JPH0195101A - Manufacture of high-purity acid-type cellulose derivative - Google Patents

Manufacture of high-purity acid-type cellulose derivative

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Publication number
JPH0195101A
JPH0195101A JP25106587A JP25106587A JPH0195101A JP H0195101 A JPH0195101 A JP H0195101A JP 25106587 A JP25106587 A JP 25106587A JP 25106587 A JP25106587 A JP 25106587A JP H0195101 A JPH0195101 A JP H0195101A
Authority
JP
Japan
Prior art keywords
cellulose derivative
acid
solvent
water
type
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
JP25106587A
Other languages
Japanese (ja)
Inventor
Minoru Suzuki
實 鈴木
Fuminobu Takahashi
高橋 文伸
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.)
DKS Co Ltd
Original Assignee
Dai Ichi Kogyo Seiyaku 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 Dai Ichi Kogyo Seiyaku Co Ltd filed Critical Dai Ichi Kogyo Seiyaku Co Ltd
Priority to JP25106587A priority Critical patent/JPH0195101A/en
Publication of JPH0195101A publication Critical patent/JPH0195101A/en
Pending legal-status Critical Current

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Abstract

PURPOSE:To produce a high-purity acid-type cellulose derivative, by arranging a solution of an anionic cellulose derivative in a solvent on the cathode side of the electrodes and an ion-exchange membrane or an ultrafiltration membrane as diaphragm thereby converting the cellulose into an acid-type. CONSTITUTION:An anionic cellulose derivative is dispersed into a solvent thereby allowing it to swell or dissolve. Thereafter it is arranged on the cathode side or, preferably, on both sides of the electrodes, and an ion-exchange membrane or an ultrafiltration membrane is arranged as diaphragm, thereby producing the aimed cellulose derivative of an acid-type. As the applicable anionic cellulose derivative, carboxymethylcellulose, sulfoethylcellulose, carboxymethylhydroxyethylcellulose, or the like can be mentioned. As the solvent, water or a mixed solvent of water and an organic solvent, or the like can be mentioned. As the organic solvent which is used together with water, 3C or lower alcohols, lower ketones, etc., can be mentioned.

Description

【発明の詳細な説明】 (産業上の利用分!?) 未発す1は、高純度酸型セルロース誘導体の製造方υ、
にlff1するものである。
[Detailed description of the invention] (Industrial use!?) Unreleased 1 is a method for producing a high-purity acid-type cellulose derivative υ,
lff1.

(従来の技術) アニオン性のセルロース誘導体の酸型は、それ自身を出
発原料として耳々の金属11!型に変換することによっ
て利用される場合が多く、特に最近ではファインケミカ
ルの分野である医薬、香粧、セラミックス等への利用分
野がIU+待されるに当たり品質上純度の高さが要求さ
れる。
(Prior Art) The acid form of anionic cellulose derivative uses itself as a starting material to produce 11 metals! In many cases, it is used by converting it into a mold, and in particular, recently, IU+ is expected to be used in the fields of fine chemicals such as medicine, cosmetics, and ceramics, so high purity is required for quality.

実際の応用例を挙げると、アニオン性のセルロース誘導
体、例えばカルボキシメチルセルロース(以下CMCと
いう)の酸型またはカルシウム1!4の場合は、医薬錠
剤の崩壊剤または漂白剤、リチウムIS! 8よびカリ
ウム11!は電池組成物、アンモニウム11!はセラミ
ックス/<イングー、石膏粘土、蛍光体膜、大々分散剤
、増粘剤または保護コロイド剤等への用途があり、他の
セルロース誘導体についても各a J71 mへのII
JI待が大きい。
Examples of practical applications include anionic cellulose derivatives, such as the acid form of carboxymethylcellulose (hereinafter referred to as CMC) or calcium 1!4, as a disintegrating agent or bleaching agent for pharmaceutical tablets, and lithium IS! 8 and potassium 11! is a battery composition, ammonium 11! It has applications in ceramics/ingu, gypsum clay, phosphor films, large-scale dispersants, thickeners, protective colloids, etc., and also for other cellulose derivatives, II to each a J71 m.
JI wait is big.

