JPS5980459A - Water-absorbing powdery resin composition - Google Patents

Water-absorbing powdery resin composition

Info

Publication number
JPS5980459A
JPS5980459A JP19151782A JP19151782A JPS5980459A JP S5980459 A JPS5980459 A JP S5980459A JP 19151782 A JP19151782 A JP 19151782A JP 19151782 A JP19151782 A JP 19151782A JP S5980459 A JPS5980459 A JP S5980459A
Authority
JP
Japan
Prior art keywords
water
powder
hydrated
absorbing
weight
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
JP19151782A
Other languages
Japanese (ja)
Inventor
Muneharu Makita
蒔田 宗治
Katsuzou Tanioku
谷奥 勝三
Takayasu Touda
當田 隆康
Toshiyuki Imai
敏之 今井
Nobuyuki Oshima
大島 信幸
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.)
Arakawa Rinsan Kagaku Kogyo KK
Arakawa Chemical Industries Ltd
Original Assignee
Arakawa Rinsan Kagaku Kogyo KK
Arakawa 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 Arakawa Rinsan Kagaku Kogyo KK, Arakawa Chemical Industries Ltd filed Critical Arakawa Rinsan Kagaku Kogyo KK
Priority to JP19151782A priority Critical patent/JPS5980459A/en
Publication of JPS5980459A publication Critical patent/JPS5980459A/en
Pending legal-status Critical Current

Links

Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J20/00Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof
    • B01J20/22Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising organic material
    • B01J20/26Synthetic macromolecular compounds

Abstract

PURPOSE:To prepare a composition resistant to blocking caused by moisture absorption, capable of keeping the powdery form even after being left for a long period, and keeping the water-absorptivity, by adding the powder of a compound selected from hydrated silicon dioxide, hydrated aluminum oxide, hydrated titanium oxide, etc. to a water-absorbing resin powder. CONSTITUTION:Dry powder of a water-absorbing resin is compounded with the powder of a material selected from hydrated silicon dioxide, hydrated aluminum oxide, hydrated titanium oxide, their anhydride, and inorganic substance containing the above materials as main component. The water-absorbing resin is the one capable of absorbing >=about 10 times weight of deionized water based on the own weight of the resin, preferably crosslinked polyacrylic acid salt. The particle size of the inorganic powder is <=10mum, and the amount of the inorganic powder is 0.01-10wt%, preferably 0.1-5wt%, based on the resin powder.

Description

【発明の詳細な説明】 本発明は吸水性樹脂粉末組成物、詳しくは吸水性樹脂特
有の吸湿性(ブロッキング性)を改善した新しい吸水性
樹脂粉末組成物に関する。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a water-absorbing resin powder composition, and more particularly to a new water-absorbing resin powder composition that has improved hygroscopicity (blocking property) peculiar to water-absorbing resins.

吸水性樹脂は近年、生理用品、衛生用品、保水剤、脱水
剤、汚泥凝固剤、増粘剤、結露防止剤さらに各種薬品の
リリースコントロール剤などの種々の用途に利用されて
いる。
In recent years, water-absorbing resins have been used for a variety of purposes, including sanitary products, sanitary products, water retention agents, dehydration agents, sludge coagulants, thickeners, anti-condensation agents, and release control agents for various chemicals.

これら吸水性樹脂としては、澱粉−アクリルニトリルグ
ラフト重合体の加水分解物、カルボキシメチルセルロー
ス、ポリアクリル酸塩架橋物、その他ポリビニルアルコ
ール系、ポリエチレンオキサイド系、ポリアクリロニト
リル系などが知られて#す、之等の中で、吸水能および
品質安定性ともに優れた樹脂として、ポリアクリル酸塩
架橋物が有望視されている。
Known examples of these water-absorbing resins include hydrolysates of starch-acrylonitrile graft polymers, carboxymethyl cellulose, polyacrylate crosslinked products, and other polyvinyl alcohol-based, polyethylene oxide-based, and polyacrylonitrile-based resins. Among these, crosslinked polyacrylates are considered promising as resins with excellent water absorption ability and quality stability.

本発明者らは兼てより上記吸水性樹脂殊にポリアクリル
酸塩架橋物につき種々研究を重ね、その過程をとおいて
アクリル酸カリウムと水混和性ポリビニル単量体とを含
有し、2等単量体の濃度が55〜80重量%の範囲にあ
る加温水溶液に、重合反応開始剤を添加して外部加熱を
行なうことなく重合反応を行なわせると共に水分を気化
させる吸水性樹脂乾燥固体の製造方法(特願昭56−1
71559号)及びアクリル酸アルカリ金属塩、水混和
性ポリビニル単量体、沸点40〜1506Cの有機溶剤
及び水を含有し、2等単量体の濃度が55〜80重量%
の範囲にある加温水性液に、重合反応開始剤を添加して
外部加熱を行なうことなく重合反応を行なわせると共に
水分を気化させる乾燥した吸水性樹脂の製造方法(特願
昭57−128266号)を確立した。
The present inventors have repeatedly conducted various studies on the above-mentioned water-absorbing resins, especially cross-linked polyacrylates, and through the process, they have developed a compound containing potassium acrylate and a water-miscible polyvinyl monomer, Production of a dry solid water-absorbing resin by adding a polymerization reaction initiator to a heated aqueous solution having a polymer concentration in the range of 55 to 80% by weight, carrying out a polymerization reaction without external heating, and vaporizing water. Method (Patent Application 1982-1)
71559) and an alkali metal salt of acrylic acid, a water-miscible polyvinyl monomer, an organic solvent with a boiling point of 40 to 1506C, and water, and the concentration of secondary monomers is 55 to 80% by weight.
A method for producing a dry water-absorbent resin in which a polymerization reaction initiator is added to a heated aqueous liquid in the range of ) was established.

之等の方法によれば、極めて短時間内に充分に重合反応
が進行し、しかもこの重合反応の反応熱によって、反応
系内より水分が迅速に気化し、これによって引き続き何
らの乾燥工程を要することなく直接に所望の低含水率の
吸水性樹脂乾燥固体を収得でき、得られる固体は容易に
粉砕でき、所望の用途に好適な粉末とすることができ、
また外部加熱及び乾燥工程の採用によるオーバーヒート
等に起因する架橋度の不均一化やこれによる吸水能の低
下等の詔それも全くなく、非常に良好な品質を具備し、
更に後者の方法では、初期吸水速度のより改善された樹
脂固体が収得される。
According to these methods, the polymerization reaction proceeds sufficiently within an extremely short period of time, and the reaction heat of this polymerization reaction quickly evaporates water from the reaction system, which necessitates the need for any subsequent drying step. The desired dry water-absorbing resin solid with a low water content can be obtained directly without any process, and the obtained solid can be easily pulverized and made into a powder suitable for the desired use.
In addition, there is no unevenness in the degree of crosslinking due to overheating due to external heating and drying processes, and there is no decrease in water absorption capacity due to this, and the product has very good quality.
Moreover, in the latter method, resin solids with improved initial water absorption rates are obtained.

