JPH0138403B2 - - Google Patents

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Publication number
JPH0138403B2
JPH0138403B2 JP18573682A JP18573682A JPH0138403B2 JP H0138403 B2 JPH0138403 B2 JP H0138403B2 JP 18573682 A JP18573682 A JP 18573682A JP 18573682 A JP18573682 A JP 18573682A JP H0138403 B2 JPH0138403 B2 JP H0138403B2
Authority
JP
Japan
Prior art keywords
cellulose
alkali
surfactant
water
parts
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.)
Expired
Application number
JP18573682A
Other languages
Japanese (ja)
Other versions
JPS5975902A (en
Inventor
Akira Shigematsu
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.)
Daicel Corp
Original Assignee
Daicel Chemical 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 Daicel Chemical Industries Ltd filed Critical Daicel Chemical Industries Ltd
Priority to JP18573682A priority Critical patent/JPS5975902A/en
Publication of JPS5975902A publication Critical patent/JPS5975902A/en
Publication of JPH0138403B2 publication Critical patent/JPH0138403B2/ja
Granted legal-status Critical Current

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  • Polysaccharides And Polysaccharide Derivatives (AREA)

Description

【発明の詳細な説明】 本発明は水溶性のヒドロキシエチルセルロース
を製造する方法に係り、さらに詳しくはセルロー
ス原料を有機溶剤と水からなる媒体中スラリー状
態にてアルカリを作用させてアルカリセルロース
を生成させる際に界面活性剤を添加して行ない、
引続き界面活性剤の存在下に酸化エチレンを反応
させることにより、製品の水溶液の透視度の著し
く改善されたヒドロキシエチルセルロースを与え
る製造法に関するものである。 一般にヒドロキシエチルセルロースの製造は、
イソプロピルアルコール(IPA)、第三ブチルア
ルコール(TBA)などの低級脂肪族アルコール、
水、アルカリの混合液中スラリー状態にてセルロ
ース原料をアルカリと反応せしめてアルカリセル
ロースとすることにより開始される。このアルカ
リセルロースが生成される過程での溶液相の状態
は、これら低級脂肪族アルコールとアルカリ水溶
液とが互に相溶しないため、二層に分離したまま
でセルロース原料と反応せしめられることにな
り、セルロースに対するアルカリの均一な浸透は
必ずしも順調には進行しない。さらに引続き行わ
れる酸化エチレンとの反応においても同様に不均
一な系で反応が進むため、従来技術では最終製品
の重要な性質である水溶液の濁度および浮遊物の
減少に限界があり、透視度の優れたものが得にく
い欠点を有していた。 本発明者は、ヒドロキシエチルセルロースの水
溶液の溶解特性が著しく改良されたヒドロキシエ
チルセルロースの製造法について鋭意研究した結
果、アルカリセルロースを生成させる際に界面活
性剤を添加してセルロースへのアルカリの浸透性
を高め、引続き界面活性剤の存在下においてアル
カリセルロースと酸化エチレンを反応させること
により目的を達成できることを見い出した。 本発明に使用する原料セルロースは、通常化学
反応に用いられる木材パルプ、リンターなど何れ
でもよい。また原料セルロースは反応に先立ち粉
砕機により容易にそのスラリーが撹拌できる程度
の大きさに粉砕しておくのが望ましい。また、使
用するアルカリは水酸化ナトリウム、水酸化カリ
ウム、水酸化リチウムの何れでもよいが、工業的
には水酸化ナトリウムが通常用いられる。 本発明の実施に当つての好ましい反応仕込組成
及び操作条件としては、分散媒であるイソプロピ
ルアルコール(IPA)、第ブチルアルコール
(TBA)などの有機溶剤と水の合計重量がセルロ
ースに対して5〜15倍のスラリー系に於て、水/
セルロースの重量比が1.5〜3.0の範囲、アルカ
リ/セルロースの重量比が0.25〜0.50の範囲にお
いて、界面活性剤が有機溶剤と水の合計重量に対
して0.1〜10重量%、好ましくは0.2〜1重量%添
加され、反応温度10〜40℃において30〜200分撹
拌混合してアルカリセルロースを製造する。引続
きセルロース1部に対し0.8〜1.2部の酸化エチレ
ンを加え、反応温度30〜80℃において1〜4時間
反応させればよい。 本発明に使用する界面活性剤としては、アルキ
ルナフタレンスルホン酸ナトリウム、ラウリル硫
酸ナトリウム、アルキルベンゼンスルホン酸ナト
リウム、ポリオキシエチレンアルキルエーテル硫
酸ナトリウム、ポリオキシエチレンアルキルフエ
ノールエーテル硫酸ナトリウム、アルキルナフタ
レンスルホン酸ナトリウム、ポリオキシエチレン
アルキルフエノールエーテル、アルキルトリメチ
ルアンモニウムクロライドなどのアニオン性、ノ
ニオン性、及びカチオン性界面活性剤が挙げられ
るが、これらに限定されるものではない。 界面活性剤の添加方法は、有機溶剤と水の混合
液中に界面活性剤を添加後、セルロースを撹拌分
散させたのちアルカリ水溶液を滴下する方法、有
機溶剤と水の混合液にあらかじめセルロースを撹
拌分散させておき、界面活性剤を溶解したアルカ
リ水溶液を滴下する方法、又は有機溶剤、水、界
面活性剤及びアルカリの混合液中にセルロースを
撹拌下に分散させる方法の何れもが採用できる。 以下実施例及び比較例によつて本発明を説明す
る。部は重量部を表わす。 比較例 撹拌装置付の1セパラブルフラスコに第三ブ
チルアルコール12.8部と12.7%水酸化ナトリウム
水溶液2.5部を加えて混合し、これにリンター1
部を加えて、撹拌下に20℃で60分間アルセル化反
応を行つた。ついで酸化エチレン0.95部を加え10
分混合し、その後50〜75℃で3時間ヒドロキシエ
チル化反応を行つた。反応物を酢酸で中和した
後、反応生成物を過し、メタノール/アセトン
混合液で2回洗浄後別し乾燥した。得られたヒ
ドロキシエチルセルロースの1%水溶液の粘度は
3600cps、JIS法(K0102)より測定した透視度は
140mmであつた。 実施例 1 撹拌装置付の1フラスコに第三ブタノール
(94.6重量%濃度、残部水)13.6部とポリオキシ
エチレンラウリルエーテル硫酸ナトリウム(オキ
シエチレンモル数n=20)を0.045部加え、これ
にあらかじめ粉砕したリンター1部を加えてよく
混合した。これに18.3%水酸化ナトリウム水溶液
1.75部を約10分で滴下した。界面活性剤の溶剤と
水の合計量に対する添加量は0.3重量%である。
60分間撹拌を続けてアルカリセルロースとし、つ
いで50〜75℃で3時間かけて酸化エチレン0.95部
を反応させた後、比較例の方法で後処理を行つ
た。得られたヒドロキシエチルセルロースの1%
水溶液の粘度は3300cpsであり、JIS法で測定した
透視度は440mmであつて、比較例で得られたもの
に較べ透視度が著しく改善された。 実施例 2 界面活性剤としてポリオキシエチレンラウリル
エーテル硫酸ナトリウム(オキシエチレンモル数
n=50)を0.045部使用したほかは実施例1と同
様にしてヒドロキシエチルセルロースの製造を行
なつた。得られたヒドロキシエチルセルロースの
1%水溶液の粘度は3560cpsであり、透視度が520
mmであつて、比較例で得られたものに比し著しく
澄明であつた。 実施例 3 第三ブチルアルコール(94.6重量%濃度、残部
水)13.6部に細粉化したリンター1部を加えてよ
く撹拌する。これにポリオキシエチレンオクチル
フエノールエーテル硫酸ナトリウム0.015部を含
む18.6%水酸化ナトリウム水溶液1.74部を60分か
けて滴下してアルカリセルロースとし、ついで酸
化エチレン0.98部を加え50〜75℃で3時間反応を
行ない、比較例の方法で後処理した。界面活性剤
の溶媒と水に対する添加量は0.1重量%である。
得られた製品の1%水溶液の粘度は3900cpsで、
JIS法による透視度は400mmであつた。比較例に比
し著しく透視度の改善されたヒドロキシエチルセ
ルロースが得られた。 実施例 4〜11 実施例1に示した方法に於て界面活性剤として
