JPH0985079A - Method for producing gelling agent that absorbs organic solvent and water - Google Patents
Method for producing gelling agent that absorbs organic solvent and waterInfo
- Publication number
- JPH0985079A JPH0985079A JP24461195A JP24461195A JPH0985079A JP H0985079 A JPH0985079 A JP H0985079A JP 24461195 A JP24461195 A JP 24461195A JP 24461195 A JP24461195 A JP 24461195A JP H0985079 A JPH0985079 A JP H0985079A
- Authority
- JP
- Japan
- Prior art keywords
- water
- organic solvent
- gel
- gelling agent
- cellulose derivative
- 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
Links
Landscapes
- Solid-Sorbent Or Filter-Aiding Compositions (AREA)
- Compositions Of Macromolecular Compounds (AREA)
Abstract
(57)【要約】
【課題】 溶解度パラメーター値が9以上の有機溶媒と
水を大量に吸収してゲルとなり、しかも吸収した有機溶
媒と水の保持能力に優れたゲル化剤を製造する方法の提
供。
【解決手段】 有機溶媒と水を吸収するゲル化剤であっ
て、溶解度パラメーター値が9以上の有機溶媒又は水に
溶解するセルロース誘導体と架橋剤、及び必要に応じて
反応剤を、前記溶媒又は水に溶解又は懸濁させて混合
し、次いで加熱してゲルとし、得られたゲルを乾燥す
る。前記セルロース誘導体は、ヒドロキシプロピル基を
有し、且つ該誘導体の2重量%の固形分濃度における水
溶液の粘度が25℃でB型粘度計で測定した時、100
〜1500cpsの範囲にある。(57) [Abstract] [PROBLEMS] To produce a gelling agent having a large solubility of an organic solvent having a solubility parameter value of 9 or more and water to form a gel and having an excellent ability to retain the absorbed organic solvent and water. Offer. A gelling agent that absorbs an organic solvent and water, wherein a cellulose derivative and a cross-linking agent that are soluble in an organic solvent or water having a solubility parameter value of 9 or more, and, if necessary, a reaction agent Dissolve or suspend in water to mix, then heat to gel and dry the resulting gel. The cellulose derivative has a hydroxypropyl group, and the viscosity of the aqueous solution of the derivative at a solid content concentration of 2% by weight is 100 when measured with a B-type viscometer at 25 ° C.
-1500 cps range.
Description
【0001】[0001]
【発明の属する技術分野】本発明は有機溶媒と水を吸収
するゲル化剤の製造方法に関する。さらに詳しく述べれ
ば、本発明は、自身が膨潤することにより広範囲な極性
の有機溶媒と水を大量に吸収し、しかも吸収した後はそ
の保持能力に優れたゲル化剤を製造する方法に関する。TECHNICAL FIELD The present invention relates to a method for producing a gelling agent that absorbs an organic solvent and water. More specifically, the present invention relates to a method for producing a gelling agent which absorbs a large amount of a wide range of polar organic solvents and water by itself swelling and, after absorbing, has excellent retention ability.
【0002】[0002]
【従来の技術】従来、有機溶媒や水を吸収する材料とし
ては、例えば紙、パルプ、綿等の親水性繊維、ポリエチ
レン繊維、ポリプロピレン繊維等の疎水性繊維、或いは
親水性繊維と疎水性繊維を複合化したシートや不織布が
ある。しかしながら、これらはいずれも毛細管現象によ
って繊維間の空隙に有機溶媒や水を吸着・保持するもの
であり、大量に吸収することが不可能なばかりか、外圧
を加えることによって一旦吸収したものを容易に再放出
するという欠点を有している。2. Description of the Related Art Conventionally, as materials for absorbing organic solvents and water, hydrophilic fibers such as paper, pulp and cotton, hydrophobic fibers such as polyethylene fibers and polypropylene fibers, or hydrophilic fibers and hydrophobic fibers have been used. There are composite sheets and non-woven fabrics. However, all of these adsorb and retain organic solvents and water in the voids between the fibers due to the capillary phenomenon, and it is not possible to absorb a large amount, and it is easy to absorb what was once absorbed by applying external pressure. It has the drawback of being re-emitted.
【0003】この欠点を解決するものとして、或る種の
ポリマー中に有機溶媒を吸収して膨潤させるタイプの合
成樹脂系吸油剤が公知である。例えば、特開平5ー33
7367号公報には、長鎖(3〜30)の脂肪族炭化水
素基を有し、且つアルキル(メタ)アクリレート、アル
キルアリール(メタ)アクリレート、アルキル(メタ)
アクリルアミド、アルキルアリール(メタ)アクリルア
ミド、脂肪酸ビニルエステル、アルキルスチレンおよび
α−オレフィンからなる群より選ばれる少なくとも1種
の不飽和化合物を主成分としてなる単量体と架橋性単量
体を重合して得られた吸油性架橋重合体と、水不溶性又
は水難溶性の有機酸金属塩とを混合複合化することから
なる吸油剤が開示されている。この吸油剤は、油水混合
系からでも広範な種類の油に対して多量の油を吸収して
膨潤し、しかも吸収した油の保油性に優れ、且つ吸油速
度を著しく向上したものである。As a solution to this drawback, there is known a synthetic resin-based oil absorbing agent of a type that absorbs an organic solvent into a certain polymer and swells. For example, JP-A-5-33
No. 7367 discloses an alkyl (meth) acrylate, an alkylaryl (meth) acrylate, an alkyl (meth) having a long-chain (3 to 30) aliphatic hydrocarbon group.
By polymerizing a monomer having at least one unsaturated compound selected from the group consisting of acrylamide, alkylaryl (meth) acrylamide, fatty acid vinyl ester, alkylstyrene and α-olefin as a main component and a crosslinkable monomer. Disclosed is an oil-absorbing agent comprising a mixture of the obtained oil-absorbent crosslinked polymer and a water-insoluble or sparingly water-soluble organic acid metal salt. This oil absorbing agent absorbs a large amount of oil and swells against a wide variety of oils even from an oil-water mixed system, has excellent oil retaining property of the absorbed oil, and has significantly improved oil absorbing speed.
【0004】一方、アルコールのゲル化剤として、例え
ば特開平2−286789号公報には常温で液体のアル
コールにポリビニルアルコール及びベンジリデンソルビ
トール又は/及びヒドロキシプロピルセルロース及び水
を添加することを特徴とするアルコール系携帯用固形燃
料について開示されているが、アルコール中で架橋を施
していないセルロース誘導体とポリビニルアルコール又
はベンジリデンソルビトールとの相互作用によってアル
コールがゲル化するものであり、この方法は膨潤吸収と
いう本発明のゲル化機構とは異なる。On the other hand, as an alcohol gelling agent, for example, JP-A-2-286789 discloses an alcohol characterized by adding polyvinyl alcohol and benzylidene sorbitol or / and hydroxypropyl cellulose and water to an alcohol which is liquid at room temperature. Although a solid portable fuel of the type is disclosed, the alcohol is gelated by the interaction between the cellulose derivative which is not cross-linked in the alcohol and polyvinyl alcohol or benzylidene sorbitol. Is different from the gelation mechanism of.