しかして本発明者らは引き続き、鋭意研究を重ねた結果
、上記各種吸水性樹脂は、その種類や製法により多少の
相違はあるが、総じてその本来の吸水能に依存して、吸
湿性があり、比較的速やかに吸湿してブロッキングを起
し、粉末形態での使用を困難ならしめたり、その取扱い
が困難となる欠点を有することを認めた。
However, as a result of continued intensive research, the inventors of the present invention found that although there are some differences depending on the type and manufacturing method, the various water-absorbing resins generally have hygroscopic properties depending on their original water-absorbing ability. It has been recognized that it has the disadvantage that it absorbs moisture relatively quickly and causes blocking, making it difficult to use in powder form and making it difficult to handle.

本発明はこの吸水性樹脂特有の欠点である吸湿性殊に吸
湿によるブロッキング性を解消し、長期間放置後も製造
直後の粉末形態を保持し、しかも吸水性樹脂本来の吸水
能は全く低下させない新しい吸水性樹脂粉末組成物を提
供するものである。
The present invention eliminates the hygroscopic property, especially the blocking property due to moisture absorption, which is a drawback peculiar to this water-absorbing resin, and maintains the powder form immediately after production even after being left for a long time, and does not reduce the water-absorbing ability of the water-absorbing resin at all. A new water absorbent resin powder composition is provided.

即ち本発明は吸水性樹脂乾燥粉末に、含水二酸化ケイ素
、含水酸化アルミニウム、含水酸化チタン、之等の無水
物並びに之等を主成分として含有する無機物質から選ば
れた少なくとも1種の粉末を混合したことを特徴とする
吸水性樹脂粉末組成物に係る。
That is, the present invention mixes a water-absorbing resin dry powder with at least one kind of powder selected from anhydrides such as hydrated silicon dioxide, hydrated aluminum oxide, hydrated titanium oxide, and inorganic substances containing these as main components. The present invention relates to a water-absorbing resin powder composition characterized by the following.

本発明の吸水性樹脂粉末組成物は、上記特定の無機質粉
末を配合したことに基づいて吸水性樹脂8一 本来の吸水能は全く低下させることなく、その吸湿性(
ブロッキング性)が顕著に改善されている。
The water-absorbing resin powder composition of the present invention is characterized by the fact that the water-absorbing resin 8 does not reduce its original water-absorbing ability at all, and its hygroscopic property (
blocking performance) has been significantly improved.

即ち該組成物はこれを放置するもブロッキングすること
がなく、極めて優れた粉体流動性を具備し、その取扱い
性も良好であり、従来吸水性樹脂が用いられている分野
において非常に有効に利用できる。
In other words, the composition does not block even when left alone, has extremely excellent powder fluidity, and is easy to handle, making it very effective in fields where water-absorbing resins have been used. Available.

本発明組成物に詔いては吸水性樹脂として従来公知の各
種の吸水性樹脂をいずれも使用できるへが、自重の約1
0倍以上の脱イオン水を吸収する能力を有する樹脂が好
★しい。その代表例としては、澱粉−アクリルニトリル
グラフト重合体の加水分解物、カルボキシメ・チルセル
ロース、ポリアクリル酸塩架橋物、ポリビニルアルコー
ル系樹脂、ポリエチレンオキサイド系樹脂、ポリアクリ
ロニトリル系樹脂等を例示できる。之等のうちでポリア
クリル酸塩架橋物は好ましく、特に本発明者らが先に開
発し、特許出願した前記方法により得ら=4− れるポリアクリル酸塩架橋物は最適である。
In the composition of the present invention, any of the various water-absorbing resins conventionally known can be used as the water-absorbing resin;
Resins that have the ability to absorb 0 times more deionized water are preferred. Typical examples thereof include hydrolysates of starch-acrylonitrile graft polymers, carboxymethyl cellulose, crosslinked polyacrylates, polyvinyl alcohol resins, polyethylene oxide resins, polyacrylonitrile resins, and the like. Among these, crosslinked polyacrylates are preferred, and in particular, crosslinked polyacrylates obtained by the method previously developed and patented by the present inventors are most suitable.

以下この特に好ましいポリアクリル酸塩架橋物の製法に
つき詳述する。
The method for producing this particularly preferred crosslinked polyacrylate product will be described in detail below.

即ち第一の方法(特願昭56−171559号)におい
ては、まずアクリル酸カリウムと水混和性乃至水溶性ジ
ビニル系化合物とを含有し、2等単量体濃度が55〜8
0重量%の範囲にある混合単量体の加温水溶液を調製す
る。該水溶液は通常水中にアクリル酸、その中和剤であ
る水酸化カリウム及び上記ジビニル系化合物を上記単量
体濃度となる量で投入することにより容易に調製され、
この際充分な溶解を行なわせるために若干加熱操作を採
用することもできる。上記中和剤としての水酸化カリウ
ムは、通常アクリル酸を100モル%中和するのに充分
な量で用いられるのが望ましいが、特に100%中和す
る量とする必要はなく、約70%以上が中和される量と
すればよく、従って調製される混合単量体水溶液中には
遊離のアクリル酸が約30%までの量で含まれていても
よい。上記において用いられる水混和性乃至水溶性ジビ
ニル系化合物は、これを添加して調製される混合単量体
水溶液中に均一に溶解乃至分散される水混和性乃至水溶
性を有する必要がある。かかるジビニル系化合物として
は、例えばN、N−メチレンビスアクリルアミド、N、
N−メチレンビスメタクリルアミドなどのビスアクリル
アミド類;下記一般式(I)で表わされるジアクリル(
又はメタクリル)酸エステル類;下記一般式〇で表わさ
れるジアクリルアミド類等の通常の架橋剤を例示でき、
これらのうちで特にN、N−メチレンビスアクリルアミ
ド、N。
That is, in the first method (Japanese Patent Application No. 56-171559), potassium acrylate and a water-miscible or water-soluble divinyl compound are first contained, and the secondary monomer concentration is 55 to 8.
A warmed aqueous solution of mixed monomers in the range of 0% by weight is prepared. The aqueous solution is usually easily prepared by adding acrylic acid, its neutralizing agent potassium hydroxide, and the divinyl compound in amounts to achieve the monomer concentration described above, into water.
At this time, a slight heating operation may be employed to ensure sufficient dissolution. Potassium hydroxide as the neutralizing agent is preferably used in an amount sufficient to neutralize 100% by mole of acrylic acid, but it is not necessary to use the amount to neutralize 100%, but about 70%. The above amount may be neutralized, and therefore, the prepared mixed monomer aqueous solution may contain free acrylic acid in an amount of up to about 30%. The water-miscible or water-soluble divinyl compound used above needs to have water-miscibility or water-solubility such that it can be uniformly dissolved or dispersed in the mixed monomer aqueous solution prepared by adding it. Examples of such divinyl compounds include N,N-methylenebisacrylamide, N,
Bisacrylamides such as N-methylenebismethacrylamide; diacrylamide represented by the following general formula (I) (
or methacrylic) acid esters; common crosslinking agents such as diacrylamides represented by the following general formula 〇 can be exemplified;
Among these, especially N,N-methylenebisacrylamide, N.