表−1に示した各種の界面活性剤を使用した以外
は同様にしてヒドロキシエチルセルロースを製造
した。その結果は表−1に示す通りで、得られた
製品の1%水溶液の性状は比較例で得られたもの
と比較して極めて優れた澄明性を示した。 【表】
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a method for producing water-soluble hydroxyethyl cellulose, and more specifically, the present invention relates to a method for producing water-soluble hydroxyethyl cellulose, and more specifically, in a slurry state of a cellulose raw material in a medium consisting of an organic solvent and water, an alkali is applied to produce alkali cellulose. At the same time, a surfactant is added.
The present invention relates to a process for producing hydroxyethyl cellulose which, by subsequent reaction with ethylene oxide in the presence of a surfactant, has significantly improved visibility of an aqueous solution of the product. Generally, the production of hydroxyethylcellulose is
Lower aliphatic alcohols such as isopropyl alcohol (IPA) and tertiary butyl alcohol (TBA),
The process starts by reacting a cellulose raw material with an alkali in a slurry state in a mixed solution of water and an alkali to form alkali cellulose. In the process of producing alkali cellulose, the state of the solution phase is such that the lower aliphatic alcohol and the alkaline aqueous solution are not compatible with each other, so they are reacted with the cellulose raw material while remaining separated into two layers. Uniform permeation of alkali into cellulose does not necessarily proceed smoothly. Furthermore, in the subsequent reaction with ethylene oxide, the reaction proceeds similarly in a heterogeneous system, so conventional techniques have limitations in reducing the turbidity and suspended matter of the aqueous solution, which are important properties of the final product. Although it has excellent properties, it has the disadvantage that it is difficult to obtain. As a result of extensive research into a method for producing hydroxyethylcellulose that has significantly improved solubility characteristics in aqueous solutions of hydroxyethylcellulose, the present inventors discovered that when producing alkali cellulose, a surfactant was added to increase the permeability of alkali into cellulose. It has been found that this objective can be achieved by reacting alkali cellulose with ethylene oxide at a high temperature and subsequently in the presence of a surfactant. The raw material cellulose used in the present invention may be any material commonly used in chemical reactions, such as wood pulp or linter. Further, it is desirable that the raw material cellulose is pulverized by a pulverizer to a size that allows easy stirring of the slurry prior to the reaction. The alkali used may be sodium hydroxide, potassium hydroxide, or lithium hydroxide, but sodium hydroxide is usually used industrially. In carrying out the present invention, the preferred reaction preparation composition and operating conditions are such that the total weight of organic solvents such as isopropyl alcohol (IPA) and butyl alcohol (TBA), which are dispersion media, and water is 5 to 5% relative to the cellulose. In a 15x slurry system, water/
When the weight ratio of cellulose is in the range of 1.5 to 3.0 and the weight ratio of alkali/cellulose is in the range of 0.25 to 0.50, the surfactant is 0.1 to 10% by weight, preferably 0.2 to 1% by weight based on the total weight of the organic solvent and water. % by weight and stirred and mixed for 30 to 200 minutes at a reaction temperature of 10 to 40°C to produce alkali cellulose. Subsequently, 0.8 to 1.2 parts of ethylene oxide may be added to 1 part of cellulose, and the reaction may be carried out at a reaction temperature of 30 to 80°C for 1 to 4 hours. The surfactants used in the present invention include sodium alkylnaphthalene sulfonate, sodium lauryl sulfate, sodium alkylbenzene sulfonate, sodium polyoxyethylene alkyl ether sulfate, sodium polyoxyethylene alkyl phenol ether sulfate, sodium alkylnaphthalene sulfonate, and sodium alkylnaphthalene sulfonate. Examples include, but are not limited to, anionic, nonionic, and cationic