【0005】[0005]
【発明が解決しようとする課題】本発明者等は、かかる
現状に鑑み、溶解度パラメーター値が9以上の有機溶媒
と水を吸収してゲル化する材料について鋭意検討を行っ
た結果、溶解度パラメーター値が9以上の有機溶媒と水
に溶解する特定のセルロース誘導体に架橋剤、及び必要
に応じて反応助剤を添加し、得られる混合物の溶液又は
懸濁液を加熱して架橋反応を施し、ゲルを生成させ、次
いでゲルを乾燥して得られる架橋セルロース誘導体から
なるゲルは、自身は前記有機溶媒と水に溶解せず、逆に
前記溶媒と水をよく吸収してゲル化することを見出し本
発明を完成するに至った。本発明の目的は、自身が溶解
せずに膨潤することにより溶解パラメーター値が9以上
の有機溶媒と水を大量に吸収してゲルとなり、しかも吸
収した有機溶媒と水の保持能力に優れたゲル化剤を製造
する方法を提供することにある。In view of the above situation, the inventors of the present invention have earnestly studied a material which absorbs water and an organic solvent having a solubility parameter value of 9 or more and gelates, and as a result, the solubility parameter value is obtained. Is added to a specific cellulose derivative soluble in 9 or more organic solvents and water, a crosslinking agent, and if necessary, a reaction auxiliary agent, and a solution or suspension of the resulting mixture is heated to perform a crosslinking reaction, and a gel It is found that a gel composed of a crosslinked cellulose derivative obtained by producing a gel and then drying the gel itself does not dissolve in the organic solvent and water, but conversely absorbs the solvent and water well to form a gel. The invention was completed. The object of the present invention is to absorb a large amount of an organic solvent having a solubility parameter value of 9 or more and water to form a gel by swelling without dissolving itself, and a gel excellent in the ability to retain the absorbed organic solvent and water. It is to provide a method for producing an agent.
【0006】[0006]
【課題を解決するための手段】本発明の第一は、溶解度
パラメーター値が9以上の有機溶媒又は水に溶解するセ
ルロース誘導体と架橋剤、及び必要に応じて反応助剤
を、前記溶媒、水又は溶媒と水の混合物に溶解又は懸濁
させて混合し、次いで加熱してゲルとし、得られたゲル
を乾燥することを特徴とする有機溶媒と水を吸収するゲ
ル化剤の製造方法である。本発明の第二は、前記セルロ
ース誘導体がヒドロキシプロピル基を有し、且つ該誘導
体の2重量%の固形分濃度における水溶液の粘度が25
℃でB型粘度計で測定した時、100〜1500cps
の範囲であることを特徴とする本発明第一に記載の有機
溶媒と水を吸収するゲル化剤の製造方法である。The first aspect of the present invention is to provide a cellulose derivative and a cross-linking agent which are soluble in an organic solvent or water having a solubility parameter value of 9 or more, and, if necessary, a reaction auxiliary agent in the solvent, water. Alternatively, it is a method for producing a gelling agent that absorbs an organic solvent and water, characterized by dissolving or suspending in a mixture of a solvent and water, mixing them, and then heating to form a gel, and drying the obtained gel. . A second aspect of the present invention is that the cellulose derivative has a hydroxypropyl group, and the viscosity of an aqueous solution of the derivative at a solid content concentration of 2% by weight is 25.
100-1500 cps when measured with B-type viscometer at ℃
The method for producing a gelling agent for absorbing an organic solvent and water according to the first aspect of the present invention is characterized in that
【0007】[0007]
【発明の実施の形態】本発明で用いられる溶解度パラメ
ーター値(Solubility Parameter Value)とは、化合
物の極性を表す尺度として用いられるもので下記式
(1)で算出される値と定義され、単位が(cal/c
m3)1/2で表される(Polymer Handbook,Third Editi
on,JOHN WILEY & SONS、1989参照)。 δi={(Hi v−RT)/Vi}1/2・・・(1) ただし、δi=成分iの溶解度パラメータ値 Hi v=成分iの気化熱(cal) R=理想気体定数(cal/K・mol) T=絶対温度(K) Vi=成分iのモル体積(cm3/mol) である。BEST MODE FOR CARRYING OUT THE INVENTION The solubility parameter value used in the present invention is used as a scale representing the polarity of a compound and is defined as a value calculated by the following formula (1), and its unit is (Cal / c
m 3 ) 1/2 (Polymer Handbook, Third Editi
on, JOHN WILEY & SONS, 1989). δ i = {(H i v -RT) / V i} 1/2 ··· (1) However, [delta] i = solubility of component i parameter values H i v = heat of vaporization component i (cal) R = ideal Gas constant (cal / K · mol) T = absolute temperature (K) V i = molar volume of component i (cm 3 / mol).
【0008】本発明で用いられる溶解度パラメーター値
が9以上の有機溶媒又は水に溶解するセルロース誘導体
は、ヒドロキシプロピル基を有し、このような誘導体と
しては、ヒドロキシプロピルセルロース、ヒドロキシエ
チルヒドロキシプロピルセルロース、ヒドロキシプロピ
ルメチルセルロース等が例示でき、これらは単独で、も
しくは適宜選択して混合して用いられる。又、前記セル
ロース誘導体は、ヒドロキシプロピル基以外の置換基、
例えばメチル基、エチル基、ヒドロキシエチル基、シア
ノエチル基、カルボキシメチル基、カルボキシエチル基
等を1種以上含有していてもよい。更に、前記セルロー
ス誘導体は、溶解度パラメーター値が9以上の有機溶媒
又は水に溶解するものであればどのような置換度(セル
ロースの無水グルコース単位当りに結合している置換基
の割合)のものを用いてもよい。The cellulose derivative used in the present invention which is soluble in an organic solvent having a solubility parameter value of 9 or more or water has a hydroxypropyl group, and examples of such a derivative include hydroxypropyl cellulose, hydroxyethyl hydroxypropyl cellulose, Hydroxypropylmethyl cellulose and the like can be exemplified, and these can be used alone or appropriately selected and mixed. Further, the cellulose derivative is a substituent other than a hydroxypropyl group,
For example, it may contain one or more of methyl group, ethyl group, hydroxyethyl group, cyanoethyl group, carboxymethyl group, carboxyethyl group and the like. Further, the cellulose derivative may have any substitution degree (ratio of substituents bonded per anhydroglucose unit of cellulose) as long as it is soluble in an organic solvent having a solubility parameter value of 9 or more or water. You may use.
