JP2000336101A - Production of hydroxypropyl cellulose - Google Patents

Production of hydroxypropyl cellulose

Info

Publication number
JP2000336101A
JP2000336101A JP11151166A JP15116699A JP2000336101A JP 2000336101 A JP2000336101 A JP 2000336101A JP 11151166 A JP11151166 A JP 11151166A JP 15116699 A JP15116699 A JP 15116699A JP 2000336101 A JP2000336101 A JP 2000336101A
Authority
JP
Japan
Prior art keywords
cellulose
propylene oxide
added
weight
relative viscosity
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.)
Withdrawn
Application number
JP11151166A
Other languages
Japanese (ja)
Inventor
Hideaki Omura
英明 大村
Toshiaki Yoneda
利明 米田
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.)
Nippon Soda Co Ltd
Original Assignee
Nippon Soda 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 Nippon Soda Co Ltd filed Critical Nippon Soda Co Ltd
Priority to JP11151166A priority Critical patent/JP2000336101A/en
Publication of JP2000336101A publication Critical patent/JP2000336101A/en
Withdrawn legal-status Critical Current

Links

Abstract

PROBLEM TO BE SOLVED: To obtain the subject cellulose capable of reducing the amount of propylene oxide while maintaining qualities, excellent not only in an economical aspect but also in an environmental aspect, useful as a medicine additive by using a cellulose having a high relative viscosity. SOLUTION: (B) Propylene oxide is added to (A) a cellulose of formula I (n is 100-2,000) having >=12 relative viscosity to give the objective cellulose of formula II [R is (CH2-CH(CH3)-O)m--H] (m is 0 or 1-5). Preferably 1 pt.wt. of the component A is reacted with <=2.5 pts.wt. of the component B. For example, the component A, an organic solvent such as toluene, etc., an aqueous solution of sodium hydroxide are fed to a reactor, mixed and the mixed solution is reacted with the component B.

Description

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

【0001】[0001]

【発明が属する技術分野】本発明は、特に医薬品添加物
として有用なヒドロキシプロピルセルロース(HPC)
の製造法に関する。
The present invention relates to hydroxypropylcellulose (HPC) which is particularly useful as an excipient.
A method for producing the same.

【0002】[0002]

【従来の技術】HPCは一般にセルロースに水酸化ナト
リウム等の存在下、酸化プロピレンを付加させて製造さ
れている(特開平2−235901号)。そして、酸化
プロピレンの付加量が小さいとHPCが低分子となるた
め、洗浄した際、排水に溶けて収率が低下するため、通
常、セルロース1重量部に対し、HPCとして2.10
重量部(以下、重量パルプ比という)前後となるまで酸
化プロピレンを添加している。通常に用いられている相
対粘度11前後のセルロ−スを用いた場合、酸化プロピ
レンはセルロース1重量部に対し、2.6〜2.7重量
部必要であった。しかし過剰の酸化プロピレンは式(II
I)で表されるプロピレングリコ−ル類となって排水中
にいってしまうため、経済的な面からだけでなく、環境
面からも酸化プロピレンの量を減らすことは重要な問題
であった。
2. Description of the Related Art In general, HPC is produced by adding propylene oxide to cellulose in the presence of sodium hydroxide or the like (JP-A-2-235901). If the added amount of propylene oxide is small, the HPC becomes a low molecular weight, and when washed, the HPC is dissolved in waste water and the yield is reduced.
Propylene oxide is added until it is around the weight part (hereinafter referred to as weight pulp ratio). When cellulose having a relative viscosity of about 11, which is commonly used, was used, 2.6 to 2.7 parts by weight of propylene oxide was required for 1 part by weight of cellulose. However, the excess propylene oxide is of the formula (II
Since the propylene glycol represented by the formula (I) is contained in wastewater, it is important to reduce the amount of propylene oxide not only from an economical point of view but also from an environmental point of view.

【0003】[0003]

【化3】 Embedded image

【0004】(式中、lは1から4の整数を示す。)(Where l represents an integer of 1 to 4)

【0005】[0005]

【課題を解決するための手段】本発明者は、上記問題点
を解決すべく鋭意研究した結果、相対粘度の高いセルロ
ースを用いることにより製品の維持したまま、酸化プロ
ピレンの量を減らせることを見いだし、本発明を完成し
た。
Means for Solving the Problems The inventors of the present invention have made intensive studies to solve the above problems, and as a result, have found that the use of cellulose having a high relative viscosity can reduce the amount of propylene oxide while maintaining the product. We have found and completed the present invention.

