JPH11140213A - Production of porous substance - Google Patents

Production of porous substance

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Publication number
JPH11140213A
JPH11140213A JP9320610A JP32061097A JPH11140213A JP H11140213 A JPH11140213 A JP H11140213A JP 9320610 A JP9320610 A JP 9320610A JP 32061097 A JP32061097 A JP 32061097A JP H11140213 A JPH11140213 A JP H11140213A
Authority
JP
Japan
Prior art keywords
solution
aqueous
monomer
meth
porous substance
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
JP9320610A
Other languages
Japanese (ja)
Inventor
Susumu Seki
進 関
Chiaki Nagahama
千秋 長浜
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.)
Mitsubishi Rayon Co Ltd
Original Assignee
Mitsubishi Rayon 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 Mitsubishi Rayon Co Ltd filed Critical Mitsubishi Rayon Co Ltd
Priority to JP9320610A priority Critical patent/JPH11140213A/en
Publication of JPH11140213A publication Critical patent/JPH11140213A/en
Pending legal-status Critical Current

Links

Abstract

PROBLEM TO BE SOLVED: To provide a method for producing a porous substance, capable of easily obtaining the homogeneous polymer porous substance. SOLUTION: This method for producing a porous substance has characteristics comprising controlling an aqueous monomer solution containing monomers comprising a water-soluble vinylic monomer and a cross-linking agent, one or more kinds of compounds selected from the group consisting of carbonic salts and bicarbonic salts, a surfactant and a polymerization initiator to a pH of <=6.5, and subsequently bringing the aqueous monomer solution into contact with sound waves having a frequency of >=10 kHz, until the gelation of the aqueous monomer solution containing the generated carbon dioxide in a supersaturated state is finished.

Description

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

【0001】[0001]

【発明が属する技術分野】本発明は、均質な高分子多孔
質体の製造方法に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method for producing a homogeneous porous polymer.

【0002】[0002]

【従来の技術】高分子多孔質体を製造する方法として
は、ポリビニルアルコールなどの水溶性高分子水溶液に
アルギン酸ナトリウムのような一次ゲル化剤を加えた溶
液に重炭酸ソーダなどの発泡剤を混合して得られる水溶
液を、塩酸、塩化カルシウムを含む硼酸飽和水溶液中に
滴下して、塩化カルシウムで一次ゲル化剤をゲル化させ
ると同時に、塩酸で発泡剤を分解して発泡させて発泡性
一次ゲルを得、更にポリビニルアルコールを硼酸で不溶
化させる方法(特開昭63−137680号)、光硬化
性材料と光重合開始剤と、アルギン酸ナトリウムのよう
な一次ゲル化剤と界面活性剤を水に加えてなる水溶液を
混合攪拌して微細な泡を多数形成させたものを塩化カル
シウム水溶液中に滴下して一次ゲルを形成させ、更に紫
外線を照射して光硬化させて発泡体を得る方法(特開昭
63−137679号)がある。
2. Description of the Related Art As a method for producing a polymer porous material, a foaming agent such as sodium bicarbonate is mixed with a solution obtained by adding a primary gelling agent such as sodium alginate to an aqueous solution of a water-soluble polymer such as polyvinyl alcohol. The resulting aqueous solution is dropped into a saturated aqueous solution of boric acid containing hydrochloric acid and calcium chloride, and at the same time as the primary gelling agent is gelled with calcium chloride, the foaming agent is decomposed and foamed with hydrochloric acid to form the foamable primary gel. Then, a method of insolubilizing polyvinyl alcohol with boric acid (JP-A-63-137680), adding a photocurable material, a photopolymerization initiator, a primary gelling agent such as sodium alginate, and a surfactant to water. The resulting aqueous solution is mixed and stirred to form a number of fine bubbles, which is then dropped into an aqueous solution of calcium chloride to form a primary gel, which is then irradiated with ultraviolet light and cured. A method (JP 63-137679) to obtain a foam by.