【0009】本発明で用いられるセルロース誘導体は、
前記の構成上の相違の他、該セルロース誘導体を固形分
濃度2重量%で純水に溶解した時に、水溶液の粘度が1
00〜1500cps(25℃、B型粘度計)の範囲内
にある必要がある。水溶液の粘度が100cps未満の
場合、セルロース誘導体の分子量が小さ過ぎることを意
味し、このようなセルロース誘導体を用いて得られるゲ
ル化剤は、有機溶媒と水の吸収量が著しく低下し、実用
的ではない。逆に、水溶液の粘度が1500cpsを越
える場合、他の薬品を添加して撹拌する際に流動性が不
十分なため均一な溶液又は懸濁液が得られず、溶液又は
懸濁液を均一化するためにセルロース誘導体の濃度を減
じると十分な架橋が起き難くなり、ゲル強度が弱くて所
望のゲル化剤を製造することができない。The cellulose derivative used in the present invention is
In addition to the above structural differences, when the cellulose derivative is dissolved in pure water at a solid concentration of 2% by weight, the viscosity of the aqueous solution becomes 1
It must be in the range of 00 to 1500 cps (25 ° C, B-type viscometer). When the viscosity of the aqueous solution is less than 100 cps, it means that the molecular weight of the cellulose derivative is too small, and the gelling agent obtained by using such a cellulose derivative has a significantly reduced absorption amount of the organic solvent and water, and is practically used. is not. On the contrary, when the viscosity of the aqueous solution exceeds 1500 cps, a uniform solution or suspension cannot be obtained due to insufficient fluidity when other chemicals are added and stirred, and the solution or suspension is homogenized. Therefore, if the concentration of the cellulose derivative is reduced, sufficient cross-linking becomes difficult to occur, and the gel strength is so weak that a desired gelling agent cannot be produced.
【0010】前記したように、本発明ではセルロース誘
導体を溶媒に均一に溶解又は懸濁させるが、この時、固
形分濃度が低過ぎるとゲルの形成が困難になったり、架
橋剤を大量添加せざるを得なくなったりするので、可能
な限り高めの濃度とするのがよい。本発明では、このセ
ルロース誘導体を溶解又は懸濁させる時の固形分濃度
は、セルロース誘導体の種類、水溶液とした時の粘度、
溶媒の種類等により異なるが、全重量当り7〜15重量
%の範囲である。用いられる溶媒としては溶解度パラメ
ーター値が9以上の有機溶媒、水又は有機溶媒が水に可
溶性の場合、有機溶媒と水の混合物を挙げることができ
適宜選択して用いられる。As described above, in the present invention, the cellulose derivative is uniformly dissolved or suspended in the solvent. At this time, if the solid content concentration is too low, it becomes difficult to form a gel or a large amount of a crosslinking agent is added. There is no choice but to do so, so it is good to set the concentration as high as possible. In the present invention, the solid content concentration when the cellulose derivative is dissolved or suspended is the type of the cellulose derivative, the viscosity when the solution is an aqueous solution,
Although it depends on the type of solvent and the like, it is in the range of 7 to 15% by weight based on the total weight. Examples of the solvent used include an organic solvent having a solubility parameter value of 9 or more, water, and when the organic solvent is soluble in water, a mixture of the organic solvent and water can be used, and the solvent is appropriately selected and used.
【0011】本発明で用いられる架橋剤は、有機溶媒や
水中でセルロース誘導体に対して反応性のあるものであ
ればよく、例えば、ホルムアルデヒド、グリオキザール
等のアルデヒド類;エチレングリコールジグリシジルエ
ーテル、ポリエチレングリコールジグリシジルエーテ
ル、ジエポキシブタン等の多価エポキシ化合物類;ジビ
ニルスルホン、メチレンビスアクリルアミド等のジビニ
ル化合物類;ジクロロアセトン、ジクロロプロパノー
ル、ジクロロ酢酸等の多価ハロゲン化合物類;エピクロ
ロヒドリン、エピブロモヒドリン等のハロヒドリン化合
物類;並びにN,N’−ヘキサメチレン−1−ビス−
(1−アジリジンカルボキシアミド)、テトラメチロー
ルメタン−トリ−β−アジリジニルプロピオネート、ト
リメチロールプロパン−トリ−β−アジリジニルプロピ
オネート等の多価アジリジン化合物類等を挙げることが
でき、適宜選択して1種以上が用いられる。The cross-linking agent used in the present invention may be one which is reactive with the cellulose derivative in an organic solvent or water, for example, aldehydes such as formaldehyde and glyoxal; ethylene glycol diglycidyl ether, polyethylene glycol. Polyvalent epoxy compounds such as diglycidyl ether and diepoxy butane; Divinyl compounds such as divinyl sulfone and methylenebisacrylamide; Polyvalent halogen compounds such as dichloroacetone, dichloropropanol and dichloroacetic acid; Epichlorohydrin, epibromo Halohydrin compounds such as hydrin; and N, N'-hexamethylene-1-bis-
(1-aziridinecarboxamide), tetramethylolmethane-tri-β-aziridinylpropionate, trimethylolpropane-tri-β-aziridinylpropionate, and other polyvalent aziridine compounds, and the like. , Appropriately selected and used in one or more kinds.
【0012】セルロース誘導体と架橋剤との混合物を加
熱して架橋を行う場合に、架橋剤の種類によっては反応
助剤を必要とするものがあるので適宜必要に応じて反応
助剤が用いられる。例えば、架橋剤としてアルデヒド類
を用いる場合には、反応助剤として塩酸のような酸が必
要であるし、ジビニル化合物類、多価ハロゲン化合物
類、多価エポキシ化合物類及び多価アジリジン化合物類
を用いる場合には、反応助剤としてアルカリ金属水酸化
物のようなアルカリが必要である。架橋剤の添加率は、
架橋剤の種類によって異なるが、セルロース誘導体の絶
乾重量当り0.5%〜20重量%である。添加率が0.
5重量%未満では、量が少な過ぎてゲルの形成が困難と
なり、逆に添加率が20重量%を越えて多くなると、得
られたゲル化剤の有機溶媒や水の吸収量が低下する。When a mixture of a cellulose derivative and a cross-linking agent is heated for cross-linking, a reaction aid may be used depending on the type of the cross-linking agent. For example, when aldehydes are used as a cross-linking agent, an acid such as hydrochloric acid is required as a reaction aid, and divinyl compounds, polyvalent halogen compounds, polyvalent epoxy compounds and polyvalent aziridine compounds are required. When used, an alkali such as an alkali metal hydroxide is required as a reaction aid. The crosslinker addition rate is
The amount is 0.5% to 20% by weight based on the absolute dry weight of the cellulose derivative, although it depends on the type of the crosslinking agent. The addition rate is 0.