【0006】即ち、本発明は式(I)で表される相対粘
度12以上のセルロースに酸化プロピレンを付加させる
ことを特徴とする式(II)で表されるHPCの製造法で
ある。
That is, the present invention is a process for producing HPC represented by the formula (II), wherein propylene oxide is added to cellulose having a relative viscosity of 12 or more represented by the formula (I).

【0007】[0007]

【化4】 Embedded image

【0008】[0008]

【化5】 Embedded image

【0009】[式中、nは100から2000を、Rは
- (CH2 - CH(CH3) - O)m - H (式中mは0又は1から
5の整数を示す。但し、式(II)中のRの全てが同時に
m=0ではない。)を示す。]
[Wherein n is from 100 to 2000, and R is
-(CH 2 -CH (CH 3 ) -O) m -H (where m represents 0 or an integer of 1 to 5, provided that not all R in the formula (II) are m = 0 at the same time). ). ]

【0010】[0010]

【発明の実施の形態】本発明に用いる相対粘度12以上
のセルロースとしては、特に制限はないが、あまり粘度
が高いと反応時の撹拌が困難となる等の問題が生じるの
で30以下が好ましく、特に14から20のセルロース
が好ましい。本発明の製造法を実施するにはセルロー
ス、有機溶媒、水酸化ナトリウム水溶液を反応容器に加
え混合する。この混合液に、酸化プロピレンを加え反応
させる。加える酸化プロピレンは、付加が均一になるよ
う通常2回に分けて加える。加える割合は、1回目にセ
ルロース1重量部に対し酸化プロピレン2重量部前後、
2回目に残りを加える方法が好ましい。反応終了後は有
機溶媒を除去した後、温水洗浄等を行うことにより目的
物を得ることができる。
BEST MODE FOR CARRYING OUT THE INVENTION The cellulose having a relative viscosity of 12 or more used in the present invention is not particularly limited. Particularly, 14 to 20 cellulose is preferable. To carry out the production method of the present invention, cellulose, an organic solvent and an aqueous solution of sodium hydroxide are added to a reaction vessel and mixed. Propylene oxide is added to this mixed solution and reacted. The propylene oxide to be added is usually added in two portions so that the addition becomes uniform. The proportion to be added is about 2 parts by weight of propylene oxide per 1 part by weight of cellulose for the first time,
The method of adding the remainder the second time is preferred. After completion of the reaction, the target compound can be obtained by removing the organic solvent and then performing washing with warm water or the like.

【0011】本発明に用いる有機溶媒としては、トルエ
ン等反応に不活性な溶媒が使用でき、その使用量は、セ
ルロース1重量部に対し、1から10重量部である。水
酸化ナトリウム水溶液の濃度は特に制限はないが通常2
0%前後が好ましく、その使用量はセルロース1重量部
に対し、20%水溶液の場合、0.1重量部から1重量
部である。使用する酸化プロピレンの量は、多くても品
質には影響ないが、前述したとおり、経済性、環境面か
らセルロース1重量部に対し、2.2から2.5重量部
が好ましい。
As the organic solvent used in the present invention, a solvent inert to the reaction such as toluene can be used, and the amount of the solvent used is 1 to 10 parts by weight based on 1 part by weight of cellulose. The concentration of the aqueous sodium hydroxide solution is not particularly limited, but is usually 2
The amount is preferably about 0%, and the amount is 0.1 to 1 part by weight in the case of a 20% aqueous solution with respect to 1 part by weight of cellulose. Although the amount of propylene oxide used does not affect the quality at most, it is preferably from 2.2 to 2.5 parts by weight based on 1 part by weight of cellulose from the viewpoint of economy and environment as described above.

【0012】[0012]

【実施例】次に実施例を挙げ本発明を更に詳細に説明す
る。 実施例1(相対粘度14.6のセルロース(I)を用い
て、2回目に加える酸化プロピレンの量を8%減らした
実験(C))
Next, the present invention will be described in more detail by way of examples. Example 1 (Experiment (C) in which the amount of propylene oxide added for the second time was reduced by 8% using cellulose (I) having a relative viscosity of 14.6)

【0013】反応容器にセルロース(I)220g、2
0%水酸化ナトリウム水溶液85g、トルエン752g
を窒素置換しながら室温で撹拌させた。昇温させながら
1回目の酸化プロピレン463gを加えて80℃で熟成
させ、冷却した後、2回目の酸化プロピレン72gを加
え更に85℃で熟成させた。反応液はトルエンを除去し
た後温水で洗浄し、真空乾燥させてヒドロキシプロピル
セルロース(II)(重量パルプ比2.14)を得た。
In a reaction vessel, 220 g of cellulose (I), 2 g
85 g of 0% sodium hydroxide aqueous solution, 752 g of toluene
Was stirred at room temperature while replacing with nitrogen. While raising the temperature, 463 g of the first propylene oxide was added and the mixture was aged at 80 ° C., and after cooling, 72 g of the second propylene oxide was added and the mixture was further aged at 85 ° C. After removing toluene, the reaction solution was washed with warm water and dried under vacuum to obtain hydroxypropylcellulose (II) (weight pulp ratio: 2.14).

