Deprecated: The each() function is deprecated. This message will be suppressed on further calls in /home/zhenxiangba/zhenxiangba.com/public_html/phproxy-improved-master/index.php on line 456
JPS6036201B2 - Process for producing carboxymethylcellulose sodium salt - Google Patents
[go: Go Back, main page]

JPS6036201B2 - Process for producing carboxymethylcellulose sodium salt - Google Patents

Process for producing carboxymethylcellulose sodium salt

Info

Publication number
JPS6036201B2
JPS6036201B2 JP56204578A JP20457881A JPS6036201B2 JP S6036201 B2 JPS6036201 B2 JP S6036201B2 JP 56204578 A JP56204578 A JP 56204578A JP 20457881 A JP20457881 A JP 20457881A JP S6036201 B2 JPS6036201 B2 JP S6036201B2
Authority
JP
Japan
Prior art keywords
cmc
water
carboxylic acid
sodium salt
carboxymethylcellulose sodium
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
JP56204578A
Other languages
Japanese (ja)
Other versions
JPS58104901A (en
Inventor
哲夫 兼松
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 JP56204578A priority Critical patent/JPS6036201B2/en
Publication of JPS58104901A publication Critical patent/JPS58104901A/en
Publication of JPS6036201B2 publication Critical patent/JPS6036201B2/en
Expired legal-status Critical Current

Links

Landscapes

  • Polysaccharides And Polysaccharide Derivatives (AREA)

Description

【発明の詳細な説明】 本発明は水分散性に優れたカルボキシメチルセルロース
・ナトリウム塩の製製法に関する。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a method for producing carboxymethyl cellulose sodium salt having excellent water dispersibility.

詳しくはカルボキシメチルセルロース・ナトリウム塩を
高温で加熱架橋処理することによる水分散性に優れたカ
ルボキシメチルセルロース・ナトリウム塩の製造方法に
関するものである。一般に、カルボキシメチルセルロー
ス・ナトリウム塩(以下Na−CMCと略称)は、水に
対する分散性を悪く、いわゆるママコになりやすいため
、水落解時には十分櫨拝しながら少量ずつ添加しなけれ
ばならず、更に完全熔解までには長時間を必要とすると
いう欠点がある。このため、ママコ現象を防止する方法
としてNa−CMCを頚粒状にする方法もあるが、部分
的にはママコにあり、必ずしも十分ではない。
Specifically, the present invention relates to a method for producing carboxymethylcellulose sodium salt having excellent water dispersibility by thermally crosslinking carboxymethylcellulose sodium salt at high temperature. In general, carboxymethyl cellulose sodium salt (hereinafter abbreviated as Na-CMC) has poor dispersibility in water and tends to form so-called "mamako", so it must be added little by little while thoroughly stirring when dissolved in water, and it is necessary to completely It has the disadvantage that it takes a long time to melt. For this reason, there is a method of making Na-CMC into neck grains as a method of preventing the mamako phenomenon, but this is partially due to the mamako phenomenon and is not necessarily sufficient.

また、グリオキザールなどで処理する方法も知られてい
るが、処理及びpH調整に手間がか)り、第三成分添加
のための純度の点で用途的に制約を受けることにもなる
。本発明者らは、上述のような第三成分を全く添加する
ことのないNa−CMCの製法を鋭意検討した結果、水
分散性が極めて優れたNa−CMCの製法を発見し、完
成したものである。
Furthermore, a method of treating with glyoxal or the like is known, but it requires time and effort for treatment and pH adjustment, and is also subject to restrictions in terms of purity for addition of a third component. As a result of intensive research into a method for producing Na-CMC without adding any third component as described above, the present inventors discovered and completed a method for producing Na-CMC with extremely excellent water dispersibility. It is.

Na−CMCが水落解時にママコになる理由は、Na−
CMCの水に対する親和力及び溶解力が非常に高いため
、水に接触したNa−CMC粒子の表面が即時溶解する
と同時に水分子を結合保持するため、Na−CMC粒子
内部への水の浸透拡散を妨げることにある。
The reason why Na-CMC turns into a lump when it dissolves in water is because Na-
Because CMC has a very high affinity and dissolving power for water, the surface of Na-CMC particles that come into contact with water immediately dissolves and at the same time binds and retains water molecules, which prevents water from penetrating and diffusing inside the Na-CMC particles. There is a particular thing.