(発明が解決しようとする問題点) 従来からの7ニオン性セルロ一ス話導体の酸型は、通常
アニオン性セルロース誘導体の金属塩型からの合成によ
る場合が多く、しかも殆どナトリウム塩型である。
(Problems to be Solved by the Invention) The acid type of conventional 7-ionic cellulose conductors is usually synthesized from the metal salt type of anionic cellulose derivative, and most of them are sodium salt type. .

従って、これを酸をとする場合は硫酸、!!!酸等の鉱
酸またはカルボンm笠の有機醸を用いて酸型にする方法
か−・殻に知られているが、残Fli酸の洗浄除去のた
め多量の1&薄酸廃液が派生し、その中和処理、4x水
処理に、多くの手数を必要とする等、設備の腐食性、公
害性および経済性の問題を抱えている。
Therefore, when referring to this as an acid, it is sulfuric acid! ! ! Is it possible to convert it into an acid form using a mineral acid such as an acid or an organic brew of carbon dioxide? This method is known for shells, but a large amount of 1 & dilute acid waste liquid is derived to wash and remove the remaining Fri acid. It requires a lot of work for neutralization treatment and 4x water treatment, and has problems with equipment corrosivity, pollution, and economic efficiency.

またセルロース誘導体におけるエーテル基の置換度が高
くなると酸をでも水溶性となる場合が多く1例えばCM
Cの場合、そのDSが2以上になると水溶性となり、特
公昭80−17445号公報に提案されている方法では
、かかる酸型のCMCが水溶液状であるため、99%ア
セトン等の有機溶媒で沈ドさせてIJ&m状として取出
す方法が記載されているが、そのために発生した含水有
機溶媒の精留等が不可欠で、経済的に極めて不利な要因
が存在する。さらに同公報の酸を使用する方法の欠点と
しては、セルロース鎖の解重合を必然的に引き起こし、
特に錫酸類を使用した場合エステル化物の生成もある等
、物性上においても好ましくない影響を与えることが挙
げられる。
In addition, when the degree of substitution of ether groups in cellulose derivatives increases, they often become water-soluble even with acids1, for example, CM
In the case of C, when its DS becomes 2 or more, it becomes water-soluble, and in the method proposed in Japanese Patent Publication No. 80-17445, since the acid type CMC is in the form of an aqueous solution, it can be dissolved in an organic solvent such as 99% acetone. A method is described in which it is precipitated and taken out as IJ&M, but this requires rectification of the water-containing organic solvent generated, which is an extremely disadvantageous factor economically. Furthermore, as a disadvantage of the method using acids described in the same publication, it inevitably causes depolymerization of cellulose chains;
In particular, when stannic acids are used, esterification products may be produced, which may have unfavorable effects on physical properties.

(問題点を解決するための手段) 未発151は高純度酸型セルロース誘導体を電気透析で
製造するに際し、 アニオン性のセルロース誘導体を、溶媒に分散。
(Means for solving the problem) When producing high-purity acid-type cellulose derivatives by electrodialysis, Unreleased 151 disperses anionic cellulose derivatives in a solvent.

膨潤または溶解させた後、電極のカソード、好ましくは
両電極に、隔膜としてイオン交換膜または限外口過膜を
配し、酸型とすることを特徴とする高純度酸型セルロー
ス誘導体の製造方法である。
A method for producing a high-purity acid-type cellulose derivative, which is characterized in that after swelling or dissolving, an ion exchange membrane or an ultrafiltration membrane is arranged as a diaphragm on the cathode of the electrode, preferably both electrodes, and the cellulose derivative is converted into an acid form. It is.

未発1!IIに使用するアニオン性のセルロース誘導体
とは、CMC、スルホエチルセルロース(SEC)、カ
ルボキシメチルスルホエチルセルロース(CMSEC)
、カルボキシメチルヒドロキシエチルセルロース(CM
HEC)等である。
1 unreleased! The anionic cellulose derivatives used in II include CMC, sulfoethylcellulose (SEC), and carboxymethylsulfoethylcellulose (CMSEC).
, carboxymethylhydroxyethylcellulose (CM
HEC) etc.

