solvent for the produced PAG and as a recrystallization solvent, which is why the present invention is industrially advantageous. It is.

【0009】本発明の反応は、グルコースの1〜5倍重
量、好ましくは、2〜3倍重量の非プロトン性溶媒にグ
ルコース及び反応触媒として、例えば、酢酸ナトリウム
を添加して加熱し、グルコースの5〜10倍当量、好ま
しくは、6〜8倍当量の無水酢酸を1〜5時間で滴下し
ながら行う反応である。反応温度は、80〜130℃、
好ましくは、100〜115℃の温度で行い、滴下終了
後も5〜10時間反応を続行させる。
In the reaction of the present invention, glucose is added to an aprotic solvent having a weight of 1 to 5 times, preferably 2 to 3 times the weight of glucose and, for example, sodium acetate as a reaction catalyst is added thereto, and the mixture is heated. The reaction is carried out while dropping 5 to 10 equivalents, preferably 6 to 8 equivalents of acetic anhydride in 1 to 5 hours. The reaction temperature is 80 to 130 ° C,
Preferably, the reaction is performed at a temperature of 100 to 115 ° C., and the reaction is continued for 5 to 10 hours after the completion of the dropwise addition.

【0010】なお、本発明で用いる反応触媒としては、
例えば、酢酸ナトリウム、ピリジン、硫酸、燐酸などを
挙げることができるが、好ましくは、酢酸ナトリウムを
グルコースに対して、0.01〜5倍当量、好ましく
は、0.05〜2倍当量用いるのがよい。
The reaction catalyst used in the present invention includes:
For example, sodium acetate, pyridine, sulfuric acid, phosphoric acid and the like can be mentioned. Preferably, sodium acetate is used in an amount of 0.01 to 5 equivalents, preferably 0.05 to 2 equivalents, based on glucose. Good.

【0011】反応終了後、生成したPAGを結晶化、再
結晶化処理により精製し、高純度のPAGを得ることが
できる。
After completion of the reaction, the produced PAG is purified by crystallization and recrystallization to obtain a high-purity PAG.

【0012】[0012]

【実施例】以下実施例により本発明の実施の態様を具体
的に説明する。
The embodiments of the present invention will be specifically described below with reference to examples.

【0013】実施例1 100l反応釜にp−キシレン20.6kg、無水ブド
ウ糖10.3kg(57.1モル)、及び酢酸ナトリウ
ム0.3kgを加えて撹拌加熱し、溶液温度が約100
℃になつたら、無水酢酸35kg(343モル)を徐々
に2時間かけて滴下する。反応温度を105〜110℃
に調整しながら滴下終了後も約6時間反応を続行する。
反応終了後、p−キシレン及び酢酸を減圧蒸留して回収
する。次いで、回収残渣にトルエンを加えて加熱溶解
し、該トルエン溶液を45〜50℃の温度で水洗した後
冷却して、再結晶させる。トルエンを濾過分離後、乾燥
して無色の結晶19.2kgを得た。得られた結晶の分
析結果から、β体の単一成分であるPAGであることを
確認した。純度99.7%、収率86%。
EXAMPLE 1 20.6 kg of p-xylene, 10.3 kg (57.1 mol) of anhydrous glucose, and 0.3 kg of sodium acetate were added to a 100-liter reactor, and the mixture was stirred and heated.
When the temperature reaches ℃, 35 kg (343 mol) of acetic anhydride is gradually added dropwise over 2 hours. Reaction temperature of 105-110 ° C
The reaction is continued for about 6 hours after the completion of the dropwise addition while adjusting the pH.
After completion of the reaction, p-xylene and acetic acid are recovered by distillation under reduced pressure. Next, toluene is added to the collected residue and dissolved by heating. The toluene solution is washed with water at a temperature of 45 to 50 ° C., cooled, and recrystallized. After the toluene was separated by filtration, it was dried to obtain 19.2 kg of colorless crystals. From the analysis results of the obtained crystals, it was confirmed that the PAG was a single component of the β-form. Purity 99.7%, yield 86%.

【0014】実施例2 実施例1の反応溶媒として用いたp−キシレンに代え
て、トルエンを用いた他は実施例1と全く同様にして、
PAG18.5kgを得た。純度99.6%、収率83
%。
Example 2 In the same manner as in Example 1 except that toluene was used instead of p-xylene used as the reaction solvent in Example 1,
18.5 kg of PAG were obtained. Purity 99.6%, yield 83
%.