【0003】[0003]

【発明が解決しようとする問題点】しかし、特開昭63
−137680号に記載した方法は、発泡剤を均一に分
散させることが困難であり、又、たとえ均一に分散でき
たとしても、滴下粒子での発泡とゲル化は粒子中の発泡
剤、ゲル化剤と液中の酸、塩化カルシウムとの接触によ
り生ずるため、まず滴下粒子表面で発泡とゲル化が生
じ、次いで液中成分の滴下粒子中への浸透に伴って内部
で発泡ゲル化が生じるので、粒子表面と内部での発泡環
境が異なってくるため、均一な発泡体を得るのが困難で
ある。又、高分子水溶液は高粘度であり、実験室レベル
では注射器先端からの滴下は容易であっても、ノズルか
らの滴下で工業的に量産するのは困難である。
[Problems to be solved by the invention]
In the method described in JP-A-137680, it is difficult to uniformly disperse the foaming agent, and even if it is possible to uniformly disperse the foaming agent, the foaming and gelling of the dropped particles is caused by the foaming agent in the particles and the gelling. Since it is caused by the contact between the agent and the acid and calcium chloride in the liquid, foaming and gelation occur first on the surface of the droplet particles, and then foaming gelation occurs internally as the components in the liquid penetrate into the droplet particles. Since the foaming environment differs between the particle surface and the inside, it is difficult to obtain a uniform foam. Further, the aqueous polymer solution has a high viscosity, and it is difficult to industrially mass-produce by dropping from a nozzle even though it is easy to drop from the tip of a syringe at the laboratory level.

【0004】特開昭63−137679号に記載の方法
は、界面活性剤を加えて攪拌しても相当広い孔径分布の
泡しか得られず、均一な泡を得るのは困難である。又、
界面活性剤量が少ないと泡が途中で消滅しやすく、界面
活性剤を比較的高濃度で使用する必要があるが、それで
も充分細かい泡を得ることが困難で、泡の大きさによる
多孔質体の孔径コントロールが困難となる問題がある。
又、孔質体を水中多に投入したとき、界面活性剤量が多
いと、それだけ多量の界面活性剤が溶出するので、より
少ない界面活性剤量で、均一で安定な、且つ孔径コント
ロールも容易となる多孔質体の製造方法を強く要請され
ていた。
In the method described in JP-A-63-137679, even if a surfactant is added and stirred, only a foam having a considerably wide pore size distribution can be obtained, and it is difficult to obtain a uniform foam. or,
If the amount of the surfactant is small, the bubbles are easily lost on the way, and it is necessary to use the surfactant at a relatively high concentration. However, it is still difficult to obtain sufficiently fine bubbles, and the porous material depends on the size of the bubbles. However, there is a problem that it is difficult to control the hole diameter.
Also, when the porous body is poured into a large amount of water, if the amount of the surfactant is large, a large amount of the surfactant is eluted, so that the amount of the surfactant is small, and the uniform, stable, and easy control of the pore size is possible. There has been a strong demand for a method for producing a porous body.

【0005】[0005]

【問題点を解決するための手段】本発明の目的は、上記
のような問題が少なく、孔径が均一で、孔径コントロー
ルが容易な高分子多孔質体を製造する方法を提供するこ
とにある。即ち、本発明の要旨は、水溶性ビニルモノマ
ーと架橋剤とからなるモノマーと、炭酸塩及び重炭酸塩
から構成される群より選ばれる1種以上と、界面活性剤
及び重合開始剤とを含有するモノマー水溶液のpHを
6.5以下とした後、発生する炭酸ガスが過飽和状態で
溶解しているモノマー水溶液のゲル化が終了する迄に、
周波数10kHz以上の音波にモノマー水溶液を接触さ
せることを特徴とする多孔質体の製造方法にある。
SUMMARY OF THE INVENTION An object of the present invention is to provide a method for producing a polymer porous body which has less of the above-mentioned problems, has a uniform pore size, and is easy to control the pore size. That is, the gist of the present invention comprises a monomer comprising a water-soluble vinyl monomer and a crosslinking agent, one or more selected from the group consisting of carbonates and bicarbonates, a surfactant and a polymerization initiator. After the pH of the aqueous monomer solution is reduced to 6.5 or less, the generated carbon dioxide gas is dissolved in a supersaturated state until the gelation of the aqueous monomer solution is completed.
A method for producing a porous body, comprising contacting an aqueous solution of a monomer with a sound wave having a frequency of 10 kHz or more.