If it is less than 5% by weight, the amount of the gelling agent becomes too small and it becomes difficult to form a gel. On the contrary, if the amount of addition exceeds 20% by weight, the gelling agent obtained has a low absorption amount of organic solvent and water.
【0013】本発明では、セルロース誘導体と架橋剤を
溶媒に溶解させ、更に必要に応じて反応助剤を添加して
溶解又は懸濁させ、このようにして得られた混合溶液又
は懸濁液を30〜90℃の温度で2〜24時間加熱する
ことによって架橋反応を行う。温度が30℃未満では架
橋反応の進行が遅く、温度が90℃を越えると、セルロ
ース誘導体の低分子化が進行して、得られるゲル化剤の
有機溶媒と水に対する吸収量の低下をもたらす。時間に
ついては通常、2〜5時間の加熱時間でブロック状のゲ
ルが生成するが、更に、24時間以内の範囲で加熱を継
続すると、得られるゲル化剤は有機溶媒や水に対して吸
収量が増加するので時間の長い方が好ましい。しかしな
がら、加熱時間が24時間を越えると、セルロース誘導
体の低分子化を招き、前記吸収量の低下をもたらす恐れ
がある。In the present invention, the cellulose derivative and the cross-linking agent are dissolved in a solvent, and if necessary, a reaction aid is added to dissolve or suspend the mixture, and the mixed solution or suspension thus obtained is added. The crosslinking reaction is carried out by heating at a temperature of 30 to 90 ° C. for 2 to 24 hours. If the temperature is lower than 30 ° C., the progress of the crosslinking reaction is slow, and if the temperature exceeds 90 ° C., the molecular weight of the cellulose derivative is promoted, and the gelling agent obtained has a reduced absorption amount with respect to the organic solvent and water. Regarding the time, usually, a block-like gel is formed in a heating time of 2 to 5 hours, but when the heating is continued within the range of 24 hours, the obtained gelling agent absorbs an organic solvent and water. Therefore, the longer the time is, the better. However, if the heating time exceeds 24 hours, the molecular weight of the cellulose derivative may be lowered, and the absorption amount may be lowered.
【0014】一方、セルロース誘導体の架橋反応を行う
際に、加熱前の混合物の溶液又は液ー液懸濁液を合成フ
ィルム、シート状基材、布もしくは不織布に塗工又は含
浸した後、前記の温度と時間の条件下で加熱することに
よって架橋反応と乾燥を同時に行い、用いた基材にゲル
化剤を担持させたものを得ることもできる。この方法に
よってフィルム状、シート状、布状もしくは不織布の形
状をしたゲル化剤が得られ、様々な用途に応用すること
ができる。更に、前記のセルロース誘導体混合物の架橋
前の水溶液又懸濁液に、パルプ繊維のような短繊維を混
合して加熱、乾燥してゲル化剤に強度を付与したり、同
様にして水酸化アルミニウム、酸化アルミニウム等の難
燃性や不燃性物質を混合してゲル化剤に難燃性を付与す
ることもできる。このようにして得られる架橋セルロー
ス誘導体ゲル化剤は、未反応の架橋剤や反応助剤を含有
するが、そのまま乾燥してもよいし、後処理によってこ
れらを除去してもよい。その場合、例えば、得られたゲ
ル化剤を水中で膨潤させ、次いで取り出し、加熱して脱
膨潤させるという操作を数回繰り返すことによって水溶
性の不純物を除去することができる。On the other hand, in carrying out the cross-linking reaction of the cellulose derivative, after applying or impregnating the solution or liquid-liquid suspension of the mixture before heating onto the synthetic film, sheet-shaped substrate, cloth or nonwoven fabric, It is also possible to obtain a product in which the gelling agent is supported on the base material used by simultaneously performing the crosslinking reaction and drying by heating under the conditions of temperature and time. By this method, a gelling agent in the form of a film, a sheet, a cloth or a non-woven fabric can be obtained and applied to various uses. Furthermore, short fibers such as pulp fibers are mixed with an aqueous solution or suspension of the above-mentioned cellulose derivative mixture before crosslinking, and the mixture is heated and dried to impart strength to the gelling agent, or similarly aluminum hydroxide is used. It is also possible to impart flame retardancy to the gelling agent by mixing a flame retardant or non-flammable substance such as aluminum oxide. The cross-linked cellulose derivative gelling agent thus obtained contains unreacted cross-linking agent and reaction aid, but may be dried as it is or may be removed by post-treatment. In that case, for example, the water-soluble impurities can be removed by repeating the operation of swelling the obtained gelling agent in water, then taking it out, and heating and de-swelling it several times.
【0015】本発明のゲル化剤は、前記したように、反
応によって生成されたゲルに含有される不純物を除去し
ないで、又は除去し、次いで有機溶媒や水を除去するこ
とによって得られるが、ゲル中の有機溶媒が水を含んで
いる場合には、ゲル中の水を有機溶媒で置換除去してか
ら乾燥する方が高い吸収能力を有するゲル化剤が得られ
る。ゲル中の水を有機溶媒で置換する方法には、水と混
和する有機溶媒を使用する方法と、水と混和しない有機
溶媒を使用する方法とがある。前者にはメタノールのよ
うな低級アルコール類、アセトンのようなケトン類等が
用いられ、水を含むゲルをそれら水混和性有機溶媒の中
に一定時間浸漬して、ゲル中の水を水混和性有機溶媒で
置換するというものである。後者にはトルエンのように
水と混和せず、且つ100℃以上の温度で水と共沸する
有機溶媒が用いられ、水を含むゲルをそれらの水と混和
しない有機溶媒の中で加熱することによってゲル中の水
が共沸除去されるというものである。有機溶媒での水の
置換除去や脱水した後のゲルの乾燥は、150℃以下の
温度で行うのが好ましく、熱風乾燥、マイクロ波乾燥、
赤外線乾燥、減圧乾燥等の公知の乾燥方法を用いてゲル
中の有機溶媒を除去することができる。As described above, the gelling agent of the present invention can be obtained by removing the impurities contained in the gel produced by the reaction, or by removing the impurities and then removing the organic solvent and water. When the organic solvent in the gel contains water, a gelling agent having a higher absorption capacity can be obtained by substituting water in the gel with an organic solvent and then drying. As a method for replacing water in the gel with an organic solvent, there are a method using an organic solvent miscible with water and a method using an organic solvent immiscible with water. For the former, lower alcohols such as methanol and ketones such as acetone are used, and the gel containing water is immersed in the water-miscible organic solvent for a certain period of time to make the water in the gel miscible with water. Substitution with an organic solvent. For the latter, an organic solvent which is immiscible with water, such as toluene, and which is azeotropic with water at a temperature of 100 ° C. or higher is used, and the gel containing water is heated in an organic solvent which is immiscible with water. The water in the gel is removed azeotropically. The gel is preferably dried at a temperature of 150 ° C. or lower after the removal of water by an organic solvent and the dehydration of the gel, hot air drying, microwave drying,
The organic solvent in the gel can be removed by using a known drying method such as infrared drying or reduced pressure drying.