【0015】[0015]

【発明の効果】本発明によれば、工業的に安全且つ安価
で、しかも高純度かつ高収率でペンタアセチル−β−D
−グルコースを製造することができる。
According to the present invention, pentaacetyl-β-D is industrially safe and inexpensive, and has high purity and high yield.
-Glucose can be produced.

Claims (2)

【特許請求の範囲】[Claims] 【請求項1】 グルコースを非プロトン性溶媒の存在
下、無水酢酸と反応させることを特徴とする、ペンタア
セチル−β−D−グルコースの製造方法。
1. A process for producing pentaacetyl-β-D-glucose, which comprises reacting glucose with acetic anhydride in the presence of an aprotic solvent.
【請求項2】 非プロトン性溶媒が芳香族炭化水素であ
る、請求項1記載のペンタアセチル−β−D−グルコー
スの製造方法。
2. The method for producing pentaacetyl-β-D-glucose according to claim 1, wherein the aprotic solvent is an aromatic hydrocarbon.
JP37559798A 1998-12-17 1998-12-17 Method for producing pentaacetyl-β-D-glucose Pending JP2000178294A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP37559798A JP2000178294A (en) 1998-12-17 1998-12-17 Method for producing pentaacetyl-β-D-glucose

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP37559798A JP2000178294A (en) 1998-12-17 1998-12-17 Method for producing pentaacetyl-β-D-glucose

Publications (1)

Publication Number Publication Date
JP2000178294A true JP2000178294A (en) 2000-06-27

Family

ID=18505770

Family Applications (1)

Application Number Title Priority Date Filing Date
JP37559798A Pending JP2000178294A (en) 1998-12-17 1998-12-17 Method for producing pentaacetyl-β-D-glucose

Country Status (1)

Country Link
JP (1) JP2000178294A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US6350865B1 (en) * 1999-02-19 2002-02-26 Nisshin Pharma Inc. Process for the preparation of pentaacetyl-β-D-glucopyranose
JP2007269765A (en) * 2006-03-31 2007-10-18 National Institute Of Advanced Industrial & Technology Method and apparatus for producing saccharide acyl compounds

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US6350865B1 (en) * 1999-02-19 2002-02-26 Nisshin Pharma Inc. Process for the preparation of pentaacetyl-β-D-glucopyranose
JP2007269765A (en) * 2006-03-31 2007-10-18 National Institute Of Advanced Industrial & Technology Method and apparatus for producing saccharide acyl compounds

Similar Documents

Publication Publication Date Title
RU2230748C2 (en) Method for preparing clarithromycin as crystals of form ii
EP0342990A2 (en) Process for preparing erythromycin A oxime or a salt therof
JP2546659B2 (en) Method for producing podophyllotoxin type compound
EP0418925B1 (en) Method of producing (S)-4-hydroxymethyl-gamma-lactone
US4464527A (en) Antibacterial 9-deoxo-9a-alkyl-9a-aza-9a-homoerythromycin A derivatives and intermediates therefore
JP3231765B2 (en) Method for producing demethyl epipodophyllotoxin
KR20040043169A (en) Process for the production of beraprost and its salts
KR20040031784A (en) Process for the preparation of l-ribavirin
HUP0003399A2 (en) An improved process for the production of an antiparasitic substance
HU209724B (en) Process for preparing glucosidase inhibitors and pharmaceutical comp. contg. them
JP3029806B2 (en) Glycosidation of colchicine derivative and product thereof
PT94337A (en) PROCESS FOR TIGOGENIN BETA-CELOBIOSIDE SYNTHESIS
JP2000178294A (en) Method for producing pentaacetyl-β-D-glucose
EP2963048B1 (en) Method for producing alpha-halo-tetraacyl glucose
EP0389110A2 (en) Process for the preparation of 2'-deoxy-5-trifluoromethyl-beta-uridine
JP2002201192A (en) Novel synthetic method of febrifudine and febrifudine compound
US20040158059A1 (en) Process for the preparation of ribofuranose derivatives
Xiao et al. Convenient Synthesis of D‐Talose from D‐Galactose
HUP0102333A2 (en) Morphine-6-glucuronide synthesis
NO312593B1 (en) Process for preparing a deoxyuridine derivative
JPH051053A (en) New method for producing 6- (3-dimethylaminopropionyl) forskolin
JP4115066B2 (en) Carbohydrate amidine derivatives
HUP0102297A2 (en) Process for the preparation of 4,5-epoxymorphinan-6-oxyglucuronides
US6841183B2 (en) Process for producing aspartame derivatives, process for purifying aspartame derivatives, production intermediates, and process for producing production intermediates
JPH031317B2 (en)