surfactants such as oxyethylene alkyl phenol ether and alkyl trimethyl ammonium chloride. The surfactant can be added by adding the surfactant to a mixture of organic solvent and water, stirring and dispersing the cellulose, and then dropping an aqueous alkali solution, or stirring cellulose to the mixture of organic solvent and water in advance. Either a method of dispersing the cellulose and dropping an aqueous alkali solution in which a surfactant is dissolved, or a method of dispersing the cellulose in a mixed solution of an organic solvent, water, a surfactant, and an alkali while stirring can be adopted. The present invention will be explained below with reference to Examples and Comparative Examples. Parts represent parts by weight. Comparative Example 12.8 parts of tertiary butyl alcohol and 2.5 parts of a 12.7% aqueous sodium hydroxide solution were added to a 1 separable flask equipped with a stirrer, mixed, and mixed with linter 1.
of the mixture was added, and the arcelification reaction was carried out at 20°C for 60 minutes with stirring. Next, add 0.95 parts of ethylene oxide to 10
After mixing for 3 minutes, the hydroxyethylation reaction was carried out at 50 to 75°C for 3 hours. After neutralizing the reaction product with acetic acid, the reaction product was filtered, washed twice with a methanol/acetone mixture, and then separated and dried. The viscosity of the obtained 1% aqueous solution of hydroxyethylcellulose is
3600cps, transparency measured by JIS method (K0102)
It was 140mm. Example 1 13.6 parts of tertiary butanol (94.6% by weight, balance water) and 0.045 parts of sodium polyoxyethylene lauryl ether sulfate (number of moles of oxyethylene n = 20) were added to a flask equipped with a stirring device, and pulverized in advance. 1 part of linter was added and mixed well. Add to this 18.3% sodium hydroxide aqueous solution
1.75 parts were added dropwise over about 10 minutes. The amount of surfactant added to the total amount of solvent and water is 0.3% by weight.
Stirring was continued for 60 minutes to form an alkali cellulose, and then 0.95 parts of ethylene oxide was reacted at 50 to 75° C. for 3 hours, followed by post-treatment according to the method of the comparative example. 1% of the resulting hydroxyethyl cellulose
The viscosity of the aqueous solution was 3300 cps, and the transparency measured by JIS method was 440 mm, which was significantly improved compared to that obtained in the comparative example. Example 2 Hydroxyethyl cellulose was produced in the same manner as in Example 1, except that 0.045 parts of sodium polyoxyethylene lauryl ether sulfate (oxyethylene mole number n=50) was used as a surfactant. The viscosity of the obtained 1% aqueous solution of hydroxyethylcellulose was 3560 cps, and the transparency was 520 cps.
mm, and was significantly clearer than that obtained in the comparative example. Example 3 1 part of pulverized linter is added to 13.6 parts of tertiary butyl alcohol (94.6% by weight, balance water) and stirred well. To this, 1.74 parts of an 18.6% sodium hydroxide aqueous solution containing 0.015 parts of sodium polyoxyethylene octyl phenol ether sulfate was added dropwise over 60 minutes to obtain alkali cellulose, and then 0.98 parts of ethylene oxide was added and the reaction was carried out at 50 to 75°C for 3 hours. It was then post-treated by the method of Comparative Example. The amount of surfactant added to the solvent and water is 0.1% by weight.
The viscosity of the 1% aqueous solution of the obtained product is 3900 cps,
The visibility according to JIS method was 400mm. Hydroxyethyl cellulose with significantly improved transparency compared to the comparative example was obtained. Examples 4 to 11 Hydroxyethyl cellulose was produced in the same manner as in Example 1 except that the various surfactants shown in Table 1 were used as surfactants. The results are shown in Table 1, and the properties of the 1% aqueous solution of the obtained product showed extremely excellent clarity compared to that obtained in the comparative example. 【table】