【0006】本発明で用いられる水溶性ビニルモノマー
としては、ノニオン性ビニルモノマーでもよく、アニオ
ン性のビニルモノマー、カチオン性のビニルモノマーで
もよい。なお、以下において、(メタ)アクリルアミ
ド、(メタ)アクリレートはそれぞれ、アクリルアミド
とメタクリルアミド、アクリレートとメタクリレートの
双方を意味する。ノニオン性ビニルモノマーとしては、
(メタ)アクリルアミド、イソプロピルアクリルアミ
ド、t−ブチル(メタ)アクリルアミド、ジメチル(メ
タ)アクリルアミドなどのN−アルキル置換(メタ)ア
クリルアミド、N−メチロール(メタ)アクリルアミド
などのN−ヒドロキシアルキル置換(メタ)アクリルア
ミド、ヒドロキシエチル(メタ)アクリレート、2−ヒ
ドロキシプロピル(メタ)アクリレートなどのヒドロキ
シアルキル(メタ)アクリレート、ビニルピロリドン、
N−ビニルアセトアミドなどを例示できる。
[0006] The water-soluble vinyl monomer used in the present invention may be a nonionic vinyl monomer, an anionic vinyl monomer or a cationic vinyl monomer. In the following, (meth) acrylamide and (meth) acrylate mean both acrylamide and methacrylamide, and both acrylate and methacrylate. As nonionic vinyl monomers,
N-alkyl-substituted (meth) acrylamide such as (meth) acrylamide, isopropylacrylamide, t-butyl (meth) acrylamide, dimethyl (meth) acrylamide, and N-hydroxyalkyl-substituted (meth) acrylamide such as N-methylol (meth) acrylamide Hydroxyalkyl (meth) acrylates such as hydroxyethyl (meth) acrylate, 2-hydroxypropyl (meth) acrylate, vinylpyrrolidone,
Examples thereof include N-vinylacetamide.

【0007】アニオン性のビニルモノマーとしては、
(メタ)アクリル酸、マレイン酸などのα,β−不飽和
カルボン酸、2−アクリルアミド−2−メチルプロパン
スルホン酸などのスルホン基を側鎖に有するビニルモノ
マーを例示できる。
The anionic vinyl monomers include:
Examples thereof include vinyl monomers having a side chain having a sulfone group such as α, β-unsaturated carboxylic acid such as (meth) acrylic acid and maleic acid, and 2-acrylamido-2-methylpropanesulfonic acid.

【0008】カチオン性のビニルモノマーとしては、例
えば、ジメチルアミノエチル(メタ)アクリレート、ジ
エチルアミノエチル(メタ)アクリレートなどのジアル
キルアミノアルキル(メタ)アクリレートならびにこれ
らの4級アンモニウム塩、ジメチルアミノエチル(メ
タ)アクリルアミド、ジエチルアミノエチル(メタ)ア
クリルアミド、ジメチルアミノプロピル(メタ)アクリ
ルアミドなどのジアルキルアミノアルキル(メタ)アク
リルアミドならびにこれらの4級アンモニウム塩、ビニ
ルピリジン、ビニルイミダゾールなどを挙げることがで
きる。
Examples of the cationic vinyl monomer include dialkylaminoalkyl (meth) acrylates such as dimethylaminoethyl (meth) acrylate and diethylaminoethyl (meth) acrylate, and quaternary ammonium salts thereof, and dimethylaminoethyl (meth) acrylate. Examples thereof include dialkylaminoalkyl (meth) acrylamides such as acrylamide, diethylaminoethyl (meth) acrylamide and dimethylaminopropyl (meth) acrylamide, and quaternary ammonium salts thereof, vinylpyridine and vinylimidazole.