これらのセルロース誘導体は、公知の方法1例えIf 
CM Cの場合バルブ等のセルロース原ネ1をNaOH
等でマーセル化し、クロロ酢酸等によってエーテル化し
て得られるものである。
These cellulose derivatives can be prepared using known methods such as If
In the case of CM C, cellulose raw material 1 for valves etc. is diluted with NaOH.
It is obtained by mercerizing with chloroacetic acid or the like and etherifying with chloroacetic acid or the like.

池の物質についても、同様に公知の方法によって得るこ
とができる。
Pond substances can be similarly obtained by known methods.

本発明に使用する溶媒とは水、または水と有機溶媒の混
合溶媒等である。
The solvent used in the present invention is water or a mixed solvent of water and an organic solvent.

水と併用する有機溶媒としては炭素数3以下の低級アル
コール類(例えばメタノール、エタノール、2−プロパ
ツール等)、低級ケトンgA(例えばアセトン等)等が
挙げられる。また、その混合比率は重量で水/有機溶媒
=10〜119790〜lである。
Examples of organic solvents to be used in combination with water include lower alcohols having 3 or less carbon atoms (for example, methanol, ethanol, 2-propatol, etc.), lower ketones gA (for example, acetone, etc.). Moreover, the mixing ratio is water/organic solvent=10 to 119,790 to 1 by weight.

本発明にかかる高純度酸型セルロース誘導体の製造方法
とは1重犯アニオン性のセルロース誘導体を、前記溶媒
に分散、膨潤または溶解させた後電気透析によってS型
とする方法である。
The method for producing a high-purity acid-type cellulose derivative according to the present invention is a method in which a single-acid anionic cellulose derivative is dispersed, swollen, or dissolved in the above-mentioned solvent, and then converted into S-type by electrodialysis.

かかる電気透析とは1通常の電解!jt置を組み、電極
として酸化還元反応が生じない様な材質、好ましくは白
金を用い、カソードまたは好ましくは両電極に、隔膜を
配し、電解槽中へ、前記アニオン性のセルロース誘導体
を試料溶液として調製したものを入れ、金属イオンを取
出し、7ノードまたはアノード隔膜に目的物とするゲル
状または固形状の生成物をf!するものである。好まし
くは両電極に隔膜を配するとは、アノードにゲルが生成
する際にゲル中に若干含まれる低分子の陰イオン成分を
7ノード隔膜中に取込み、より高純度のセルロースゲル
を7ノ一ド隔膜表面に生成させる目的によるものである
What is this electrodialysis? 1. Ordinary electrolysis! The electrodes are made of a material that does not cause redox reactions, preferably platinum, and a diaphragm is placed on the cathode or preferably on both electrodes, and the anionic cellulose derivative is introduced into the electrolytic cell as a sample solution. The metal ions are removed, and the desired gel or solid product is placed in the 7-node or anode diaphragm. It is something to do. Preferably, placing a diaphragm on both electrodes means that when a gel is formed on the anode, a small amount of low-molecular anion components contained in the gel are incorporated into the 7-node diaphragm, and a higher purity cellulose gel is added to the 7-node diaphragm. This is due to the purpose of producing it on the surface of the diaphragm.

また隔膜としてはイオン交換膜、限外口過膜等が挙げら
れる。
Examples of the diaphragm include ion exchange membranes and ultrafiltration membranes.

(発11の効果) 未発IJIJの製造方法に従ってmられる酸型セルロー
ス誘導体は。
(Effects of Development 11) The acid type cellulose derivative prepared according to the method for producing undeveloped IJIJ is as follows.

(1)金属イオンの含有率が0.1z以下で殆ど完全に
近い酸型であり、またご硝等の塩類が殆ど存在しない等
極めて純度が高い、 (2)元の金属fil型に戻した場合の水溶液粘度が、
最初の金属用型の水溶液粘度と比較して殆ど低下せずセ
ルロース鎖の重合度低下を殆ど生じない 等、優れた性質を有する。
(1) It is an almost perfect acid type with a metal ion content of 0.1z or less, and has extremely high purity, with almost no salts such as salts present. (2) When it is returned to its original metal fil type. The viscosity of the aqueous solution is
It has excellent properties, such as the viscosity of an aqueous solution of the first metal type, which hardly decreases and hardly causes a decrease in the degree of polymerization of cellulose chains.