そこで、本発明は加熱処理によりNa−CMC分子鎖内
に、部分的に水不溶性のェステル架橋結合を導入するこ
とによって、Na−CMC粒子内部への水の浸透を促進
することにより、ママコを防止しようと考えたものであ
る。
Therefore, the present invention prevents mako by promoting the penetration of water into the inside of Na-CMC particles by partially introducing water-insoluble ester crosslinks into the Na-CMC molecular chains through heat treatment. That's what I was thinking of doing.

本発明は、Na−CMC中に少量存在させた遊離カルボ
ン酸基(Cell−○−CH2COOH)を高温で加熱
することにより、Na−CMC分子鎖の未置換の水酸基
(Cell−OH)と架橋反応(ェステル結合Cell
−○−CH2COO−Cell)を行なわしめることを
活用したことにある。
The present invention involves a crosslinking reaction with an unsubstituted hydroxyl group (Cell-OH) of the Na-CMC molecular chain by heating a small amount of free carboxylic acid group (Cell-○-CH2COOH) in Na-CMC at high temperature. (Ester bond Cell
-○-CH2COO-Cell).

本発明の出発原料であるNa−CMCは水媒法又は溶媒
法のいずれのものも使用できる。
Na-CMC, which is the starting material of the present invention, can be produced using either an aqueous method or a solvent method.

Na−CMCの置換度(以下DSと略称)については、
0.3以上3未満のものが使用できる。DSO.3未満
のCMCは水に不溶性であり、DS3のCMCは、未置
換の水置換の水酸基がないため、ェステル架橋が不可能
となる。Na−CMCの重合度又は粘度については加熱
処理条件と関連するが、1%水溶液大占度で100セン
チポィズ以上のNa−CMCであることが必要である。
100センチポィズ以下の低粘度Na−CMCでは分子
鎖が短いため、加熱架橋しても加熱防止効果が発現し難
い。
Regarding the degree of substitution (hereinafter abbreviated as DS) of Na-CMC,
Those having a molecular weight of 0.3 or more and less than 3 can be used. DSO. A CMC of less than 3 is insoluble in water, and since the CMC of DS3 has no unsubstituted water-substituted hydroxyl group, ester crosslinking is impossible. The degree of polymerization or viscosity of Na-CMC is related to the heat treatment conditions, but it is necessary that the Na-CMC has a major concentration of 100 centipoise or more in a 1% aqueous solution.
Since Na-CMC with a low viscosity of 100 centipoise or less has a short molecular chain, it is difficult to exhibit a heating prevention effect even if it is thermally crosslinked.

Na−CMCの粘度と加熱条件の目安としは、1%水溶
液粘度が100〜1000センチポィズのものならば1
40oo以上で数時間、1000〜3000センチポイ
ズのものならば14q○付近で1〜2時間、3000セ
ンチポイズ以上のものならば100〜130qoで数1
び分間の加熱処理で目的物を得ることができる。加熱温
度は100〜200qCが適当であり、更に好ましくは
120〜180ooである。100oo以下では一応可
能性があるものの、非常な長時間処理を必要とし、また
200qC以上ではNa−CMCの着色及び分解が激し
くなるので不適当である。
As a guideline for the viscosity and heating conditions of Na-CMC, if the viscosity of a 1% aqueous solution is 100 to 1000 centipoise,
40oo or more for several hours, if it is 1000 to 3000 centipoise, it will take around 14q○ for 1 to 2 hours, if it is 3000 centipoise or more, it will take several hours at 100 to 130qo.
The desired product can be obtained by heat treatment between two steps. The heating temperature is suitably 100 to 200 qC, more preferably 120 to 180 qC. Although it is possible to use less than 100 qC, it requires a very long treatment time, and above 200 qC, the coloring and decomposition of Na-CMC will become severe, so it is not suitable.

