JPS6330506A - Production of improved water-soluble acrylamide polymer - Google Patents

Production of improved water-soluble acrylamide polymer

Info

Publication number
JPS6330506A
JPS6330506A JP17182986A JP17182986A JPS6330506A JP S6330506 A JPS6330506 A JP S6330506A JP 17182986 A JP17182986 A JP 17182986A JP 17182986 A JP17182986 A JP 17182986A JP S6330506 A JPS6330506 A JP S6330506A
Authority
JP
Japan
Prior art keywords
polymer
particles
surfactant
acrylamide
water
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.)
Granted
Application number
JP17182986A
Other languages
Japanese (ja)
Other versions
JPH0680087B2 (en
Inventor
Kazuo Ueno
一夫 上野
Mikio Noto
能登 幹雄
Fumio Kimura
文雄 木村
Hiroyuki Kuroki
黒木 博之
Hikotada Tsuboi
坪井 彦忠
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.)
MITSUI SAIANAMITSUDO KK
Mitsui Cyanamid Ltd
Original Assignee
MITSUI SAIANAMITSUDO KK
Mitsui Cyanamid 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 MITSUI SAIANAMITSUDO KK, Mitsui Cyanamid Ltd filed Critical MITSUI SAIANAMITSUDO KK
Priority to JP17182986A priority Critical patent/JPH0680087B2/en
Publication of JPS6330506A publication Critical patent/JPS6330506A/en
Publication of JPH0680087B2 publication Critical patent/JPH0680087B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

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  • Addition Polymer Or Copolymer, Post-Treatments, Or Chemical Modifications (AREA)
  • Processes Of Treating Macromolecular Substances (AREA)
  • Processing And Handling Of Plastics And Other Materials For Molding In General (AREA)

Abstract

PURPOSE:To obtain the title high-MW polymer of excellent water solubility and improved dusting property, by drying hydrated gel particles to have a specified net polymer content, pulverizing, if required, the polymer and granulating the powder by wetting with an aqueous surfactant solution. CONSTITUTION:Acrylamide is polymerized together with, optionally, a monomer copolymerizable therewith in the presence of a radical initiator to obtain acrylamide polymer hydrated gel particles (A) of a net polymer content >=20 wt%. Component A is dried at 70-100 deg.C to form particles of a net polymer content of 50-85 wt%. These particles, if required, after being pulverized, are granulated by wetting by spraying with an aqueous solution of 500-20,000 ppm, based on the net polymer content, of a surfactant (e.g., sorbitan monooleate) to obtain the title polymer as granules of about 2 mm or smaller.

Description

【発明の詳細な説明】 産業上の利用分野 本発明は、発塵性と溶解性の改良された水溶性アクリル
アマイド系重合体の製造法に関する。
DETAILED DESCRIPTION OF THE INVENTION Field of the Invention The present invention relates to a method for producing a water-soluble acrylamide polymer with improved dust generation and solubility.

従来の技術 アクリルアマイド系重合体は廃水処理用凝集剤、抄紙用
粘剤、汚泥脱水用助剤、石油回収用薬剤等各種の分野で
広く使用されているが、一般に粉末の形で供給され、前
記分野で使用する際、これ等重合体粉末を水に溶解させ
て水溶液の形で使用に供される。
Conventional technology Acrylamide polymers are widely used in various fields such as flocculants for wastewater treatment, sticky agents for paper making, sludge dewatering aids, and oil recovery agents, but they are generally supplied in powder form. When used in the above field, these polymer powders are dissolved in water and used in the form of an aqueous solution.

発明が解決しようとする問題点 この溶解作業に際して、重合体粉末中には微粒子も含ま
れる為粉塵が立ち易く、環境上の問題としてしばしば指
摘されている。またいわゆる「ま−こ」が発生して長い
溶解時間を要するケースも多い。
Problems to be Solved by the Invention During this dissolution operation, since the polymer powder contains fine particles, dust tends to be generated, which is often pointed out as an environmental problem. In addition, there are many cases where so-called "magic" occurs and a long dissolution time is required.