また本発明の製造方法は、従来の酸処理法と比較して低
公害性であり、さらに酸を用いて酸型にする時、水溶性
を示す酸型セルロース誘導体の場合でも、ゲル状または
固形状として高収率で、且つ効率良く分離して取出すこ
とができる。
In addition, the production method of the present invention is less polluting than conventional acid treatment methods, and when converted into acid form using acid, even in the case of water-soluble acid form cellulose derivatives, gel-like or solid The shape can be separated and extracted with high yield and efficiency.

(実施例) 尚、実施例中r%1は重量基準である。(Example) In the examples, r%1 is based on weight.

実施例1゜ 両電極に白金板を使用した電解装置i!I (KIKU
SUIELECTRON[S C0RP、製、 MOD
EL PAB 110−0.8 、以下の実施例も同様
である)を組み、カルボキシメチルセルロースナトリウ
ムJ!1(市販品Na−CMC、0S−0,135,2
5℃ニ第1tル2%水溶液粘度3380−Pass;以
下、同じく粘度値は全て25℃におけるイ〆【である)
が4zとなる様に50%ア七トン水溶液に溶解した糊液
650gを電解槽に入れ両電極にカチオン交換11!2
(旭化X&、製、アシプレックス−F)を配して0.6
5Aの電流を流した。4時間後にゲルとしてII(Og
の収量を得た。
Example 1 Electrolysis device i using platinum plates for both electrodes! I (KIKU
SUIELECTRON [S C0RP, made, MOD
EL PAB 110-0.8 (the same applies to the following examples), and carboxymethylcellulose sodium J! 1 (commercial product Na-CMC, 0S-0,135,2
Viscosity of 1 ton 2% aqueous solution at 5°C: 3380-Pass; Below, all viscosity values are at 25°C.
Put 650g of the paste solution dissolved in 50% aqueous solution of A7Tone into an electrolytic cell so that 4z becomes cation exchange 11!2 to both electrodes.
(Asahi Kax&, manufactured by Aciplex-F) 0.6
A current of 5A was applied. II (Og) as a gel after 4 hours
yield was obtained.

このゲルの無水物重量は22.8gで、残存ナトリウム
は0.022%であった。
The anhydrous weight of this gel was 22.8 g, and the residual sodium was 0.022%.

また、このゲルを5%NaOH水溶液に入れて。Also, put this gel in a 5% NaOH aqueous solution.

Na−CMCの2%水溶液となるように調製した糊液の
粘度を測定した。
The viscosity of a paste prepared as a 2% aqueous solution of Na-CMC was measured.

この時の粘度は3290 mPa* sであった。The viscosity at this time was 3290 mPa*s.

実施例2゜ 両電極に白金板を使用した電解装置を組み、予め31整
した6%N a−CM C(O5−2,18,2x水溶
液粘度1830 mPa e s)の40%2−プロパ
ツール水溶液1667gを、両電極に限外口過膜(東洋
曹達製、UF−300PS、分画分子量30万)を配し
て電気透析を行なった。 10分装にゲル取出しを縁返
し、5時間後にゲルとして672gの収量を得た。この
ゲルの固形分は82.3gで、残存ナトリウムは0.0
45%であった。
Example 2 An electrolytic device using platinum plates for both electrodes was assembled, and 40% 2-propertool of 6% Na-CMC (O5-2,18,2x aqueous solution viscosity 1830 mPa e s) was prepared in advance. 1667 g of the aqueous solution was subjected to electrodialysis using an ultrafiltration membrane (manufactured by Toyo Soda, UF-300PS, molecular weight cut off: 300,000) placed on both electrodes. The gel was taken out in 10 portions and turned over, and 672 g of gel was obtained after 5 hours. The solid content of this gel is 82.3g, and the residual sodium is 0.0
It was 45%.