N−メチレンビスメタクリルアミド等のビスアクリルア
ミド類は好適である。
Bisacrylamides such as N-methylenebismethacrylamide are preferred.

o=c−o−x−o−c=。o=c-o-x-o-c=.

(式中Xはエチレン、プロピレン、2−ヒドロキシプロ
ピレン、 CH9CH8 基を示し、n及びmは5〜40の整数を示す。)該一般
式(I)の化合物は、例えばエチレングリコール、プロ
ピレングリコール、グリセリン、ポリエチレングリコー
ル、ポリプロピレングリコールなどのポリオール類とア
クリル酸又はメタクリル酸との反応により得られる。
(In the formula, X represents ethylene, propylene, 2-hydroxypropylene, CH9CH8 group, and n and m represent integers of 5 to 40.) The compound of the general formula (I) is, for example, ethylene glycol, propylene glycol, glycerin , polyethylene glycol, polypropylene glycol, and other polyols and acrylic acid or methacrylic acid.

0=C−NH+CH2CHgNH+1C=0(式中lは
2又は3を示す。) 該一般式〇の化合物は、例えばジエチレントリアミン、
トリエチレンテトラミンなどのポリアルキレンポリアミ
ン類とアクリル酸との反応により得られる。
0=C-NH+CH2CHgNH+1C=0 (in the formula, l represents 2 or 3) The compound of the general formula 〇 is, for example, diethylenetriamine,
It is obtained by the reaction of polyalkylene polyamines such as triethylenetetramine and acrylic acid.

上記ジビニル系化合物は、通常調製される混合単量体水
溶液中のアクリル酸カリウム塩又は場合によってはこれ
と遊離のアクリル酸との合計重量7− の約0.001〜0.3重量%、好ましくは0.005
〜0.1重量%の範囲で有利に用いられ、これにより目
的とする吸水能に優れたポリアクリル酸塩架橋物の乾燥
固体を収得できる。
The divinyl compound is preferably about 0.001 to 0.3% by weight of the total weight of potassium acrylate salt or, in some cases, this and free acrylic acid in the commonly prepared mixed monomer aqueous solution. is 0.005
It is advantageously used in a range of 0.1% by weight, thereby making it possible to obtain the desired dry solid crosslinked polyacrylate product having excellent water absorption ability.

次いで上記方法では上記により調製された混合単量体の
水性液を予め加温後、これに重合反応開始剤を添加して
重合反応(及び架橋反応)を開始させる。ここで加温条
件は、重合反応開始剤の添加により重合反応が開始され
ることを前提として特に制限はないが、通常約50〜8
5°C1好ましくは約60〜75°C程度とすればよい
。また重合反応開始剤としては、従来よりポリアクリル
酸塩の製造に利用されることの知られている各種のもの
をいずれも使用できる。その具体例としては例えばアル
カリ金属の亜硫酸塩もしくは重亜硫酸塩、亜硫酸アンモ
ニウム、重亜硫酸アンモニウム等の還元剤と、アルカリ
金属の過硫酸塩、過硫酸アンモニウム等の開始剤との組
み合せよりなるレドッ8− クス系開始剤やアゾビスイソブチロニトリル、4−t−
ブチルアゾ−4−シアノ吉草酸、4,4−アゾビス(4
−シアノ吉草酸)、2.2−アゾビス(2−アミジノプ
ロパン)塩酸塩等の所謂アゾ系開始剤等或は之等の二種
以上の組み合せを適宜選択使用できる。かかる重合開始
剤の使用量は、通常のそれと特に異ならず、通常固型分
重量が単量体とするアクリル酸塩(又はこれとアクリル
酸)及びポリビニル単量体の合計重量の0,1〜10重
量%重量%上り好ましくは0.5〜5重量%程度とす°
るのがよい。また上記重合反応開始剤の種類及び使用量
によっては、これと共にイソプロピルアルコールやアル
キルメルカプタン等の通常の連鎖移動剤を併用して、生
成するポリアクリル酸塩の分子量を調節することができ
る。
Next, in the above method, the aqueous solution of the mixed monomers prepared above is heated in advance, and then a polymerization reaction initiator is added thereto to start the polymerization reaction (and crosslinking reaction). Here, the heating conditions are not particularly limited on the premise that the polymerization reaction is initiated by the addition of a polymerization initiator, but are usually about 50 to 80%
5°C1, preferably about 60 to 75°C. Furthermore, as the polymerization reaction initiator, any of the various types known to be used in the production of polyacrylates can be used. A specific example thereof is a redox consisting of a combination of a reducing agent such as an alkali metal sulfite or bisulfite, ammonium sulfite, or ammonium bisulfite, and an initiator such as an alkali metal persulfate or ammonium persulfate. System initiator, azobisisobutyronitrile, 4-t-
Butylazo-4-cyanovaleric acid, 4,4-azobis(4
-cyanovaleric acid), 2,2-azobis(2-amidinopropane) hydrochloride, etc., or a combination of two or more of them can be appropriately selected and used. The amount of the polymerization initiator to be used is not particularly different from the usual one, and usually the solid weight is 0.1 to 100% of the total weight of the acrylate (or acrylic acid and acrylic acid) as monomers and the polyvinyl monomer. 10% by weight, preferably about 0.5 to 5% by weight
It is better to Further, depending on the type and amount of the polymerization reaction initiator used, a common chain transfer agent such as isopropyl alcohol or alkyl mercaptan may be used together with the polymerization reaction initiator to control the molecular weight of the polyacrylate to be produced.

上記重合反応開始剤の添加による重合反応及び水分の気
化は、より有利には、混合単量体加温水溶液に重合反応
開始剤又はその水溶液の所定量を添加混合し、この混合
液を移動するベルト上に流下延展させることにより実施
される。重合反応開始剤を水溶液の形態で用いる場合、
得られる混合液中のアクリル酸塩濃度が前述した55〜
80重量%の範囲を下回らないようにしなければならな
い。また上記ベルト上への混合液の流下に当っては、該
ベルトの混合液流下部分に更に重合反応開始剤を配置し
ておくこともでき゛る。
The polymerization reaction and vaporization of water by addition of the polymerization initiator are more advantageously carried out by adding and mixing a predetermined amount of the polymerization initiator or its aqueous solution to a heated aqueous solution of mixed monomers, and then transferring this mixed solution. It is carried out by flowing down and spreading on a belt. When using the polymerization reaction initiator in the form of an aqueous solution,
The acrylate concentration in the resulting mixed solution is 55~
It must not fall below a range of 80% by weight. Further, when the mixed liquid flows down onto the belt, a polymerization reaction initiator may be further placed in the downstream part of the belt.