加熱処理のみによりヱステル化架橋反応を行なわせるた
め、Na−CMC中には遊離のカルボン酸基(Cell
−OCH2COOH)の存在が必要である。その量は当
量比でカルボン酸Na塩100に対して0.05以上必
要であり、このような遊離カルボン酸基が存在するNa
−CMCは製造時の中和工程に於てpHを7.5以下に
調整するとによって可能である。通常pH7.5〜6.
0の場合、存在する遊離カルボン酸基の量としては、カ
ルボン酸基が多いほどェステル化架橋は起こり易いこと
になる。従って0.05以下では加熱しても架橋結合点
が少なすぎてママコ防止は期待できない。遊離カルボン
酸基の定量はカルボン酸Na塩と同様、酸・アルカリ滴
定法によって測定した。また逆に、遊離カルボン酸基の
量が当量比でカルボン酸Na塩100に対し20を越え
ると、加熱紫後のCMCの水への分散性は良好であるが
、水落i性が低下するため好ましくない。従って望まし
い遊離カルボン酸基とカルボン酸Na塩の当量比は0.
05〜2政す100である。以上の如く、DSが0.3
以上3未満であり、遊離カルボン酸基とカルボン酸Na
塩の当量比が0.05〜2の村100で、且つ1%水溶
液粘度が100センチポィズ以上であるNa−CMCを
100〜200こ0で数十分から数時間以内加熱処理す
ることにより水分散性の著しく優れたNa−CMCが得
られることを見出し本発明に至ったものである。なお、
本発明の処理によるNa−CMCを水に没入すると、迅
速に水面上を拡散するすると同時に迅速に水中に沈降し
ていく。
In order to carry out the esterification crosslinking reaction only by heat treatment, free carboxylic acid groups (Cell
-OCH2COOH) is required. The amount is required to be at least 0.05 per 100 of the sodium carboxylic acid salt in terms of equivalent ratio.
-CMC is possible by adjusting the pH to 7.5 or less in the neutralization step during production. Usually pH 7.5-6.
In the case of 0, as for the amount of free carboxylic acid groups present, the more carboxylic acid groups there are, the more likely esterification crosslinking will occur. Therefore, if it is less than 0.05, there will be too few cross-linking points even when heated, and prevention of macaques cannot be expected. The quantitative determination of free carboxylic acid groups was carried out by the acid-alkali titration method, as in the case of carboxylic acid Na salt. Conversely, if the amount of free carboxylic acid groups exceeds 20 to 100 of the sodium carboxylic acid salt in equivalent ratio, the dispersibility of CMC in water after heating is good, but the water dropability decreases. Undesirable. Therefore, the desirable equivalent ratio of free carboxylic acid group to carboxylic acid Na salt is 0.
05-2 administration is 100. As mentioned above, DS is 0.3
or more, less than 3, free carboxylic acid group and carboxylic acid Na
Na-CMC with a salt equivalent ratio of 0.05 to 2 and a 1% aqueous solution viscosity of 100 centipoise or more is water-dispersed by heating at 100 to 200 centipoise within several tens of minutes to several hours. The inventors discovered that Na-CMC with significantly superior properties could be obtained, leading to the present invention. In addition,
When Na-CMC treated according to the present invention is immersed in water, it quickly diffuses on the water surface and at the same time quickly settles into the water.

この水溶液は加熱処理前のNa−CMCを溶解した場合
に比べ、見かけの粘度が低下し、不溶解分が増加する場
合には、アルカリ性物質の添加によって容易に増粘し、
且つ不熔解分を完結させることが可能である。
This aqueous solution has a lower apparent viscosity than when Na-CMC is dissolved before heat treatment, and if the undissolved content increases, the viscosity can be easily increased by adding an alkaline substance,
Moreover, it is possible to complete the non-melting decomposition.