【0016】一方、上記ブロック状ゲルは、粒径を小さ
くすることによって溶媒の吸収速度を向上させることが
できる。粒径を小さくする方法は、架橋反応直後のゲル
状のゲルをカッター、ミキサー等で粉砕してもよく、脱
水乾燥後のゲル化剤をミルで粉砕してもよい。このよう
にして得られる本発明のゲル化剤は、フィルム状、シー
ト状、布状、不織布状、或いはブロック状、粒状、粉末
状をしており、溶解度パラメーター値が9以上の有機溶
媒、水或いは両者の混合物を吸収してゲル化し、加圧下
においても吸収した溶媒を保持でき、しかも原料がセル
ロース系であるためゲル化剤は生分解性を有している。On the other hand, the block-shaped gel can improve the absorption rate of the solvent by reducing the particle size. As a method for reducing the particle size, a gel-like gel immediately after the crosslinking reaction may be pulverized with a cutter, a mixer, or the like, and a gelling agent after dehydration drying may be pulverized with a mill. The gelling agent of the present invention thus obtained has a film shape, a sheet shape, a cloth shape, a non-woven cloth shape, or a block shape, a granular shape, or a powder shape, and has an solubility parameter value of 9 or more, an organic solvent, or water. Alternatively, the mixture of both is absorbed and gelled, and the absorbed solvent can be retained even under pressure, and the gelling agent is biodegradable because the raw material is cellulose.
【0017】本発明のゲル化剤は種々の形態で使用する
ことができ、例えば、ブロック状、粒状或いは粉末状の
ゲル化剤を前記液体の中に直接散布してもよく、円筒管
のような開放系容器内に充填し、被吸収液体を通過させ
てもよい。或いは別の方法としては、前記ブロック状、
粒状或いは粉末状のゲル化剤を液体通過性のよい袋や多
孔質パッケージ内に充填して用いてもよく、更に、パル
プ繊維、綿、不織布、多孔質炭酸カルシウム、多孔質シ
リカ、ナイロン繊維、ポリプロピレン繊維等の公知の充
填剤又は吸収剤と併用して用いることができる。一方、
本発明のフィルム状又はシート状のゲル化剤は親水性の
インクを吸収する記録材料として用いることもできる。
以上説明したように、本発明により得られるゲル化剤
は、漏洩有機溶媒処理剤、有機廃液固化剤、有機溶媒ガ
スの吸着材、工業用又は家庭用ふき取り材、化学ぞうき
ん、溶剤漏洩センサー、有機溶媒保持材、土壌保水材、
育苗用シート等の農業資材分野、食品鮮度保持材、防か
び剤、脱水剤等の食品分野、建物の結露防止シートなど
の建築材料、各種芳香剤、殺虫剤等の徐放性基材として
広範囲に使用できるものである。The gelling agent of the present invention can be used in various forms, for example, a block, granular or powdery gelling agent may be directly dispersed in the liquid, such as a cylindrical tube. The liquid to be absorbed may be allowed to pass through by filling the inside of an open system container. Alternatively, as another method, the block shape,
Granular or powdery gelling agent may be used by filling it in a bag or a porous package having good liquid permeability, and further, pulp fiber, cotton, nonwoven fabric, porous calcium carbonate, porous silica, nylon fiber, It can be used in combination with a known filler or absorbent such as polypropylene fiber. on the other hand,
The film-like or sheet-like gelling agent of the present invention can also be used as a recording material that absorbs hydrophilic ink.
As described above, the gelling agent obtained by the present invention is a leakage organic solvent treating agent, an organic waste liquid solidifying agent, an organic solvent gas adsorbent, an industrial or household wiping material, a chemical wipe, a solvent leakage sensor, an organic solvent. Solvent retention material, soil water retention material,
Widely used as a field for agricultural materials such as nursery sheets, food freshness-maintaining materials, food fields for fungicides, dehydrating agents, building materials such as dew condensation prevention sheets for buildings, various release agents for aromatic agents, insecticides, etc. It can be used for.
【0018】[0018]
【実施例】以下に実施例を挙げて本発明をより具体的に
説明するが、勿論本発明はこれらによって限定されるも
のではない。なお、特に断りのない限り、%は重量%を
示す。The present invention will be described in more detail with reference to the following examples, but of course the present invention is not limited thereto. Unless otherwise specified,% means% by weight.
【0019】実施例1 水76gに水酸化ナトリウム2gを溶解し、次いでイソ
プロピルアルコール970gとエチレングリコールジグ
リシジルエーテル10gを混合し、撹拌しながらヒドロ
キシプロピルセルロース(東京化成工業製、2%水溶液
のB型粘度計による粘度は250cps)100gを添
加して溶解させ、全重量当りのヒドロキシプロピルセル
ロースの濃度が8.6%の混合溶液を準備した。次に、
この混合溶液を温度40℃で16時間加熱し、架橋反応
を行なわせ、ゲルを生成させた。得られたゲルをカッタ
ーナイフで5mm角に切断し、1規定塩酸400g中に
1時間浸漬して過剰な水酸化ナトリウムを除去した。得
られた水和ゲルを6000gの水中に移し、50℃に加
熱してゲル中の水分を追い出した後取り出し、続いて5
000gのアセトンに2時間浸漬して完全に水をアセト
ンで置換し、取り出した後、減圧乾燥してゲル化剤を得
た。得られた乾燥ゲル化剤を下記に示す測定法により各
種の有機溶媒と純水の吸収量を測定し、その品質を評価
した。Example 1 2 g of sodium hydroxide was dissolved in 76 g of water, and then 970 g of isopropyl alcohol and 10 g of ethylene glycol diglycidyl ether were mixed, and hydroxypropyl cellulose (manufactured by Tokyo Chemical Industry Co., Ltd., 2% aqueous solution type B) was mixed with stirring. 100 g of a viscosity measured by a viscometer was 250 cps) and dissolved to prepare a mixed solution in which the concentration of hydroxypropyl cellulose based on the total weight was 8.6%. next,
This mixed solution was heated at a temperature of 40 ° C. for 16 hours to cause a crosslinking reaction to form a gel. The obtained gel was cut into a 5 mm square with a cutter knife and immersed in 400 g of 1N hydrochloric acid for 1 hour to remove excess sodium hydroxide. The obtained hydrated gel was transferred to 6000 g of water, heated to 50 ° C. to drive out water in the gel and then taken out, followed by 5
It was immersed in 000 g of acetone for 2 hours to completely replace water with acetone, taken out, and dried under reduced pressure to obtain a gelling agent. The quality of the dried gelling agent thus obtained was evaluated by measuring the amounts of various organic solvents and pure water absorbed by the following measuring methods.