上記混合単量体加温水溶液への重合反応開始剤の添加混
合によれば、混合後極めて速やかに重合反応が開始され
、短時間に、通常約30秒から1゜分程度で反応は完結
する。しかもこの反応は発熱反応であり、反応系はこの
重合熱により速やかに約100〜130°C程度に上昇
し、これによって系内の水分は、外部より他に何ら加熱
等を行なわずとも急速に気化蒸発し、所望の低含水率の
重合体(乾燥固体)が収得される。得られる重合体の含
水率は、反応条件等により若干具なるが通常約15%以
下、より好ましくは約10%以下であり、これは引き続
き何らの乾燥工程を要することなく、単に常法番と従い
粉砕等を行なうのみで所望の粉末製品とすることができ
る。
According to the addition and mixing of the polymerization reaction initiator to the heated aqueous solution of mixed monomers, the polymerization reaction starts extremely quickly after mixing, and the reaction is completed in a short time, usually about 30 seconds to 1 minute. . Moreover, this reaction is an exothermic reaction, and the reaction system quickly rises to about 100 to 130°C due to the heat of polymerization, and as a result, the moisture in the system is rapidly removed without any external heating. After evaporation, the desired low water content polymer (dry solid) is obtained. The water content of the resulting polymer varies slightly depending on the reaction conditions, etc., but is usually about 15% or less, more preferably about 10% or less, and this can be achieved by simply using a conventional method without any subsequent drying step. Therefore, a desired powder product can be obtained only by pulverization or the like.

かくして上記方法によれば極めて迅速且つ容易に通常含
水率が15%以下の乾燥固体状態のポリアクリル酸塩架
橋物を収得できる。該重合体中に残存する単量体は、重
合体に対し僅か2000ppm以下であり、重合率も極
めて良好である。
Thus, according to the above method, a dry solid crosslinked polyacrylate product having a moisture content of usually 15% or less can be obtained very quickly and easily. The monomer remaining in the polymer is only 2000 ppm or less based on the polymer, and the polymerization rate is also extremely good.

かくして得られる重合体乾燥固体は、これを引き続き通
常の粉砕機等を用いて容易に粉末化することができる。
The thus obtained dry polymer solid can be easily powdered using a conventional grinder or the like.

またポリアクリル酸塩架橋物の好ましい第二の製法(特
願昭57−128266号)は、上記第一の方法におけ
る混合単量体の加温水溶液の調製に当り、更に沸点40
〜150°Cの有機溶剤を必須成分として利用する点を
最大の特徴とし、その他は基本的には、はぼ同様にして
実施される。該第二11− の方法における上記特定の溶剤としては、例えばメタノ
ール、エタノール、n−プロパツール、アセトン、メチ
ルエチルケトン、シクロヘキサン、n−へ−t−サン、
n−へブタン、ベンゼン、トルエン、テトラヒドロフラ
ン等が挙げられ、これらは□ 前記単量体に対して0.
5〜15重量%好ましくは1〜10重量%となる量で用
いられる。
A second preferred method for producing a cross-linked polyacrylate product (Japanese Patent Application No. 128266/1982) further includes a boiling point of 40
The main feature is that an organic solvent of ~150°C is used as an essential component, and other aspects are basically carried out in the same manner as in Habo. Examples of the above-mentioned specific solvent in the method of No. 11-- include methanol, ethanol, n-propanol, acetone, methyl ethyl ketone, cyclohexane, n-h-t-san,
Examples include n-hebutane, benzene, toluene, tetrahydrofuran, etc., and these are □0.
It is used in an amount of 5 to 15% by weight, preferably 1 to 10% by weight.

本発明に用いる上記吸水性樹脂は、粉末状である限り、
特にその形状、大きさ等に制限はないが、通常約10〜
600メツシユの粒子径を有するのが好ましい。
As long as the water-absorbing resin used in the present invention is in powder form,
There are no particular restrictions on its shape or size, but it is usually about 10~
Preferably, the particle size is 600 mesh.

本発明組成物を構成する他方の必須成分とする無機質粉
末は、含水二酸化ケイ素、含水酸化アルミニウム、含水
酸化チタン、之等の無水物並びに之等を主成分として含
有するものから選択される。
The inorganic powder which is the other essential component constituting the composition of the present invention is selected from anhydrides such as hydrated silicon dioxide, hydrated aluminum oxide, hydrated titanium oxide, etc., and those containing these as main components.

上記各無機化合物は、その結晶系に制限はなく、例えば
酸化アルミニウムではα型、β型、γ型のいずれも同様
に有効に利用できる。また酸化チタ12− ンはTie、 T i 2OB 、TiO2のいずれで
あってもよい。
The crystal systems of the above-mentioned inorganic compounds are not limited; for example, in the case of aluminum oxide, any of the α-type, β-type, and γ-type can be effectively utilized. Furthermore, the titanium oxide may be any of Tie, Ti2OB, and TiO2.

更に之等の含水物の含水量も特に限定はなく、例。Furthermore, there is no particular limitation on the water content of the water-containing products, such as the following.

えば酸化アルミニウムではA12oB・[20、A/2
08・2H20、k120s・3H20が、酸化チタン
ではTiO2・I(20、TiO2・2H20等が同様
に用い得る。
For example, for aluminum oxide, A12oB・[20, A/2
For titanium oxide, TiO2.I(20, TiO2.2H20, etc.) can be similarly used.

また上記含水もしくは無水の無機化合物を主成分として
含有する物質としては、例えばコロイダルシリカ、ホワ
イトカーボン、超微粒子状無水二酸化ケイ素等の含水二
酸化ケイ素及び(又は)無水二酸化ケイ素を主成分とす
るもの、板状水和ア・ル這す、繊維状水和アルミナ等の
微粉アルミナのように含水乃至無水の酸化アルミニウム
を主成分とするもの、クレー、タルク、カオリン等のル
チル形及びアナタース形の含水乃至無水酸化チタンを主
成分として含有するもの等を例示できる。2等無機質粉
末はその1種を単独でもまた2種以上を混合しても同様
に使用できる。その吸水性樹脂粉末に対する配合量は、
通常該樹脂粉末重量の約0.01〜10重量%、好まし
くは約0.1〜5重量%とされ、これ番こより本発明所
期の効果を奏し得る。
Examples of substances containing the above-mentioned hydrous or anhydrous inorganic compound as a main component include those containing hydrous silicon dioxide and/or anhydrous silicon dioxide as a main component, such as colloidal silica, white carbon, and ultrafine particulate anhydrous silicon dioxide; Platy hydrated alumina, fibrous hydrated alumina and other fine powder aluminas whose main component is hydrated or anhydrous aluminum oxide, clay, talc, kaolin and other rutile and anatase hydrated aluminas. Examples include those containing anhydrous titanium oxide as a main component. The secondary inorganic powders can be used alone or in combination of two or more. The amount of water-absorbing resin powder is as follows:
Usually, the amount is about 0.01 to 10% by weight, preferably about 0.1 to 5% by weight, based on the weight of the resin powder, and the desired effect of the present invention can be achieved by this amount.