また、このゲルから2−プロパツールを除去し、5%N
 aOH水溶液にNa−CMCとして2%となるよう調
製した糊液の粘度を測定した。
Additionally, 2-propatool was removed from this gel and 5% N
The viscosity of a paste prepared by adding 2% Na-CMC to an aOH aqueous solution was measured.

この時の粘度は1800 mPa・Sであった。The viscosity at this time was 1800 mPa·S.

実施例3゜ 両電極に白金板を使用した電解装置を組み、4%N a
−CM C(DS讃1.40. 2z水溶液粘度550
0 mPa *S)の55%メタノール水溶液3000
gを、カソードにカチオン交換膜(旭化成製、アシプレ
、クスーF)を配して電気透析を行なった。
Example 3 An electrolysis device using platinum plates for both electrodes was assembled, and 4% Na
-CM C (DS San 1.40. 2z aqueous solution viscosity 550
0 mPa *S) 55% methanol aqueous solution 3000
g was subjected to electrodialysis using a cation exchange membrane (manufactured by Asahi Kasei Co., Ltd., Acipre, Kusu F) placed at the cathode.

IIIIF間後にゲルとして937.4gの収量を得た
A yield of 937.4 g as gel was obtained after IIIF.

このゲルの揮発分は90.1%で、残存ナトリウムは0
.037%であった。
The volatile content of this gel is 90.1% and the residual sodium is 0.
.. It was 037%.

このゲルからメタノールを除去し、5%N aOH水溶
液にNa−CMCとして2%となるよう調製した糊液の
粘度を測定した。
Methanol was removed from this gel, and the viscosity of a paste solution prepared by adding 2% Na-CMC to a 5% NaOH aqueous solution was measured.

この時の粘度は5370 mPa拳sであった。The viscosity at this time was 5370 mPa.

実施例4゜ 両電極に白金板を使用した電解装置を組み、6%スルホ
エチルセルロースナトリウムfil(Na−3EC; 
DS−0,85,2z水溶液粘度1f170 mPa*
 s)の60%メタノール水溶液4500gを、両電極
に限外口過11’(東洋曹達製、UF−300PS、分
両分子ffi:30万)を配して電気透析を行なった。
Example 4 An electrolytic device using platinum plates for both electrodes was assembled, and 6% sodium sulfoethyl cellulose fil (Na-3EC;
DS-0,85,2z aqueous solution viscosity 1f170 mPa*
4,500 g of a 60% aqueous methanol solution of s) was subjected to electrodialysis using an ultrafiltration filter 11' (manufactured by Toyo Soda, UF-300PS, fractional molecular ffi: 300,000) placed on both electrodes.

2時間後にゲルとして1890gの収量、を得た。この
ゲルの揮発分は88.02で、残存ナトリウムは0.0
11%であった。
A yield of 1890 g as gel was obtained after 2 hours. The volatile content of this gel was 88.02, and the residual sodium was 0.0.
It was 11%.

このゲルからメタノールを除去し、5%N aOH水溶
液にNa−3ECとして2%となるよう調製した糊液の
粘度を測定した。
Methanol was removed from this gel, and the viscosity of a paste solution prepared by adding Na-3EC to a 5% NaOH aqueous solution to give a concentration of 2% was measured.

この時の粘度は1520 mPa* sであった。The viscosity at this time was 1520 mPa*s.

実施例5 両電極に白金板を使用した電解装置を組み、5%カルボ
キシメチルスルホエチルセルロースナトリウム11!(
Na−CMS E C; S E置換度0.58、CM
2!1換度0.53. 2%水溶液粘度2230 +*
Pa ・s )の50り5工タノール水溶液8800g
を、両電極に限外口過11Q(東洋fr lf!製、 
0F−300PS、分画分子Q 30万) ヲ配して電
気透析を行なった。90分後にゲルとして855gの収
7^を得た。このゲルの揮発分は87.7$で、残存ナ
トリウムは0.033%であった。
Example 5 An electrolytic device using platinum plates for both electrodes was assembled, and 5% carboxymethylsulfoethylcellulose sodium 11! (
Na-CMS E C; S E substitution degree 0.58, CM
2!1 conversion degree 0.53. 2% aqueous solution viscosity 2230 +*
8,800 g of 50% 50% tanol aqueous solution of
, both electrodes are equipped with an ultraviolet filter 11Q (manufactured by Toyo fr lf!,
0F-300PS, fractionated molecule Q 300,000) was used for electrodialysis. After 90 minutes, 855 g of 7^ was obtained as a gel. The volatile content of this gel was 87.7$ and the residual sodium was 0.033%.