例えば、本発明の処理によるNa−CMCを炭酸ナトリ
ウムなどの弱アルカリ性水溶液に投入すればママコにな
らずに分散し、且つ完全に溶解する。更に具体的には、
置換度0.7、粘度150比ps、遊離カルボン酸基0
.09(対カルボン酸Na塩100)のNa−CMCを
140℃で2hr加熱処理したもの2夕を炭酸ナトリウ
ムでpHを10及び11に調整した水溶液各200のと
に投入した。その結果、共にママコにならず、迅速に分
散し、且つサンプル粒子は完全に溶解して1%水溶液粘
度で100比psの高粘度溶液が得られた。なお、本発
明のNa−CMCは石油ボ−リング、繊維壁、食品、飼
料、鉄剤崩壊剤、糊料、泥水調整剤などに使われる。
For example, when Na-CMC treated according to the present invention is put into a weakly alkaline aqueous solution such as sodium carbonate, it will be dispersed and completely dissolved without becoming lumpy. More specifically,
Degree of substitution 0.7, viscosity 150 ps, free carboxylic acid group 0
.. Two nights of Na-CMC of No. 09 (versus 100% of sodium carboxylic acid salt) heat-treated at 140° C. for 2 hours were added to 200% of each aqueous solution whose pH was adjusted to 10 and 11 with sodium carbonate. As a result, a high viscosity solution with a 1% aqueous solution viscosity of 100 ps was obtained, in which the sample particles did not become lumpy, were dispersed quickly, and the sample particles were completely dissolved. The Na-CMC of the present invention can be used in petroleum borings, fiber walls, foods, feeds, iron disintegrators, glues, muddy water conditioners, and the like.

水に対する分散性の評価方法は特に定まったものがない
ので、便宜的に次の方法で測定した。即ち300の‘の
ビーカーに200地の水を入れ、水面上30物高さの中
央部分にロートを固定し、このロートに0.5夕のサン
プルを山気に投入して終始静暦状態下でサンプルの拡散
l大況及び沈降状況を観察すると共に、0.5夕のサン
プルが全て水中に分散する時間を測定して、この時岡を
水に対する分散性(ママコ防止効果)の代表値とした。
以下実施例にて説明する。
Since there is no established method for evaluating dispersibility in water, the following method was used for convenience. That is, put 200 ml of water in a 300 ml beaker, fix a funnel in the center at a height of 30 ml above the water surface, and put a 0.5 ml sample into the funnel and keep it under static conditions from beginning to end. In addition to observing the dispersion and settling conditions of the sample, we also measured the time it took for all the samples to disperse into the water for 0.5 days, and used this time as a representative value for the dispersibility in water (preventing effect). .
This will be explained below using examples.

実施例 1−6 以下の種々のNa−CMCを加熱処理し、純水に対する
分散性を評価した。
Example 1-6 The following various Na-CMCs were heat-treated and their dispersibility in pure water was evaluated.

評価方法は前述の簡便法により、静層状態下でサンプル
全量が水中に分散する時間を測定した。使用した原料N
a−CMCは、水分5〜10%、粒度80メッシュパス
であった。熱処理には、熱風循環式乾燥機を使用した。
結果を第1表に示した。第 1 表 注)*印; 4時間静置後でも殆んど分散せず、ママコ
に友つた。
The evaluation method was to measure the time required for the entire sample to be dispersed in water under static conditions using the above-mentioned simple method. Raw materials used
The a-CMC had a moisture content of 5-10% and a particle size of 80 mesh pass. A hot air circulation dryer was used for heat treatment.
The results are shown in Table 1. Note in Table 1) Marked with *: There was almost no dispersion even after 4 hours of standing, and it was compatible with mamako.

実施例 7〜10置換度および遊離カルボン酸基とカル
ボン酸ナトリウム塩との当量比の異なる4種のCMCを
、*140o01時間加熱処理し、純水に対する分散性
を実施例1と同じ方法で評価した。
Examples 7 to 10 Four types of CMC with different degrees of substitution and equivalent ratios of free carboxylic acid groups and carboxylic acid sodium salts were heat-treated for *140°C for 1 hour, and their dispersibility in pure water was evaluated in the same manner as in Example 1. did.

結果を第2表に示した。The results are shown in Table 2.

第 2 表 注)*印;4時間静置後でも殆と分散せず、ァマコにな
った。
Note in Table 2) *Marked: Even after standing for 4 hours, it was hardly dispersed and became sticky.