【0014】実施例2(相対粘度18.5のセルロース
(I)を用いて、2回目に加える酸化プロピレンの量を
8%減らした実験(C))
Example 2 (Experiment (C) using cellulose (I) having a relative viscosity of 18.5 and reducing the amount of propylene oxide added second time by 8%)

【0015】反応容器にセルロース(I)220g、2
0%水酸化ナトリウム水溶液85g、トルエン752g
を窒素置換しながら室温で撹拌させた。昇温させながら
1回目の酸化プロピレン463gを加えて80℃で熟成
させ、冷却した後、2回目の酸化プロピレン72gを加
え更に85℃で熟成させた。反応液はトルエンを除去し
た後温水で洗浄し、真空乾燥させてヒドロキシプロピル
セルロース(II)(重量パルプ比2.09)を得た。
In a reaction vessel, 220 g of cellulose (I), 2 g
85 g of 0% sodium hydroxide aqueous solution, 752 g of toluene
Was stirred at room temperature while replacing with nitrogen. While raising the temperature, 463 g of the first propylene oxide was added and the mixture was aged at 80 ° C., and after cooling, 72 g of the second propylene oxide was added and the mixture was further aged at 85 ° C. After removing toluene, the reaction solution was washed with warm water and dried under vacuum to obtain hydroxypropylcellulose (II) (pulp weight ratio: 2.09).

【0016】比較例1(相対粘度6.9のセルロース
(I)を用いて、2回目に加える酸化プロピレンの量を
4%減らした実験(B))
Comparative Example 1 (Experiment (B) in which the amount of propylene oxide added for the second time was reduced by 4% using cellulose (I) having a relative viscosity of 6.9)

【0017】反応容器にセルロース(I)220g、2
0%水酸化ナトリウム水溶液85g、トルエン752g
を窒素置換しながら室温で撹拌させた。昇温させながら
1回目の酸化プロピレン463gを加えて80℃で熟成
させ、冷却した後、2回目の酸化プロピレン96gを加
え更に85℃で熟成させた。反応液はトルエンを除去し
た後温水で洗浄し、真空乾燥させてヒドロキシプロピル
セルロース(II)(重量パルプ比1.95)を得た。
In a reaction vessel, 220 g of cellulose (I), 2 g
85 g of 0% sodium hydroxide aqueous solution, 752 g of toluene
Was stirred at room temperature while replacing with nitrogen. While raising the temperature, 463 g of the first propylene oxide was added and the mixture was aged at 80 ° C., and after cooling, 96 g of the second propylene oxide was added and the mixture was further aged at 85 ° C. After removing toluene, the reaction solution was washed with warm water and dried under vacuum to obtain hydroxypropylcellulose (II) (weight pulp ratio: 1.95).

【0018】比較例2(相対粘度11.3のセルロース
(I)を用いての標準実験(A))
Comparative Example 2 (Standard experiment (A) using cellulose (I) having a relative viscosity of 11.3)

【0019】反応容器にセルロース(I)220g、2
0%水酸化ナトリウム水溶液85g、トルエン752g
を窒素置換しながら室温で撹拌させた。昇温させながら
1回目の酸化プロピレン463gを加えて80℃で熟成
させ、冷却した後、2回目の酸化プロピレン120gを
加え更に85℃で熟成させた。反応液はトルエンを除去
した後温水で洗浄し、真空乾燥させてヒドロキシプロピ
ルセルロース(II)(重量パルプ比2.11)を得た。
In a reaction vessel, 220 g of cellulose (I), 2
85 g of 0% sodium hydroxide aqueous solution, 752 g of toluene
Was stirred at room temperature while replacing with nitrogen. While raising the temperature, 463 g of propylene oxide for the first time was added and aged at 80 ° C., and after cooling, 120 g of propylene oxide for the second time was added and further aged at 85 ° C. After removing toluene, the reaction solution was washed with warm water and dried under vacuum to obtain hydroxypropyl cellulose (II) (weight pulp ratio: 2.11).