このゲルからエタノールを除去し、5%N a Oi(
水溶液にNa−CMSECとして2%となるよう調製し
た糊液の粘度を測定した。
Ethanol was removed from this gel and 5% NaOi (
The viscosity of a paste solution prepared to have a concentration of 2% Na-CMSEC in an aqueous solution was measured.

この時の粘度は2140 mPa* sであった。The viscosity at this time was 2140 mPa*s.

比較例1゜ N a−CM C(DSJ、85.2z水溶液粘度33
80 mPa * s)28.0gに17χH2S 0
4520g加え、50℃5時間酸型化した。過剰の酸を
分離した後、水1000gを加え脱酸処理を行ない、こ
の操作をさらに3回繰り返した。この廃酸液的3000
.をNaOHで中和した。
Comparative example 1゜N a-CM C (DSJ, 85.2z aqueous solution viscosity 33
80 mPa * s) 17χH2S 0 at 28.0g
4,520g was added and acidified at 50°C for 5 hours. After separating excess acid, 1000 g of water was added to perform deacidification treatment, and this operation was repeated three more times. This waste acid liquid 3000
.. was neutralized with NaOH.

この方法によって得られた酸型CMCの生成量は+7.
[1gであり、残存ナトリウムは0.197L残存硫酸
イオンは0.82 %であった。
The amount of acid type CMC obtained by this method was +7.
[1g, residual sodium was 0.197L, residual sulfate ion was 0.82%.

また、Na−CMCとして2%になるよう、酸yliC
MCを5%NaOH水溶液に溶解Φ調製した糊液の粘度
を測定した。
In addition, acid yliC was added so that the concentration of Na-CMC was 2%.
The viscosity of a paste prepared by dissolving MC in a 5% NaOH aqueous solution was measured.

この時の粘度は2200 sPaφSであった。The viscosity at this time was 2200 sPaφS.

比較例2゜ N a−CM C(OS−2,18,22水溶液粘度1
830 mPa *s)100gに18 ZH2S O
45000g加えた。徐々にCMCが溶解を始め、2時
間で完全に溶解し、さらに50℃で3時間酸型化した。
Comparative Example 2゜N a-CM C (OS-2, 18, 22 aqueous solution viscosity 1
830 mPa *s) 18 ZH2SO in 100g
Added 45,000g. CMC gradually began to dissolve, was completely dissolved in 2 hours, and was further acidified at 50° C. for 3 hours.

次にHXアセトン20000gを加え、沈澱させた。沈
殿物を分離し、さらに95zアセトン水溶液3000c
cで5回洗浄した。この方法によって得られた酸型CM
Cの生成量は55.7gであり、残存ナトリウムは0.
25 X、残存硫酸イオンは0.81 !であった。
Next, 20,000 g of HX acetone was added to cause precipitation. Separate the precipitate and further add 95z acetone aqueous solution 3000c
Washed 5 times with c. Acid type CM obtained by this method
The amount of C produced was 55.7g, and the residual sodium was 0.
25X, residual sulfate ion is 0.81! Met.

またNa−CMCとして2%になるよう、酸型CMCを
5%NaOH水溶液に溶解争調製した糊液の粘度を測定
した。
In addition, the viscosity of a paste prepared by dissolving acid CMC in a 5% NaOH aqueous solution so that the concentration of Na-CMC was 2% was measured.

この時の粘度は450 mPa* sであった。The viscosity at this time was 450 mPa*s.

これらの実施例および比較例の結果を、第1表に、まと
めて記載する。
The results of these Examples and Comparative Examples are summarized in Table 1.