勿論上記範囲を上回る量の添加も可能であるが、この場
合製品中の吸水性樹脂粉末自体がそれだけ少なくなり、
本発明組成物の見掛けの吸水能が低下する(同一用途に
それだけ多くの組成物の使用が必要となる)不利がある
。また上記無機質粉末は、通常人手される粉末形態のま
ま使用できるが、好ましくはその粉末粒子径は約10μ
m以下であるのがよい。
Of course, it is possible to add an amount exceeding the above range, but in this case, the amount of water-absorbing resin powder itself in the product will decrease accordingly.
A disadvantage is that the apparent water absorption capacity of the composition according to the invention is reduced (requiring the use of more composition for the same application). Further, the above-mentioned inorganic powder can be used in the form of a powder that is usually manually prepared, but preferably the powder particle size is about 10 μm.
It is preferable that it is less than m.

本発明組成物は、単に上記吸水性樹脂粉末に、上記特定
の無機質粉末の所定量を均−Iこ混合(粉末混合)する
ことにより調製される。混合方法は粉末混合に通常用い
られる各種の操作、代表的には機械的混合操作によるこ
とができる。
The composition of the present invention is prepared simply by uniformly mixing (powder mixing) a predetermined amount of the above-mentioned specific inorganic powder with the above-mentioned water-absorbing resin powder. The mixing method can be any of the various operations commonly used for powder mixing, typically mechanical mixing operations.

かくして得られる本発明組成物は、吸水性樹脂本来の吸
水能は全く変化させることなく、その吸湿性(ブロッキ
ング性)を顕著に改善されており、例えば生理用品、紙
おむつ、使い捨てぞうきん等の衛生用品や農林園芸関係
の保水剤、諸工業用脱水剤、汚泥凝固剤、増粘剤、建材
の結露防止剤、更に各種薬剤のリリースコントロール剤
等の各種用途に非常に有効に利用できる。
The thus obtained composition of the present invention has significantly improved hygroscopicity (blocking property) without changing the water-absorbing ability inherent to the water-absorbing resin at all, and can be used for sanitary products such as sanitary products, disposable diapers, and disposable cloths. It can be very effectively used for various purposes such as water retention agents for agriculture, forestry, and horticulture, dehydration agents for various industries, sludge coagulants, thickeners, anti-condensation agents for building materials, and release control agents for various chemicals.

以下本発明番更に詳しく説明するため吸水性樹脂の製法
を参考例として挙げ、次いで実施例を挙げる。
Hereinafter, in order to explain the present invention in more detail, a method for producing a water-absorbing resin will be given as a reference example, and then examples will be given.

参考例1 アクリル酸72.1yを脱イオン水22.2yに加え、
更にこれに中和剤として純度85%の水酸化カリウム4
9.5yと、ジビニル系化合物としてN、N−メチレン
ビスアクリルアミド0.01yとを順次添加し、混合単
量体濃度70重量%のアクリル酸カリ−ラム水溶液(中
和度75%)を調製する。
Reference Example 1 Add 72.1y of acrylic acid to 22.2y of deionized water,
Furthermore, potassium hydroxide 4 with a purity of 85% is added as a neutralizing agent.
9.5y and 0.01y of N,N-methylenebisacrylamide as a divinyl compound are sequentially added to prepare a potassium rum acrylate aqueous solution (neutralization degree 75%) with a mixed monomer concentration of 70% by weight. .

上記で調製された水溶液を70°Cに保温し、こ。The aqueous solution prepared above was kept warm at 70°C.

れに過硫酸アンモニウムの18%水溶液2.9y(アク
リル酸カリウム、遊離アクリル酸及びN、 Nl 5− 一メチレンビスアクリルアミドの合計重量、以下同じ、
に対し0.5重量%)及び亜硫酸水素す) IJウムの
30.6%水溶液1.7y(0,5重量%)を混合し、
混合液をエンドレスの移動ベルト上に厚さ約10mmの
層状に流下延展させる。約30秒後、重合反応が開始さ
れ、該反応は約1分間で完結する。
Add 2.9y of an 18% aqueous solution of ammonium persulfate (total weight of potassium acrylate, free acrylic acid and N, Nl 5-monethylenebisacrylamide, the same below)
0.5% by weight) and hydrogen sulfite) and 1.7y (0.5% by weight) of a 30.6% aqueous solution of IJium,
The mixed solution is spread on an endless moving belt in a layer having a thickness of about 10 mm. After about 30 seconds, the polymerization reaction starts and is completed in about 1 minute.

その間の最高温度は約120°Cである。The maximum temperature during this period is approximately 120°C.

かくして含水率11%、残存単量体濃度1200ppm
のポリアクリル酸カリウム架橋物の帯状乾燥固体を得る
。これは粉砕機により粉砕することにより粉末化される
。得られる粉末の吸水能は脱イオン水の場合450であ
り、1%食塩水の場合60であった。尚この吸水能は、
得られる重合体粉末1y(絶乾重量換算)を供試水に投
入後、該粉末が吸収した供試水重量(9)を求めること
により評価されるものである。
Thus, the water content was 11% and the residual monomer concentration was 1200 ppm.
A strip-shaped dry solid of crosslinked potassium polyacrylate is obtained. This is pulverized by pulverization using a pulverizer. The water absorption capacity of the resulting powder was 450 in deionized water and 60 in 1% saline. Furthermore, this water absorption capacity is
The evaluation is performed by adding the resulting polymer powder 1y (calculated as absolute dry weight) to test water and then determining the weight (9) of the test water absorbed by the powder.

参考例2〜9 参考例1にかいて調製される混合単量体の濃度、16− その保温温度条件、用いるジビニル系化合物(N。Reference examples 2 to 9 Concentration of mixed monomer prepared in Reference Example 1, 16- The insulation temperature conditions, the divinyl compound (N.