【0009】本発明で用いる架橋剤としては、メチレン
ビスアクリルアミド、ジビニルベンゼン、ポリエチレン
グリコールジ(メタ)アクリレート、ポリプロピレング
リコールジ(メタ)アクリレートなどを例示できる。
Examples of the crosslinking agent used in the present invention include methylene bisacrylamide, divinylbenzene, polyethylene glycol di (meth) acrylate, and polypropylene glycol di (meth) acrylate.

【0010】本発明で用いる開始剤としては、ベンゾイ
ルパーオキサイド、過硫酸塩などの過酸化物系開始剤、
アゾビスイソブチロニトリル、アゾビスバレロニトリ
ル、2,2’−アゾビス−(2−アミジノプロパン)二
塩酸塩などのアゾ系開始剤、過硫酸塩などの過酸化物と
亜硫酸水素ナトリウムなどの還元剤の組合せのようなレ
ドックス触媒など、通常のビニル重合に用いられる開始
剤であればどのようなものも用いることができるが、レ
ドックス触媒を用いることが好ましい。レドックス触媒
を用いる場合は、過酸化物と還元剤を別個の水溶液とし
て準備し、重合直前に混合するのが好ましい。本発明で
用いるモノマー水溶液及び重合に供する各種水溶液は必
要に応じて窒素ガスなどの不活性ガスで脱酸素してから
使用する。
The initiator used in the present invention includes peroxide initiators such as benzoyl peroxide and persulfate;
Azo-based initiators such as azobisisobutyronitrile, azobisvaleronitrile, 2,2'-azobis- (2-amidinopropane) dihydrochloride, peroxides such as persulfates and reduction of sodium bisulfite and the like Any initiator can be used as long as it is used in ordinary vinyl polymerization, such as a redox catalyst such as a combination of agents, but it is preferable to use a redox catalyst. When a redox catalyst is used, it is preferable to prepare the peroxide and the reducing agent as separate aqueous solutions and mix them immediately before polymerization. The aqueous monomer solution and various aqueous solutions to be used in the polymerization used in the present invention are used after being deoxygenated with an inert gas such as nitrogen gas, if necessary.

【0011】本発明で用いる炭酸塩及び重炭酸塩から構
成される群より選ばれる1種以上(以下、(重)炭酸塩
という)としては、炭酸水素ナトリウム、炭酸水素アン
モニウム、炭酸ナトリウムなどを例示できる。
The one or more kinds (hereinafter, referred to as (bi) carbonate) selected from the group consisting of carbonate and bicarbonate used in the present invention include sodium bicarbonate, ammonium bicarbonate, sodium carbonate and the like. it can.

【0012】本発明のモノマー水溶液のモノマー濃度は
5wt%以上であることが好ましく、10wt%以上である
ことがより好ましい。開始剤濃度は充分なゲル化が達成
できる濃度であればよい。(重)炭酸塩濃度は0.1〜
2wt%であることが好ましく、0.5〜1wt%であるこ
とがより好ましい。
[0012] The monomer concentration of the aqueous monomer solution of the present invention is preferably at least 5 wt%, more preferably at least 10 wt%. The initiator concentration may be any concentration at which sufficient gelation can be achieved. (Bi) carbonate concentration is 0.1 ~
It is preferably 2 wt%, more preferably 0.5 to 1 wt%.