Claims (3)

【特許請求の範囲】[Claims] (1)高純度酸型セルロース誘導体を電気透析で製造す
るに際し、 アニオン性のセルロース誘導体を、溶媒に分散、膨潤ま
たは溶解させた後、電極のカソード、好ましくは両電極
に、隔膜としてイオン交換膜または限外ロ過膜を配し、
酸型とすることを特徴とする高純度酸型セルロース誘導
体の製造方法。
(1) When producing a high-purity acid cellulose derivative by electrodialysis, an anionic cellulose derivative is dispersed, swollen, or dissolved in a solvent, and then an ion exchange membrane is applied as a diaphragm to the cathode of the electrode, preferably both electrodes. Or with an ultrafiltration membrane,
A method for producing a high-purity acid type cellulose derivative, characterized in that it is in an acid type.
(2)溶媒が水、または水と有機溶媒の混合溶媒である
特許請求の範囲第(1)項記載の方法。
(2) The method according to claim (1), wherein the solvent is water or a mixed solvent of water and an organic solvent.
(3)有機溶媒が、炭素数3以下の低級アルコール類お
よびケトン類からなる群より選らばれた少なくとも1種
である特許請求の範囲第(2)項記載の方法。
(3) The method according to claim (2), wherein the organic solvent is at least one selected from the group consisting of lower alcohols having 3 or less carbon atoms and ketones.
JP25106587A 1987-10-05 1987-10-05 Manufacture of high-purity acid-type cellulose derivative Pending JPH0195101A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP25106587A JPH0195101A (en) 1987-10-05 1987-10-05 Manufacture of high-purity acid-type cellulose derivative

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP25106587A JPH0195101A (en) 1987-10-05 1987-10-05 Manufacture of high-purity acid-type cellulose derivative

Publications (1)

Publication Number Publication Date
JPH0195101A true JPH0195101A (en) 1989-04-13

Family

ID=17217106

Family Applications (1)

Application Number Title Priority Date Filing Date
JP25106587A Pending JPH0195101A (en) 1987-10-05 1987-10-05 Manufacture of high-purity acid-type cellulose derivative

Country Status (1)

Country Link
JP (1) JPH0195101A (en)

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2000008059A1 (en) * 1998-08-04 2000-02-17 Union Carbide Chemicals & Plastics Technology Corporation Production of polysaccharide ethers
JP2003088394A (en) * 2001-09-19 2003-03-25 Ehime Prefecture Method for producing organic hydrolyzate and method for producing the same
US6933381B2 (en) 2001-02-02 2005-08-23 Charles B. Mallon Method of preparing modified cellulose ether
WO2022145318A1 (en) * 2020-12-28 2022-07-07 パナソニックIpマネジメント株式会社 Alkali metal ion-conductive solid electrolyte, method for producing same, separator for nonaqueous electrolyte secondary batteries, method for producing said separator for nonaqueous electrolyte secondary batteries, and nonaqueous electrolyte secondary battery

Cited By (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2000008059A1 (en) * 1998-08-04 2000-02-17 Union Carbide Chemicals & Plastics Technology Corporation Production of polysaccharide ethers
US6933381B2 (en) 2001-02-02 2005-08-23 Charles B. Mallon Method of preparing modified cellulose ether
JP2003088394A (en) * 2001-09-19 2003-03-25 Ehime Prefecture Method for producing organic hydrolyzate and method for producing the same
WO2022145318A1 (en) * 2020-12-28 2022-07-07 パナソニックIpマネジメント株式会社 Alkali metal ion-conductive solid electrolyte, method for producing same, separator for nonaqueous electrolyte secondary batteries, method for producing said separator for nonaqueous electrolyte secondary batteries, and nonaqueous electrolyte secondary battery
JPWO2022145318A1 (en) * 2020-12-28 2022-07-07
CN116711089A (en) * 2020-12-28 2023-09-05 松下知识产权经营株式会社 Alkali metal ion-conductive solid electrolyte and method for producing same, separator for nonaqueous electrolyte secondary battery and method for producing same, and nonaqueous electrolyte secondary battery
CN116711089B (en) * 2020-12-28 2025-11-11 松下知识产权经营株式会社 Alkali metal ion-conductive solid electrolyte and method for producing same, separator for nonaqueous electrolyte secondary battery and method for producing same, and nonaqueous electrolyte secondary battery

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