N−メチレンビスアクリルアミド)の使用量、中和剤の
種類とその使用量(中和度)並びに重合反応開始剤とす
る過硫酸アンモニウム(APSと略す)及び亜硫酸水素
す) IJウム(SPSと略す)の混合単量体に対する
使用量のいずれか少なくとも1種を下記第1表に示す通
り変化させ、同様にして重合体を得る。尚第1表には参
考例1のものをも併記する・   第 1 表 混合単量     ジビニ 開始剤濃度参考例 体濃度 N  (重量%) (”C)       APS  
 5PS1   70   70  0.01  0.
5    G、5   0H75260700,010
,50,511II3   70   75  0.0
1  0.5   0.5    n   n4   
70   7G   0.03  0.5   0.5
    s   /15   7G    70  0
.05   G、5   0.5    //   n
6   70   70   G、10   G、5 
  0.5    tt   u7   70   7
0  0.01  0.8   0.8    II 
  II8   70   70  0.01  1.
OLo    n表中ジビニル系化合物の使用量は、混
合単量体(アクリル酸カリウム、遊離アクリル酸及び該
ジビニル系化合物)中の重量%により表示し、また開始
剤濃度は上記混合単量体と該開始剤との総重量(固型分
換算)中の開始剤重量%により表示するものである。
The amount of N-methylenebisacrylamide used, the type and amount of neutralizing agent used (degree of neutralization), and ammonium persulfate (abbreviated as APS) and hydrogen sulfite (abbreviated as SPS) as polymerization reaction initiators. Polymers were obtained in the same manner by changing the amount of at least one of the mixed monomers used as shown in Table 1 below. In Table 1, the results of Reference Example 1 are also listed.Table 1 Mixed monomer amount Gibini Initiator concentration reference example Body concentration N (wt%) (''C) APS
5PS1 70 70 0.01 0.
5 G, 5 0H75260700,010
,50,511II3 70 75 0.0
1 0.5 0.5 n n4
70 7G 0.03 0.5 0.5
s /15 7G 70 0
.. 05 G, 5 0.5 // n
6 70 70 G, 10 G, 5
0.5 tt u7 70 7
0 0.01 0.8 0.8 II
II8 70 70 0.01 1.
The amount of the divinyl compound used in the OLo n table is expressed in weight% of the mixed monomer (potassium acrylate, free acrylic acid, and the divinyl compound), and the initiator concentration is the proportion of the above mixed monomer and the divinyl compound. It is expressed as the weight % of the initiator in the total weight (in terms of solid content) including the initiator.

得られた各重合体(ポリアクリル酸カリウム架橋物)の
乾燥固体の含水率及びこれを参考例1と同様に粉末化後
の粉末を、脱イオン水及び1%食塩水に添加して求めた
吸水能を下記第2表に示す。
The moisture content of the dry solid of each obtained polymer (potassium polyacrylate crosslinked product) was determined by adding the powder after powdering to deionized water and 1% saline in the same manner as in Reference Example 1. The water absorption capacity is shown in Table 2 below.

第  2  表 参考例10〜13 アクリル酸72.1 ftを脱イオン水18.0 y、
固形水酸化カリウム(含水率4%)40.9p及び第3
表に記載の各種溶剤5.2y(対モノマー5%に相当)
を混合し75°Cに加温してお(。このモノマー水性液
及び2.2−アゾビス(2−アミジノプロパン)塩酸塩
の10%水溶液4.0yを混合し、ただちにエンドレス
の移動ベルト上に厚さ5mmに流下延展させ葛。約15
秒後重合反応が始まり約30秒で完結した。その間の最
高温度はいずれも130〜135°Cであった。
Table 2 Reference Examples 10 to 13 72.1 ft of acrylic acid was added to 18.0 y of deionized water,
Solid potassium hydroxide (water content 4%) 40.9p and 3rd
Various solvents listed in the table 5.2y (equivalent to 5% of monomer)
This monomer aqueous liquid and 4.0 y of a 10% aqueous solution of 2,2-azobis(2-amidinopropane) hydrochloride were mixed and immediately placed on an endless moving belt. Dry and spread the kudzu to a thickness of 5 mm. Approximately 15
A few seconds later, the polymerization reaction started and was completed in about 30 seconds. The maximum temperature during that time was 130-135°C.

かくしてポリアクリル酸カリウム架橋物の乾燥した帯状
物を得た。これを粉砕して20〜100メツシユの粉末
とした。いずれも含水率は4〜6%であった。
A dried strip of crosslinked potassium polyacrylate was thus obtained. This was ground into a powder of 20 to 100 meshes. In all cases, the moisture content was 4 to 6%.

これらの粉末各0.1yを精秤し、脱イオン水または1
%食塩水に10秒、30秒及び15分間浸漬後の吸水能
を測定した。結果を第3表に示す。
Accurately weigh 0.1y of each of these powders, add deionized water or
% saline solution for 10 seconds, 30 seconds, and 15 minutes. The results are shown in Table 3.

第  3  表 実施例1 上記参考例1で得たポリアクリル酸カリウム架橋物粉末
(粒径約50〜200メツシユ)100重量部に、酸化
ケイ素(5i02、粒径的12mμ)を0.2〜5.0
重量部の範囲で夫々粉体混合して本発明組成物(試料N
o、 、1〜5)を得た。
Table 3 Example 1 To 100 parts by weight of the potassium polyacrylate crosslinked powder (particle size of about 50 to 200 mesh) obtained in Reference Example 1, 0.2 to 5 parts of silicon oxide (5i02, particle size of 12 mμ) was added. .0
The composition of the present invention (sample N) was prepared by mixing powders in the range of parts by weight.
o, , 1 to 5) were obtained.

得られた各混合粉末試料につき、以下の通り粉体流動性
試験を行なった。即ち各試料を25°C175%RH零
囲気中で24時間放置後、之等を内径42mm、 高さ
90m1nで、2.5%〜18 mmft ’(D、範
W異なる5種の孔径をもつガラス製テスト用じょうごに
入れ、各じょうごをオリフィスを下方に重直に懸吊し、
オリフィスから流出する試料の流出状態を目視で判定し
、以下の基準により評価した。
A powder fluidity test was conducted on each of the obtained mixed powder samples as follows. That is, after each sample was left in a zero atmosphere at 25°C and 175% RH for 24 hours, it was made into a glass with an inner diameter of 42 mm, a height of 90 mm, and 2.5% to 18 mmft' (D, range W) with five different pore sizes. Place each funnel in a manufactured test funnel, suspend each funnel vertically with the orifice downward,
The flow state of the sample flowing out from the orifice was visually determined and evaluated based on the following criteria.