【0013】(重)炭酸塩を水溶液あたり1wt%程度含
有する上記モノマー水溶液のpHを6〜6.5程度に下
げただけでは発生した炭酸ガスは過飽和状態で溶解した
ままで、直ちには発泡しない。そこで、この水溶液が重
合によりゲル化をする前に周波数10kHz以上の音波
に接触させる。音波への接触は、重合開始から10分以
内であることが好ましく、5分以内であることがより好
ましく、3分以内であることが更に好ましい。
If the pH of the aqueous monomer solution containing (bi) carbonate in an amount of about 1% by weight of the aqueous solution is reduced only to about 6 to 6.5, the generated carbon dioxide gas remains dissolved in a supersaturated state and does not foam immediately. . Therefore, this aqueous solution is brought into contact with a sound wave having a frequency of 10 kHz or more before gelling by polymerization. Contact with a sound wave is preferably within 10 minutes, more preferably within 5 minutes, even more preferably within 3 minutes from the start of polymerization.

【0014】本発明で用いる界面活性剤としては、脂肪
族石鹸、アルキルエーテルカルボン酸塩等のカルボン酸
塩、アルキルベンゼンスルホン酸等のスルホン酸塩、高
級アルコール硫酸エステル塩、アルキルエーテルリン酸
エステル塩等の陰イオン界面活性剤、アルキル及びアル
キルアリルポリオキシエチレンエーテル、ソルビタンエ
ステルのポリオキシエチレンエーテル、ポリエチレング
リコール脂肪族エステル、ポリオキシエチレンアルキル
アミン等のノニオン界面活性剤を用いることができる。
本発明の場合は使用する界面活性剤の量は0.01〜
0.5wt%程度と、同一の界面活性剤を加えて攪拌混合
して発泡させる場合に比べて半分以下と少なくてすみ、
従って、それだけ環境に与える悪影響も少なくてすむ。
The surfactants used in the present invention include aliphatic soaps, carboxylate salts such as alkyl ether carboxylate salts, sulfonates such as alkylbenzene sulfonic acid, higher alcohol sulfates, alkyl ether phosphates and the like. And nonionic surfactants such as alkyl and alkyl allyl polyoxyethylene ethers, polyoxyethylene ethers of sorbitan esters, polyethylene glycol aliphatic esters, and polyoxyethylene alkylamines.
In the case of the present invention, the amount of the surfactant used is 0.01 to
0.5% by weight, less than half of the case where the same surfactant is added, stirred, mixed and foamed,
Therefore, the adverse effect on the environment can be reduced accordingly.

【0015】炭酸ガス発生のためのpH調節は、pHを
下げすぎると重合に支障を与える場合もあるため、pH
は5〜7であることが好ましく、6〜6.5であること
がより好ましい。pHの調節には硫酸、塩酸、リン酸、
酢酸、リン酸二水素ナトリウムなど種々の酸を用いるこ
とができる。又、必要に応じてpH緩衝液も添加するこ
とが出来る。
In the pH adjustment for generating carbon dioxide, if the pH is lowered too much, polymerization may be hindered.
Is preferably 5 to 7, and more preferably 6 to 6.5. Sulfuric acid, hydrochloric acid, phosphoric acid,
Various acids such as acetic acid and sodium dihydrogen phosphate can be used. Also, a pH buffer can be added as needed.

【0016】音波に接触させる時間はモノマー水溶液が
重合によりゲル化するまでの間であれば特に制限はない
が、10分以内でもよく、好ましくは5分以内、更に好
ましくは3分以内でよい。音波の強さは、モノマー水溶
液全体が発泡する程度であればよい。孔径のコントロー
ルは、界面活性剤量、音波の周波数、出力を調節するこ
とによって行うことができる。以上の条件を組み合わせ
ることによって、より均一な孔径の気泡の生成が可能と
なり、気泡を含むモノマー溶液を直ちに重合することに
より、音波と接触させない場合に比べて、均一な気泡を
有する多孔質体が得られる。
The time of contact with the sound wave is not particularly limited as long as the monomer aqueous solution is gelled by polymerization, but may be within 10 minutes, preferably within 5 minutes, more preferably within 3 minutes. The intensity of the sound wave may be such that the entire aqueous monomer solution foams. The pore size can be controlled by adjusting the amount of the surfactant, the frequency of the sound wave, and the output. By combining the above conditions, it is possible to generate bubbles with a more uniform pore size, and by immediately polymerizing the monomer solution containing the bubbles, a porous body having uniform bubbles can be obtained, as compared to a case where it is not brought into contact with a sound wave. can get.