【0020】吸収量の測定法 乾燥試料0.8gを10cm×10cmの250メッシ
ュナイロン製網袋に封入し、これを下記、表1及び表2
に示される溶解度パラメーター値が7〜24の範囲の有
機溶媒と水からなる各種の被測定溶液に24時間浸漬し
て吸収させ、次いで、これを引き上げて10分間吊り下
げ液切りを行った後、試料の重量を測定し、絶乾試料1
g当りに吸収された被測定溶液(g)をもって加圧前の
吸収量とした。次いで、直径16cmのNo.2濾紙
(東洋濾紙製)25枚(ゲル化剤の上に10枚、同じく
ゲル化剤の下に15枚)の間に挟み、重ねた濾紙の上に
直径16cm、重量100gのステンレス板を重ね、更
にその上に1kgのおもりを乗せて5分間試料に圧力を
かけ、ゲル中の隙間に存在する液体を濾紙に吸収させ
た。その後、試料の重量を測定し、絶乾試料1g当りの
吸収・保持されている被測定溶液(g)をもって加圧後
の吸収量とした。 Method of measuring absorption amount 0.8 g of a dried sample was sealed in a 10 cm × 10 cm 250-mesh nylon net bag, which was shown in Table 1 and Table 2 below.
Solubility parameter value shown in is immersed in various measured solutions consisting of an organic solvent and water in the range of 7 to 24 for 24 hours for absorption, and then pulled up and suspended for 10 minutes to drain, Weigh the sample and dry sample 1
The measured solution (g) absorbed per g was defined as the absorption amount before pressurization. Then, the No. 2 Sheets of filter paper (made by Toyo Roshi Kaisha, Ltd.) 25 sheets (10 sheets above the gelling agent, 15 sheets below the gelling agent as well) were sandwiched, and a stainless steel plate having a diameter of 16 cm and a weight of 100 g was stacked on the stacked filter sheets. Then, a weight of 1 kg was placed on the sample, and pressure was applied to the sample for 5 minutes so that the liquid existing in the gap in the gel was absorbed by the filter paper. After that, the weight of the sample was measured, and the measured and absorbed solution (g) per 1 g of the absolutely dried sample was defined as the absorption amount after pressurization.
【0021】測定に用いた被測定溶液を以下に示す。た
だし()内の数字は被測定溶液の溶解度パラメーター値
を示す。 (1)溶解度パラメーター値が9以上の溶媒:イオン交
換樹脂を通して脱イオンした水を蒸留して得た純水(2
3.4)、エチレングリコール(14.6)、メタノー
ル(14.5)、エタノール(12.7)、イソプロピ
ルアルコール(11.5)、酢酸(10.1)、アセト
ン(9.9)、クロロホルム(9.3)、テトラヒドロ
フラン(9.1)。 (2)溶解度パラメーター値が9未満の溶媒:トルエン
(8.9)、シクロヘキサン(8.2)、n−ヘキサン
(7.3)。The solution to be measured used for the measurement is shown below. However, the number in parentheses indicates the solubility parameter value of the solution to be measured. (1) Solvent having a solubility parameter value of 9 or more: Pure water obtained by distilling deionized water through an ion exchange resin (2
3.4), ethylene glycol (14.6), methanol (14.5), ethanol (12.7), isopropyl alcohol (11.5), acetic acid (10.1), acetone (9.9), chloroform. (9.3), tetrahydrofuran (9.1). (2) Solvent having a solubility parameter value of less than 9: toluene (8.9), cyclohexane (8.2), n-hexane (7.3).
【0022】実施例2 得られた水和ゲルをアセトンに浸漬して水分を除去する
代わりに、水和ゲルをトルエン4000g中で加熱し共
沸脱水したこと以外は、実施例1と同様にして減圧乾燥
しゲル化剤を得た。実施例1と同様にして被測定溶液の
吸収量を測定した。Example 2 In the same manner as in Example 1 except that the obtained hydrated gel was heated in 4000 g of toluene and azeotropically dehydrated instead of immersing the obtained hydrated gel in acetone to remove water. It was dried under reduced pressure to obtain a gelling agent. The amount of absorption of the solution to be measured was measured in the same manner as in Example 1.
【0023】実施例3 水76gに水酸化ナトリウム10gを溶解し、次にエピ
クロルヒドリン5gとイソプロピルアルコール970g
を加え、次いでヒドロキシプロピルセルロース100g
を混合し、全重量当りヒドロキシプロピルセルロースの
濃度が8.6%の混合溶液とした後、この混合溶液を温
度40℃で16時間加熱した。得られた水和ゲルをトル
エン4000g中で加熱し、共沸脱水してから実施例1
と同様にして減圧乾燥しゲル化剤を得た。実施例1と同
様にして被測定液の吸収量を測定した。Example 3 10 g of sodium hydroxide was dissolved in 76 g of water, then 5 g of epichlorohydrin and 970 g of isopropyl alcohol.
And then 100 g of hydroxypropyl cellulose
Were mixed to form a mixed solution having a hydroxypropylcellulose concentration of 8.6% based on the total weight, and the mixed solution was heated at a temperature of 40 ° C. for 16 hours. The obtained hydrated gel was heated in 4000 g of toluene to undergo azeotropic dehydration, and then Example 1
It was dried under reduced pressure in the same manner as above to obtain a gelling agent. The amount of absorption of the liquid to be measured was measured in the same manner as in Example 1.
【0024】実施例4 水76gに水酸化ナトリウム10gとN,N’−メチレ
ンビスアクリルアミド5gとイソプロピルアルコール9
70gを加え、次いでヒドロキシプロピルセルロース1
00gを混合し、全重量当りヒドロキシプロピルセルロ
ースの濃度が8.6%の混合溶液とした後、この混合溶
液を温度40℃で16時間加熱した。得られた水和ゲル
をトルエン4000g中で加熱し、共沸脱水してから実
施例1と同様にして減圧乾燥しゲル化剤を得た。実施例
1と同様にして被測定液の吸収量を測定した。Example 4 10 g of sodium hydroxide, 5 g of N, N'-methylenebisacrylamide and 9 of isopropyl alcohol were added to 76 g of water.
Add 70 g, then hydroxypropyl cellulose 1
00 g was mixed to form a mixed solution having a hydroxypropylcellulose concentration of 8.6% based on the total weight, and the mixed solution was heated at a temperature of 40 ° C. for 16 hours. The obtained hydrated gel was heated in 4000 g of toluene for azeotropic dehydration, and then dried under reduced pressure in the same manner as in Example 1 to obtain a gelling agent. The amount of absorption of the liquid to be measured was measured in the same manner as in Example 1.