〈流動性評価〉 l・・・オリフィス孔径2.5mm1のじょうごより流
出する(粉体流動性非常に良好) 2・・・オリフィス孔径5mm1のじょうごより流出す
る(粉体流動性良好) 3・・・オリフィス孔径8 m m 11のじょうごよ
り流出する(粉体流動性全体として良好) 4・・・オリフィス孔径12mmgのじょうごより流出
する(粉体流動性充分) 5・・・オリフィス孔径18mm、mのじょうごより流
出する(粉体流動性不足) 6・・・オリフィス孔径1B?717Fl〆のじょうご
より流出しない(粉体流動性不充分) 結果を下記第4表に示す。尚第4表には比較のため酸化
ケイ素無添加の場合を併記する。
<Fluidity evaluation> l... Outflows from a funnel with an orifice hole diameter of 2.5 mm (very good powder fluidity) 2... Outflows from a funnel with an orifice hole diameter of 5 mm (good powder fluidity) 3...・Flows out from a funnel with an orifice hole diameter of 8 mm (good overall powder fluidity) 4... Outflows from a funnel with an orifice hole diameter of 12 mm (sufficient powder fluidity) 5... Orifice hole diameter of 18 mm, m Outflow from the funnel (lack of powder fluidity) 6... Orifice hole diameter 1B? 717Fl did not flow out from the funnel (insufficient powder fluidity) The results are shown in Table 4 below. For comparison, Table 4 also shows the case where no silicon oxide was added.

実施例2〜9 実施例1に詔いて酸化ケイ素に代え、下記第5表に示す
各無機質粉末の夫々所定量を用い同様にして本発明組成
物を得た。得られた各試料につき、同様にして行なった
粉体流動性試験の結果を第5表に併記する。
Examples 2 to 9 Compositions of the present invention were obtained in the same manner as in Example 1 except that in place of silicon oxide, predetermined amounts of each inorganic powder shown in Table 5 below were used. Table 5 also shows the results of a powder fluidity test conducted in the same manner for each sample obtained.

第  5  表 実施例10〜23 実施例1において、参考例1で得たポリアクリル酸カリ
ウム架橋物粉末に代え、参考例2〜13で得たポリアク
リル酸カリウム架橋物粉末(粒径20〜100メツシユ
)、市販吸水樹脂A(P”サンウエツ)IM−1000
J、三洋化成社製、澱粉−アクリロニトリル系吸水樹脂
)及び市販吸水樹脂B(rアクアキープ10 SHJ、
製鉄化学社製、ポリアクリル酸ナトリウム系吸水樹脂)
の夫々を用い、酸化ケイ素の添加量を1.0重量%と一
定として、同様にして本発明組成物を得た。
Table 5 Examples 10 to 23 In Example 1, in place of the potassium polyacrylate crosslinked powder obtained in Reference Example 1, potassium polyacrylate crosslinked powder obtained in Reference Examples 2 to 13 (particle size 20 to 100) was used. commercially available water-absorbing resin A (P” Sanwetsu) IM-1000
J, manufactured by Sanyo Chemical Co., Ltd., starch-acrylonitrile water absorbing resin) and commercially available water absorbing resin B (r Aqua Keep 10 SHJ,
Manufactured by Seitetsu Kagaku Co., Ltd., sodium polyacrylate water absorbing resin)
A composition of the present invention was obtained in the same manner using each of the above, and the amount of silicon oxide added was constant at 1.0% by weight.

各組成物につき実施例1と同一試験を繰り返した結果を
下記第6表に示す。尚各吸水樹脂を夫々単独で試験した
比較試験の結果、いずれの樹脂も流動性は6の評価であ
った。
The same test as in Example 1 was repeated for each composition, and the results are shown in Table 6 below. As a result of a comparative test in which each water-absorbing resin was tested individually, the fluidity of each resin was evaluated as 6.

上記第4表乃至第6表に示す結果より明らかな通り、本
発明組成物は、その粉体流動性が極めて改善されて詔り
、吸水性樹脂単独に見られる如き吸湿性(ブロッキング
性)が認められないことが判る。
As is clear from the results shown in Tables 4 to 6 above, the composition of the present invention has extremely improved powder fluidity and has no hygroscopicity (blocking property) as seen in water-absorbing resins alone. It turns out that it is not acceptable.

Claims (1)

【特許請求の範囲】[Claims] ■ 吸水性樹脂乾燥粉末に、含水二酸化ケイ素、含水酸
化アルミニウム、含水酸化チタン、之等の無水物並びに
之等を主成分として含有する無機物質から選ばれた少な
くとも1種の粉末を混合したことを特徴とする吸水性樹
脂粉末組成物。
■ The water absorbent resin dry powder is mixed with at least one powder selected from anhydrous substances such as hydrated silicon dioxide, hydrated aluminum oxide, hydrated titanium oxide, etc., and inorganic substances containing these as main components. Characteristic water-absorbing resin powder composition.
JP19151782A 1982-10-29 1982-10-29 Water-absorbing powdery resin composition Pending JPS5980459A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP19151782A JPS5980459A (en) 1982-10-29 1982-10-29 Water-absorbing powdery resin composition

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP19151782A JPS5980459A (en) 1982-10-29 1982-10-29 Water-absorbing powdery resin composition

Publications (1)

Publication Number Publication Date
JPS5980459A true JPS5980459A (en) 1984-05-09

Family

ID=16275967

Family Applications (1)

Application Number Title Priority Date Filing Date
JP19151782A Pending JPS5980459A (en) 1982-10-29 1982-10-29 Water-absorbing powdery resin composition

Country Status (1)

Country Link
JP (1) JPS5980459A (en)

Cited By (30)