【0017】[0017]

【実施例】以下に実施例を用いて本発明を更に詳しく説
明するが、本発明はこれら実施例により限定されるもの
ではない。
The present invention will be described in more detail with reference to the following examples, but the present invention is not limited to these examples.

【0018】実施例1 50%アクリルアミド水溶液798.4gと、メチレン
ビスアクリルアミド0.2gを800gのイオン交換水
に溶解し、酸を用いてpH4.5に調整してから、イオ
ン交換水を加えて全量を1776gとする。(これをA
液という) 一方、炭酸水素ナトリウム20gを176gのイオン交
換水に溶解した。(これをB液という) A液、B液ともに窒素ガスを吹き込んで窒素置換をした
後、A液に界面活性剤ポリオキシエチレンソルビタンモ
ノオレエート20g、及び過硫酸カリウム1%水溶液4
mlを加えた。一方、B液には亜硫酸水素ナトリウム1
%水溶液4mlを加えた。A液とB液を9:1の比率に
なるよう、スタティックミキサーを用いて混合し、直ち
に47kHz、185Wの超音波発信器を備え、内部に
水を満たした水槽中においた容器にこの混合モノマー水
溶液を入れ、47kHzの音波に60秒間接触させてモ
ノマー水溶液を発泡させた後、この発泡水溶液を室温の
重合容器に入れて静置した。重合容器中の発泡水溶液は
発熱を伴いながら約2分後にゲル化が終了し、約20分
後には重合が終了した。A液とB液を混合した直後の溶
液のpHは6.5であり、重合したゲル中には0.1〜
0.5mm程度の孔径がそろった気泡が多数含まれてい
た。
Example 1 798.4 g of a 50% aqueous acrylamide solution and 0.2 g of methylenebisacrylamide were dissolved in 800 g of ion-exchanged water, adjusted to pH 4.5 with an acid, and added with ion-exchanged water. The total amount is 1776 g. (This is A
On the other hand, 20 g of sodium hydrogen carbonate was dissolved in 176 g of ion-exchanged water. (This is referred to as solution B) After nitrogen gas was blown into both solution A and solution B to replace nitrogen, 20 g of surfactant polyoxyethylene sorbitan monooleate and 1% aqueous solution of potassium persulfate 4 were added to solution A.
ml was added. On the other hand, solution B contains sodium bisulfite 1
4 ml of a 1% aqueous solution were added. Solution A and solution B were mixed using a static mixer so as to have a ratio of 9: 1. The aqueous solution was charged and contacted with a 47 kHz sound wave for 60 seconds to foam the monomer aqueous solution, and then the foamed aqueous solution was placed in a polymerization container at room temperature and allowed to stand. The gelation of the aqueous foaming solution in the polymerization vessel was completed after about 2 minutes while generating heat, and the polymerization was completed after about 20 minutes. The pH of the solution immediately after mixing the solution A and the solution B is 6.5, and 0.1 to
Many bubbles having a pore size of about 0.5 mm were included.