【0020】比較例3(相対粘度11.3のセルロース
(I)を用いて、2回目に加える酸化プロピレンの量を
4%減らした実験(B))
Comparative Example 3 (Experiment (B) using cellulose (I) having a relative viscosity of 11.3 and reducing the amount of propylene oxide to be added for the second time by 4%)

【0021】反応容器にセルロース(I)220g、2
0%水酸化ナトリウム水溶液85g、トルエン752g
を窒素置換しながら室温で撹拌させた。昇温させながら
1回目の酸化プロピレン463gを加えて80℃で熟成
させ、冷却した後、2回目の酸化プロピレン96gを加
え更に85℃で熟成させた。反応液はトルエンを除去し
た後温水で洗浄し、真空乾燥させてヒドロキシプロピル
セルロース(II)(重量パルプ比2.06)を得た。
In a reaction vessel, 220 g of cellulose (I), 2 g
85 g of 0% sodium hydroxide aqueous solution, 752 g of toluene
Was stirred at room temperature while replacing with nitrogen. While raising the temperature, 463 g of the first propylene oxide was added and the mixture was aged at 80 ° C., and after cooling, 96 g of the second propylene oxide was added and the mixture was further aged at 85 ° C. After removing toluene, the reaction solution was washed with warm water and dried under vacuum to obtain hydroxypropylcellulose (II) (pulp weight ratio: 2.06).

【0022】以下に酸化プロピレンの量の違いによる重
量パルプ比の比較を含め表1に示した。
The results are shown in Table 1 below, including a comparison of the weight pulp ratio depending on the amount of propylene oxide.

【0023】[0023]

【表1】 [Table 1]

【0024】[0024]

【発明の効果】本発明によれば、相対粘度の高いセルロ
ースを用いることにより重量パルプ比を下げることな
く、酸化プロピレンの量を減らすことができる。また酸
化プロピレンの減量により、副生成物であるポリプロピ
レングリコ−ル類を抑制することができ洗浄した際排水
に含まれる比率を減少させることができ、環境が大幅に
改善される。
According to the present invention, by using cellulose having a high relative viscosity, the amount of propylene oxide can be reduced without lowering the weight pulp ratio. In addition, by reducing the amount of propylene oxide, it is possible to suppress polypropylene glycols which are by-products, to reduce the ratio contained in the wastewater when washed, and to greatly improve the environment.

Claims (2)

【特許請求の範囲】[Claims] 【請求項1】 式(I)で表される相対粘度12以上の
セルロースに酸化プロピレンを付加させることを特徴と
する式(II)で表されるヒドロキシプロピルセルロース
の製造法。 【化1】 【化2】 [式中、nは100から2000を、Rは - (CH2 - CH
(CH3) - O)m - H (式中mは0又は1から5の整数を示
す。但し、式(II)中のRの全てが同時にm=0ではな
い。)を示す。]
1. A method for producing hydroxypropyl cellulose represented by the formula (II), wherein propylene oxide is added to cellulose having a relative viscosity of 12 or more represented by the formula (I). Embedded image Embedded image Wherein n is from 100 to 2000 and R is-(CH 2 -CH
(CH 3 ) -O) m -H (where m represents 0 or an integer of 1 to 5, provided that not all Rs in the formula (II) are simultaneously m = 0). ]
【請求項2】 セルロース1重量部に対し、酸化プロピ
レン2.5重量部以下で反応させる請求項1記載の製造
法。
2. The process according to claim 1, wherein the reaction is carried out with 2.5 parts by weight of propylene oxide per 1 part by weight of cellulose.
JP11151166A 1999-05-31 1999-05-31 Production of hydroxypropyl cellulose Withdrawn JP2000336101A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP11151166A JP2000336101A (en) 1999-05-31 1999-05-31 Production of hydroxypropyl cellulose

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP11151166A JP2000336101A (en) 1999-05-31 1999-05-31 Production of hydroxypropyl cellulose

Publications (1)

Publication Number Publication Date
JP2000336101A true JP2000336101A (en) 2000-12-05

Family

ID=15512775

Family Applications (1)

Application Number Title Priority Date Filing Date
JP11151166A Withdrawn JP2000336101A (en) 1999-05-31 1999-05-31 Production of hydroxypropyl cellulose

Country Status (1)

Country Link
JP (1) JP2000336101A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2010095674A1 (en) * 2009-02-20 2010-08-26 住友精化株式会社 Method for producing hydroxyalkyl cellulose

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2010095674A1 (en) * 2009-02-20 2010-08-26 住友精化株式会社 Method for producing hydroxyalkyl cellulose
JPWO2010095674A1 (en) * 2009-02-20 2012-08-30 住友精化株式会社 Method for producing hydroxyalkyl cellulose
JP5586575B2 (en) * 2009-02-20 2014-09-10 住友精化株式会社 Method for producing hydroxyalkyl cellulose

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