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JPS6084360A (en) * 1983-08-31 1985-05-13 Sumitomo Chem Co Ltd Highly water-absorptive high-molecular material composition
JPS60152551A (en) * 1984-01-19 1985-08-10 Nitto Electric Ind Co Ltd Tacky water-containing gel
JPS61141760A (en) * 1984-12-13 1986-06-28 Miyata Kogyo Kk Gelling agent for aqueous solution
JPS62243648A (en) * 1986-04-15 1987-10-24 Hirobumi Kajiwara Water-containing powder of granule and production thereof
JPS6337143A (en) * 1986-07-31 1988-02-17 Daicel Chem Ind Ltd Highly water-absorbing composition
JPS6348341A (en) * 1986-08-18 1988-03-01 フイリツプス ピトロ−リアム カンパニ− Water dispersible polymer composition
JPS63117068A (en) * 1986-11-01 1988-05-21 Shiraishi Maretomo Production of highly water-absorbing resin composition
JPS63118375A (en) * 1986-06-04 1988-05-23 Seitetsu Kagaku Co Ltd Water-absorptive composition
JPS644653A (en) * 1987-06-26 1989-01-09 Lion Corp Polymeric absorbent composition
DE3741158A1 (en) * 1987-12-04 1989-06-15 Stockhausen Chem Fab Gmbh POLYMERISATES WITH HIGH ABSORPTION SPEED FOR WATER AND AQUEOUS LIQUIDS, METHOD FOR THE PRODUCTION THEREOF AND USE AS ABSORBENTS
JPH01162504A (en) * 1987-12-21 1989-06-27 Kawasaki Steel Corp Method and device for special rolling with different peripheral speed for metal sheet
JPH02238035A (en) * 1989-03-13 1990-09-20 Mitsubishi Petrochem Co Ltd Powder polymer composition having highly water-absorbing property
GR890100525A (en) * 1989-08-24 1991-12-30 John Bethune Kenneth Absorbents
GR1001334B (en) * 1992-05-29 1993-08-31 Colgate Palmolive Co Linear viscoelastic aqueous liquid automatic dishwasher detergent composition.
US5475062A (en) * 1993-01-26 1995-12-12 Nippon Shokubai Co., Ltd. Method for surface treatment of absorbent resin
EP0705643A1 (en) 1994-10-05 1996-04-10 Sanyo Chemical Industries, Ltd. Improved water-absorbent resin particles and the production thereof
US6514615B1 (en) 1999-06-29 2003-02-04 Stockhausen Gmbh & Co. Kg Superabsorbent polymers having delayed water absorption characteristics
US6809158B2 (en) 2000-10-20 2004-10-26 Nippon Shokubai Co., Ltd. Water-absorbing agent and process for producing the same
JP2006075055A (en) * 2004-09-08 2006-03-23 Nippon Shokubai Co Ltd Water-holding material for growing plant, consisting mainly of water-absorbing resin
JP2007513205A (en) * 2003-12-05 2007-05-24 株式会社日本触媒 Water-retaining material for particulate plant growth mainly composed of water-absorbing resin
US7473739B2 (en) 2004-02-05 2009-01-06 Nippon Shokubai Co., Ltd. Particulate water absorbent agent and production method thereof, and water absorbent article
WO2011040472A1 (en) 2009-09-29 2011-04-07 株式会社日本触媒 Particulate water absorbent and process for production thereof
WO2011115216A1 (en) 2010-03-17 2011-09-22 株式会社日本触媒 Method of producing absorbent resin
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Cited By (43)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS6084360A (en) * 1983-08-31 1985-05-13 Sumitomo Chem Co Ltd Highly water-absorptive high-molecular material composition
JPS60152551A (en) * 1984-01-19 1985-08-10 Nitto Electric Ind Co Ltd Tacky water-containing gel
JPS6313452B2 (en) * 1984-01-19 1988-03-25 Nitto Electric Ind Co
JPS61141760A (en) * 1984-12-13 1986-06-28 Miyata Kogyo Kk Gelling agent for aqueous solution
JPS627228B2 (en) * 1984-12-13 1987-02-16 Myata Kogyo Kk
JPS62243648A (en) * 1986-04-15 1987-10-24 Hirobumi Kajiwara Water-containing powder of granule and production thereof
JPH0534383B2 (en) * 1986-06-04 1993-05-21 Sumitomo Seika Kk
JPS63118375A (en) * 1986-06-04 1988-05-23 Seitetsu Kagaku Co Ltd Water-absorptive composition
JPS6337143A (en) * 1986-07-31 1988-02-17 Daicel Chem Ind Ltd Highly water-absorbing composition
JPS6348341A (en) * 1986-08-18 1988-03-01 フイリツプス ピトロ−リアム カンパニ− Water dispersible polymer composition
JPS63117068A (en) * 1986-11-01 1988-05-21 Shiraishi Maretomo Production of highly water-absorbing resin composition
JPS644653A (en) * 1987-06-26 1989-01-09 Lion Corp Polymeric absorbent composition
DE3741158A1 (en) * 1987-12-04 1989-06-15 Stockhausen Chem Fab Gmbh POLYMERISATES WITH HIGH ABSORPTION SPEED FOR WATER AND AQUEOUS LIQUIDS, METHOD FOR THE PRODUCTION THEREOF AND USE AS ABSORBENTS
DE3741158C2 (en) * 1987-12-04 1990-03-08 Chemische Fabrik Stockhausen Gmbh, 4150 Krefeld, De
JPH01162504A (en) * 1987-12-21 1989-06-27 Kawasaki Steel Corp Method and device for special rolling with different peripheral speed for metal sheet
JPH02238035A (en) * 1989-03-13 1990-09-20 Mitsubishi Petrochem Co Ltd Powder polymer composition having highly water-absorbing property
GR890100525A (en) * 1989-08-24 1991-12-30 John Bethune Kenneth Absorbents
GR1001334B (en) * 1992-05-29 1993-08-31 Colgate Palmolive Co Linear viscoelastic aqueous liquid automatic dishwasher detergent composition.
US5475062A (en) * 1993-01-26 1995-12-12 Nippon Shokubai Co., Ltd. Method for surface treatment of absorbent resin
US5668078A (en) * 1994-10-05 1997-09-16 Sanyo Chemical Industries, Ltd. Water-absorbent resin particles and the production thereof
EP0705643A1 (en) 1994-10-05 1996-04-10 Sanyo Chemical Industries, Ltd. Improved water-absorbent resin particles and the production thereof
US6514615B1 (en) 1999-06-29 2003-02-04 Stockhausen Gmbh & Co. Kg Superabsorbent polymers having delayed water absorption characteristics
US6809158B2 (en) 2000-10-20 2004-10-26 Nippon Shokubai Co., Ltd. Water-absorbing agent and process for producing the same
JP2007513205A (en) * 2003-12-05 2007-05-24 株式会社日本触媒 Water-retaining material for particulate plant growth mainly composed of water-absorbing resin
US7473739B2 (en) 2004-02-05 2009-01-06 Nippon Shokubai Co., Ltd. Particulate water absorbent agent and production method thereof, and water absorbent article
US7582705B2 (en) 2004-02-05 2009-09-01 Nippon Shokubai Co., Ltd. Particulate water absorbent agent and production method thereof, and water absorbent article
JP2006075055A (en) * 2004-09-08 2006-03-23 Nippon Shokubai Co Ltd Water-holding material for growing plant, consisting mainly of water-absorbing resin
US9062140B2 (en) 2005-04-07 2015-06-23 Nippon Shokubai Co., Ltd. Polyacrylic acid (salt) water-absorbent resin, production process thereof, and acrylic acid used in polymerization for production of water-absorbent resin
US9926449B2 (en) 2005-12-22 2018-03-27 Nippon Shokubai Co., Ltd. Water-absorbent resin composition, method of manufacturing the same, and absorbent article
US10358558B2 (en) 2005-12-22 2019-07-23 Nippon Shokubai Co., Ltd. Water-absorbent resin composition, method of manufacturing the same, and absorbent article
US9090718B2 (en) 2006-03-24 2015-07-28 Nippon Shokubai Co., Ltd. Water-absorbing resin and method for manufacturing the same
JP5289955B2 (en) * 2006-08-04 2013-09-11 住友精化株式会社 Water-absorbent resin particles, method for producing the same, and absorbent body using the same
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WO2011115221A1 (en) 2010-03-17 2011-09-22 株式会社日本触媒 Method of producing absorbent resin
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US10363544B2 (en) 2014-03-31 2019-07-30 Nippon Shokubai Co., Ltd. Particulate water-absorbing agent
EP3450485A4 (en) * 2016-10-28 2019-08-07 LG Chem, Ltd. Super absorbent polymer and method for producing same
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