【0019】比較例 A液とB液の調製、及びA液とB液を9:1の比率でス
タティックミキサーを用いて混合するまでは実施例1と
同様に実施した。こうして得られたモノマー水溶液を1
0kHz以上の音波に接触させることなく室温の重合容
器に充填した。モノマー水溶液は約3分後に気泡を殆ど
含むことなくゲル化し、更に重合が進行してゲルの温度
が上昇すると炭酸ガスがゲルから発生し、最終的には5
〜10mm程度の大きな孔が疎らに空いたゲルが得られ
た。
Comparative Example The same procedure as in Example 1 was carried out until the preparation of the liquid A and the liquid B and the mixing of the liquid A and the liquid B at a ratio of 9: 1 using a static mixer. The aqueous monomer solution thus obtained was
The reactor was filled in a polymerization container at room temperature without contacting with a sound wave of 0 kHz or more. After about 3 minutes, the aqueous monomer solution gels with almost no air bubbles, and when the polymerization proceeds and the temperature of the gel rises, carbon dioxide gas is generated from the gel.
A gel in which large holes of about 10 to 10 mm were sparsely obtained was obtained.

【0020】[0020]

【発明の効果】本発明の方法によれば、孔径が均一で、
孔径コントロールが容易な高分子多孔質体を製造でき
る。
According to the method of the present invention, the pore size is uniform,
It is possible to produce a polymer porous body whose pore size can be easily controlled.

───────────────────────────────────────────────────── フロントページの続き (51)Int.Cl.6 識別記号 FI // C08L 33:04 77:00 ──────────────────────────────────────────────────の Continued on the front page (51) Int.Cl. 6 Identification code FI // C08L 33:04 77:00

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】水溶性ビニルモノマーと架橋剤とからなる
モノマーと、炭酸塩及び重炭酸塩から構成される群より
選ばれる1種以上と、界面活性剤及び重合開始剤とを含
有するモノマー水溶液のpHを6.5以下とした後、発
生する炭酸ガスが過飽和状態で溶解しているモノマー水
溶液のゲル化が終了する迄に、周波数10kHz以上の
音波にモノマー水溶液を接触させることを特徴とする多
孔質体の製造方法。
1. An aqueous monomer solution containing a monomer comprising a water-soluble vinyl monomer and a crosslinking agent, at least one selected from the group consisting of carbonates and bicarbonates, a surfactant and a polymerization initiator. After the pH of the aqueous solution is adjusted to 6.5 or less, the monomer aqueous solution is contacted with a sound wave having a frequency of 10 kHz or more before the gelation of the aqueous monomer solution in which the generated carbon dioxide gas is dissolved in a supersaturated state is completed. A method for producing a porous body.
JP9320610A 1997-11-07 1997-11-07 Production of porous substance Pending JPH11140213A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP9320610A JPH11140213A (en) 1997-11-07 1997-11-07 Production of porous substance

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP9320610A JPH11140213A (en) 1997-11-07 1997-11-07 Production of porous substance

Publications (1)

Publication Number Publication Date
JPH11140213A true JPH11140213A (en) 1999-05-25

Family

ID=18123335

Family Applications (1)

Application Number Title Priority Date Filing Date
JP9320610A Pending JPH11140213A (en) 1997-11-07 1997-11-07 Production of porous substance

Country Status (1)

Country Link
JP (1) JPH11140213A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR20190039871A (en) * 2017-10-06 2019-04-16 에보니크 데구사 게엠베하 Absorbent polymeric foam for shoe insoles

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR20190039871A (en) * 2017-10-06 2019-04-16 에보니크 데구사 게엠베하 Absorbent polymeric foam for shoe insoles
CN109627393A (en) * 2017-10-06 2019-04-16 赢创德固赛有限公司 Absorbable polymer foam for inner sole
JP2019069148A (en) * 2017-10-06 2019-05-09 エボニック デグサ ゲーエムベーハーEvonik Degussa GmbH Absorbent polymeric foam for shoe insoles
EP3620075A1 (en) * 2017-10-06 2020-03-11 Evonik Operations GmbH Absorbent polymeric foam for shoe insoles
EP3620075B1 (en) 2017-10-06 2021-07-07 Evonik Operations GmbH Absorbent polymeric foam for shoe insoles
US11078343B2 (en) 2017-10-06 2021-08-03 Evonik Operations Gmbh Absorbent polymeric foam for shoe insoles

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