Claims (1)

【特許請求の範囲】[Claims] 1 無水グルコース単位当りの置換度が0.3以上3未
満であり、遊離カルボン酸基とカルボン酸ナトリウム塩
との当量比が0.05〜20対100で、且つ1%水溶
液粘度が100センチポイズ以上であるカルボキシメチ
ルセルロース・ナトリウム塩を、100〜200℃で加
熱処理することを特徴とするカルボキシメチルセルロー
ス・ナトリウム塩の製造法。
1 The degree of substitution per anhydroglucose unit is 0.3 or more and less than 3, the equivalent ratio of free carboxylic acid group to carboxylic acid sodium salt is 0.05 to 20:100, and the viscosity of 1% aqueous solution is 100 centipoise or more A method for producing carboxymethylcellulose sodium salt, which comprises heating carboxymethylcellulose sodium salt at 100 to 200°C.
JP56204578A 1981-12-17 1981-12-17 Process for producing carboxymethylcellulose sodium salt Expired JPS6036201B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP56204578A JPS6036201B2 (en) 1981-12-17 1981-12-17 Process for producing carboxymethylcellulose sodium salt

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP56204578A JPS6036201B2 (en) 1981-12-17 1981-12-17 Process for producing carboxymethylcellulose sodium salt

Publications (2)

Publication Number Publication Date
JPS58104901A JPS58104901A (en) 1983-06-22
JPS6036201B2 true JPS6036201B2 (en) 1985-08-19

Family

ID=16492784

Family Applications (1)

Application Number Title Priority Date Filing Date
JP56204578A Expired JPS6036201B2 (en) 1981-12-17 1981-12-17 Process for producing carboxymethylcellulose sodium salt

Country Status (1)

Country Link
JP (1) JPS6036201B2 (en)

Families Citing this family (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS60128437A (en) * 1983-12-16 1985-07-09 Konishiroku Photo Ind Co Ltd Heat-developable color photosensitive material
JPS61157502A (en) * 1984-12-28 1986-07-17 Daicel Chem Ind Ltd Production of easily dispersible carboxyalkylhydroxyalkyl cellulose
JPS63192351A (en) * 1987-02-02 1988-08-09 Dai Ichi Kogyo Seiyaku Co Ltd Fish farming feed in moist pellet state

Family Cites Families (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2639239A (en) * 1950-11-18 1953-05-19 Hercules Powder Co Ltd Heat-treated alkali-metal carboxymethyl cellulose and process of preparing it
US3379720A (en) * 1964-10-12 1968-04-23 Hercules Inc Water-soluble polymers and process of preparing
JPS54935A (en) * 1977-06-06 1979-01-06 Hitachi Ltd Pattern detector

Also Published As

Publication number Publication date
JPS58104901A (en) 1983-06-22

Similar Documents

Publication Publication Date Title
US6670470B1 (en) Modified starch
US3072635A (en) Readily dissolving cellulose derivatives and process therefor
US2853484A (en) Method of preparing cold swelling starch ethers and/or esters
US2503053A (en) Modification of starch
EP0311873A2 (en) Process for the preparation of a dry product useful as base material for an adhesive
JP5026972B2 (en) Inorganic matrix composites reinforced with ionically crosslinked polymers
US3038895A (en) Water-dispersible, partially substituted derivatives of amylose
CN114380927A (en) A kind of modified glucomannan and preparation method thereof
US3280102A (en) Preparation of carrageenan having improved water dispersibility
JPS6036201B2 (en) Process for producing carboxymethylcellulose sodium salt
KR102385432B1 (en) Method for increase resistant starch content of cross-linked starch using malic acid tratment
US4521594A (en) Process for producing sodium carboxymethylcellulose
JP4201391B2 (en) Wet heat-treated xanthan gum and method for producing the same
CN1210566A (en) Process for preparing spinnable isotropic cellulose solutions
JP2557645B2 (en) Deodorant fiber
US8445671B2 (en) Method for preparing polyanhydroglucuronic acid and/or salts thereof
US2555446A (en) Production of carboxyalkyl cellulose ethers
JP7645159B2 (en) Method for producing cellulose nanofiber aqueous suspension
JP7645160B2 (en) Method for producing cellulose nanofiber aqueous suspension
CN117285750A (en) Modified nanocellulose and preparation method and application thereof
JPH061801A (en) Process for cationing nongranular polysaccharide
US2765244A (en) Process for degrading dextran in the presence of a reducing agent
JP2673693B2 (en) Paper manufacturing method
US2737437A (en) Preparation of shaped cellulose articles
JPH0139443B2 (en)