Claims (1)

【特許請求の範囲】[Claims] 1 セルロース原料を有機溶剤と水からなる媒体
中スラリー状態にてアルカリを作用させてアルカ
リセルロースを生成させ、引続き該アルカリセル
ロースに酸化エチレンを反応させることよりなる
ヒドロキシエチルセルロースの製造法において、
アルカリセルロース生成反応およびヒドロキシエ
チル化反応を界面活性剤の存在下に行うことを特
徴とするヒドロキシエチルセルロースの製造法。
1. A method for producing hydroxyethyl cellulose, which comprises reacting a cellulose raw material with an alkali in a slurry state in a medium consisting of an organic solvent and water to produce alkali cellulose, and subsequently reacting the alkali cellulose with ethylene oxide,
1. A method for producing hydroxyethyl cellulose, which comprises carrying out an alkali cellulose production reaction and a hydroxyethylation reaction in the presence of a surfactant.
JP18573682A 1982-10-22 1982-10-22 Production of hydroxyethylcellulose Granted JPS5975902A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP18573682A JPS5975902A (en) 1982-10-22 1982-10-22 Production of hydroxyethylcellulose

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP18573682A JPS5975902A (en) 1982-10-22 1982-10-22 Production of hydroxyethylcellulose

Publications (2)

Publication Number Publication Date
JPS5975902A JPS5975902A (en) 1984-04-28
JPH0138403B2 true JPH0138403B2 (en) 1989-08-14

Family

ID=16175956

Family Applications (1)

Application Number Title Priority Date Filing Date
JP18573682A Granted JPS5975902A (en) 1982-10-22 1982-10-22 Production of hydroxyethylcellulose

Country Status (1)

Country Link
JP (1) JPS5975902A (en)

Families Citing this family (10)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP3009331B2 (en) * 1994-08-22 2000-02-14 富士電気化学株式会社 Broadband dielectric filter
DE10018155A1 (en) * 2000-04-12 2001-10-25 Clariant Gmbh Process for the preparation of readily wettable, water-soluble, powdery, at least alkylated, non-ionic cellulose ethers
JP4029272B2 (en) * 2002-03-11 2008-01-09 信越化学工業株式会社 Admixture and hydraulic composition for extrusion molding using the same
JP5586575B2 (en) * 2009-02-20 2014-09-10 住友精化株式会社 Method for producing hydroxyalkyl cellulose
CN102911272A (en) * 2012-11-15 2013-02-06 泰安赛露纤维素醚科技有限公司 Process for producing hydroxyethyl cellulose with high degree of substitution by binary complex solvent
JP6600777B2 (en) * 2015-04-23 2019-11-06 サンノプコ株式会社 Dissolving pulp composition and method for producing viscose rayon
JP6417502B2 (en) * 2015-04-23 2018-11-07 サンノプコ株式会社 Mercerization accelerator and method for producing viscose rayon
JP7030705B2 (en) 2016-09-29 2022-03-07 住友精化株式会社 Method for producing water-soluble hydroxyethyl cellulose
JP6866190B2 (en) * 2017-03-07 2021-04-28 花王株式会社 Composition containing etherified cellulose fiber and surfactant
US20220213229A1 (en) * 2019-05-29 2022-07-07 Kao Corporation Method for producing modified cellulose

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