【0025】実施例5 テトラヒドロフラン900gにヒドロキシエチルヒドロ
キシプロピルセルロース(自製、2%水溶液のB型粘度
計による粘度は450cps)100gとトルエンジイ
ソシアネート2gを溶解し、全重量当りヒドロキシエチ
ルヒドロキシプロピルセルロースの濃度が10.0%の
混合溶液とし、この混合溶液を温度40℃で10時間加
熱した。得られたゲルを5mm角に切断し、5000g
の水とともにミキサーに入れて粉砕した。粉砕したゲル
を10リットル容の容器にいれ1時間放置後、50℃に
昇温してゲル中の水を追い出し、得られた水和ゲルをト
ルエン4000g中で加熱し、共沸脱水してから実施例
1と同様にして減圧乾燥しゲル化剤を得た。実施例1と
同様にして被測定液の吸収量を測定した。Example 5 In 900 g of tetrahydrofuran, 100 g of hydroxyethyl hydroxypropyl cellulose (manufactured by itself, the viscosity of a 2% aqueous solution by a B type viscometer is 450 cps) and 2 g of toluene diisocyanate were dissolved, and the concentration of hydroxyethyl hydroxypropyl cellulose was adjusted to the total weight. A 10.0% mixed solution was prepared, and this mixed solution was heated at a temperature of 40 ° C. for 10 hours. The resulting gel is cut into 5 mm squares and 5000 g
It was put into a mixer with water and crushed. Put the crushed gel in a 10 liter container for 1 hour, then raise the temperature to 50 ° C. to drive out the water in the gel, heat the obtained hydrated gel in 4000 g of toluene, and azeotropically dehydrate it. It was dried under reduced pressure in the same manner as in Example 1 to obtain a gelling agent. The amount of absorption of the liquid to be measured was measured in the same manner as in Example 1.
【0026】実施例6 ヒドロキシプロピルセルロース100gに45%固形分
濃度のホウフッ化亜鉛水溶液5gと水700gを加えて
均一な混合溶液とした後、更にエチレングリコールジグ
リシジルエーテル10gを混合し、全重量当りのヒドロ
キシプロピルセルロースの濃度が12.3%の混合溶液
とし、この混合溶液を温度40℃で8時間加熱し、ゲル
を生成した。得られたゲルをメタノール6000gとと
もにミキサーに入れて粉砕し、粉砕したゲルを濾過し、
次いで水5000g中に1時間浸漬し、得られた水和ゲ
ルをトルエン4000g中で加熱し、共沸脱水してから
実施例1と同様にして減圧乾燥しゲル化剤を得た。実施
例1と同様にして被測定液の吸収量を測定した。Example 6 To 100 g of hydroxypropyl cellulose, 5 g of a zinc borofluoride aqueous solution having a solid concentration of 45% and 700 g of water were added to form a uniform mixed solution, and then 10 g of ethylene glycol diglycidyl ether was further mixed, based on the total weight. Was prepared as a mixed solution having a hydroxypropylcellulose concentration of 12.3%, and the mixed solution was heated at a temperature of 40 ° C. for 8 hours to form a gel. The obtained gel was put into a mixer together with 6000 g of methanol and crushed, and the crushed gel was filtered,
Then, the gel was dipped in 5000 g of water for 1 hour, the resulting hydrated gel was heated in 4000 g of toluene for azeotropic dehydration, and then dried under reduced pressure in the same manner as in Example 1 to obtain a gelling agent. The amount of absorption of the liquid to be measured was measured in the same manner as in Example 1.
【0027】実施例7 水76gに水酸化ナトリウム10gを溶解し、次にエピ
クロルヒドリン5gとイソプロピルアルコール970g
を添加し、更に実施例5で用いたヒドロキシエチルヒド
ロキシプロピルセルロース100gを混合し、全重量当
りのヒドロキシエチルヒドロキシプロピルセルロースの
濃度が8.6%の混合溶液とし、この混合溶液を温度4
0℃で16時間加熱してゲルを得、これを1cm角に切
断した。この切断したゲルを6%固形分濃度の硫酸ナト
リウム水溶液5000gとともにミキサーに入れて粉砕
した。粉砕したゲル中の未使用のアルカリを最少量の濃
硫酸で中和し、1時間放置した後に濾過し、温水100
0gで3回洗浄した後、得られたゲルをトルエン400
0g中で加熱し、共沸脱水してから実施例1と同様にし
てゲル化剤を得た。実施例1と同様にして被測定液の吸
収量を測定した。Example 7 10 g of sodium hydroxide was dissolved in 76 g of water, then 5 g of epichlorohydrin and 970 g of isopropyl alcohol.
Was further added, and 100 g of hydroxyethylhydroxypropylcellulose used in Example 5 was mixed to form a mixed solution having a concentration of hydroxyethylhydroxypropylcellulose of 8.6% based on the total weight.
A gel was obtained by heating at 0 ° C. for 16 hours, and the gel was cut into 1 cm squares. The cut gel was put into a mixer together with 5000 g of an aqueous sodium sulfate solution having a solid content of 6% and ground. The unused alkali in the crushed gel was neutralized with the minimum amount of concentrated sulfuric acid, left for 1 hour, and then filtered to obtain 100 parts of warm water.
After washing 3 times with 0 g, the gel obtained was washed with toluene 400
A gelling agent was obtained in the same manner as in Example 1 after heating in 0 g for azeotropic dehydration. The amount of absorption of the liquid to be measured was measured in the same manner as in Example 1.
【0028】比較例1 2%固形分濃度の水溶液のB型粘度計による粘度が8c
psのヒドロキシプロピルセルロース(東京化成工業
製)を用いたこと以外は、実施例3と同様にして乾燥し
たゲル化剤を得た。実施例1と同様にして被測定液の吸
収量を測定した。Comparative Example 1 An aqueous solution having a solid content of 2% has a viscosity of 8c as measured by a B-type viscometer.
A dried gelling agent was obtained in the same manner as in Example 3 except that ps hydroxypropyl cellulose (manufactured by Tokyo Chemical Industry Co., Ltd.) was used. The amount of absorption of the liquid to be measured was measured in the same manner as in Example 1.
【0029】比較例2 水240gに水酸化ナトリウム10gを溶解し、これに
エピクロルヒドリン5gとイソプロピルアルコール17
10gを添加、混合し、次いで2%固形分濃度の水溶液
のB型粘度計による粘度が1700cpsのヒドロキシ
プロピルセルロース(東京化成工業製)100gを混合
し、全重量当りヒドロキシプロピルセルロースの濃度が
4.8%の混合溶液とし、この混合溶液を温度40℃で
16時間加熱し、ゲルを生成した。しかしながら、得ら
れたゲルは、ゲル強度が弱く、その後の処理が実施不可
能であった。Comparative Example 2 10 g of sodium hydroxide was dissolved in 240 g of water, and 5 g of epichlorohydrin and 17 of isopropyl alcohol were dissolved in this solution.
3. 10 g was added and mixed, and then 100 g of hydroxypropyl cellulose (manufactured by Tokyo Kasei Kogyo Co., Ltd.) having a viscosity of 1700 cps according to a B-type viscometer of an aqueous solution having a solid content of 2% was mixed, and the concentration of hydroxypropyl cellulose was 4. An 8% mixed solution was prepared, and this mixed solution was heated at a temperature of 40 ° C. for 16 hours to form a gel. However, the gel obtained had a weak gel strength and could not be further processed.
【0030】実施例及び比較例で得られた結果を表1と
表2に示す。The results obtained in Examples and Comparative Examples are shown in Tables 1 and 2.
【0031】[0031]
【表1】 [Table 1]
【0032】[0032]
【表2】 [Table 2]
【0033】表1と表2から明らかなように、本発明に
よって得られるゲル化剤は、溶解度パラメーター値が9
以上の有機溶媒と水に対して膨潤吸収能力が極めて優れ
ており、加圧しても吸収した液を容易に放出せず、保持
力も優れている(実施例1〜7)。これに対し、2%固
形分濃度の溶液のB型粘度計による粘度が100cps
より低いセルロース誘導体から得られるゲル化剤(比較
例1)は、溶解度パラメーター値が9以上の有機溶媒と
水に対する膨潤吸収能力が劣り、ゲル化剤としては実用
に適していない。又、2%固形分濃度の溶液の粘度が1
500cpsより高いセルロース誘導体を用いると(比
較例2)、均一な溶液を得るためには低い濃度(5%未
満)とせざるを得ず、そうするとこれに架橋剤を反応さ
せても、架橋反応が進まず、ゲル強度の弱いゲルとな
り、結局ゲル化剤を得ることができなかった。As is clear from Tables 1 and 2, the gelling agent obtained by the present invention has a solubility parameter value of 9
It has extremely excellent swelling and absorption ability with respect to the above organic solvents and water, does not easily release the absorbed liquid even when pressurized, and has excellent holding power (Examples 1 to 7). On the other hand, the viscosity of the solution having a solid content of 2% by the B-type viscometer is 100 cps.
The gelling agent (Comparative Example 1) obtained from a lower cellulose derivative is inferior in swelling and absorption ability to water and an organic solvent having a solubility parameter value of 9 or more, and is not suitable for practical use as a gelling agent. Also, the viscosity of a 2% solids concentration solution is 1
When a cellulose derivative higher than 500 cps is used (Comparative Example 2), a low concentration (less than 5%) is unavoidable in order to obtain a uniform solution, and then the crosslinking reaction proceeds even if this is reacted with a crosslinking agent. First, a gel having a weak gel strength was obtained, and a gelling agent could not be finally obtained.
【0034】[0034]
【発明の効果】本発明は、溶解度パラメーター値が9以
上の広範囲な有機溶媒と水に対して膨潤吸収してゲル化
する能力を有し、加圧しても吸収液を容易に放出せず、
しかも原料がセルロース系であるため生分解性もあわせ
持つゲル化剤の製造方法を提供するという効果を奏す
る。INDUSTRIAL APPLICABILITY The present invention has the ability to swell and absorb into a wide range of organic solvents having a solubility parameter value of 9 or more and water to form a gel, and does not easily release the absorbing liquid even when pressurized,
Moreover, since the raw material is a cellulosic material, it is effective to provide a method for producing a gelling agent having biodegradability.
Claims (2)
媒又は水に溶解するセルロース誘導体と架橋剤、及び必
要に応じて反応助剤を、前記溶媒、水又は溶媒と水の混
合物に溶解又は懸濁させて混合し、次いで加熱してゲル
とし、得られたゲルを乾燥することを特徴とする有機溶
媒と水を吸収するゲル化剤の製造方法。1. A cellulose derivative and a crosslinking agent which are soluble in an organic solvent or water having a solubility parameter value of 9 or more, and a reaction aid, if necessary, are dissolved or suspended in the solvent, water or a mixture of the solvent and water. A method for producing a gelling agent for absorbing an organic solvent and water, which comprises: mixing and mixing, and then heating to form a gel, and drying the obtained gel.
ピル基を有し、且つ該誘導体の2重量%の固形分濃度に
おける水溶液の粘度が25℃でB型粘度計で測定した
時、100〜1500cpsの範囲であることを特徴と
する請求項1記載の有機溶媒と水を吸収するゲル化剤の
製造方法。2. The cellulose derivative has a hydroxypropyl group, and the viscosity of an aqueous solution of the derivative at a solid content concentration of 2% by weight is in the range of 100 to 1500 cps when measured by a B-type viscometer at 25 ° C. The method for producing a gelling agent according to claim 1, wherein the gelling agent absorbs the organic solvent and water.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP24461195A JPH0985079A (en) | 1995-09-22 | 1995-09-22 | Method for producing gelling agent that absorbs organic solvent and water |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP24461195A JPH0985079A (en) | 1995-09-22 | 1995-09-22 | Method for producing gelling agent that absorbs organic solvent and water |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| JPH0985079A true JPH0985079A (en) | 1997-03-31 |
Family
ID=17121316
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP24461195A Pending JPH0985079A (en) | 1995-09-22 | 1995-09-22 | Method for producing gelling agent that absorbs organic solvent and water |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH0985079A (en) |
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2001330188A (en) * | 2000-05-22 | 2001-11-30 | Mitsubishi Plastics Ind Ltd | Joining method of polyethylene pipe by electric fusion joint |
| JP2003515616A (en) * | 1998-10-09 | 2003-05-07 | エスシーエー・ハイジーン・プロダクツ・アーベー | Polysaccharide-based absorbent polymer material |
| JP2015232070A (en) * | 2014-06-09 | 2015-12-24 | 独立行政法人国立高等専門学校機構 | Gelling agent |
| CN117402413A (en) * | 2022-07-07 | 2024-01-16 | 上海发微医用材料有限公司 | Cellulose-based hydrogel and preparation method thereof |
-
1995
- 1995-09-22 JP JP24461195A patent/JPH0985079A/en active Pending
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2003515616A (en) * | 1998-10-09 | 2003-05-07 | エスシーエー・ハイジーン・プロダクツ・アーベー | Polysaccharide-based absorbent polymer material |
| JP2001330188A (en) * | 2000-05-22 | 2001-11-30 | Mitsubishi Plastics Ind Ltd | Joining method of polyethylene pipe by electric fusion joint |
| JP2015232070A (en) * | 2014-06-09 | 2015-12-24 | 独立行政法人国立高等専門学校機構 | Gelling agent |
| CN117402413A (en) * | 2022-07-07 | 2024-01-16 | 上海发微医用材料有限公司 | Cellulose-based hydrogel and preparation method thereof |
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