このような粉体による上記欠点を避ける為、ポリマー純
分20重量%程度のゲル状品で供給されることもあるが
、この場合、溶解作業時に電動式肉挽機等の細断機によ
り細断しても、粉末品に比べ粒子を細くする事が困難な
為に長い溶解時間を要する。またポリマー純分10重量
%以下のペースト成品も一部に使用されているが、ゲル
状品、ペースト成品共通の問題点は固形分が低い事によ
る輸送コスト、保管コストの増大等、非経済的である。
In order to avoid the above-mentioned disadvantages caused by such powder, it is sometimes supplied as a gel-like product with a polymer purity of about 20% by weight. Even in comparison to powdered products, it is difficult to make the particles thinner, so it takes a long time to dissolve. In addition, paste products with a polymer purity of 10% by weight or less are also used in some cases, but the common problem with gel-like products and paste products is that the low solid content increases transportation costs and storage costs, making them uneconomical. It is.

本発明の目的は高分子量で、且つ、水溶性の良好なアク
リルアマイド系重合体を主成分とする水溶性高分子組成
物の製造方法を提供することにある。
An object of the present invention is to provide a method for producing a water-soluble polymer composition containing as a main component an acrylamide polymer having a high molecular weight and good water solubility.

問題点を解決するための手段 即ち、本発明は、含水ゲル粒子と界面活性剤とを含有し
た水溶性アクリルアマイド系重合体の製造法において、
通常の製法により得られた含水ゲル粒子を乾燥工程に導
き、この含水ゲル粒子中のポリマー純分が50〜85重
量%含有する状態になる迄乾燥した後、これを微粉化す
るか、または微粉化せずに、界面活性剤水溶液を用いて
加湿造粒することを特徴とする発塵性と溶解性の改良さ
れた水溶性アクリルアマイド系重合体の製造方法である
Means for solving the problems, that is, the present invention is a method for producing a water-soluble acrylamide polymer containing hydrous gel particles and a surfactant.
Hydrogel particles obtained by a conventional manufacturing method are subjected to a drying process, and after drying until the polymer content in the hydrogel particles is 50 to 85% by weight, it is pulverized or finely powdered. This is a method for producing a water-soluble acrylamide-based polymer with improved dust-emitting properties and solubility, which is characterized by carrying out humidified granulation using an aqueous surfactant solution without oxidation.

作用 以下、本発明の構成要件を作用と共に説明する。action Hereinafter, the constituent elements of the present invention will be explained together with their effects.

本発明はアクリルアマイド系重合体を主成分とし、これ
に少量の界面活性剤を含有させた水溶性アクリルアマイ
ド系重合体の製造法である。アクリルアマイド系重合体
を得るため重合させる単量体としては、アクリルアマイ
ドのみの場合と、これと共重合可能なものを併用する場
合とがある。
The present invention is a method for producing a water-soluble acrylamide polymer containing an acrylamide polymer as a main component and a small amount of a surfactant. As the monomer to be polymerized to obtain an acrylamide-based polymer, there are cases where only acrylamide is used, and cases where a monomer that can be copolymerized with this is used in combination.

共重合可能な単量体としては、例えばメタアクリルアミ
ド、 (メタ)アクリル酸メチル、(メタ)アクリル酸
エチル等の(メタ)アクリル酸エステル類、アクリル酸
及びその塩、メタアクリル酸及びその塩、2−アクリル
アミド−2−メチルプロパンスルフォン酸等のアミドス
ルフォン酸及びその塩、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
ート等のアミノアルキルエステル類及びその塩、ジメチ
ルアミノプロピルメタアクリルアミド等のアミノアルキ
ルアミド類及びその塩等が挙げられる。
Examples of copolymerizable monomers include methacrylamide, (meth)acrylic acid esters such as methyl (meth)acrylate, and ethyl (meth)acrylate, acrylic acid and its salts, methacrylic acid and its salts, Amidosulfonic acids and their salts such as 2-acrylamido-2-methylpropanesulfonic acid, dimethylaminoethyl (meth)
Examples include aminoalkyl esters and salts thereof such as acrylate and diethylaminoethyl (meth)acrylate, and aminoalkylamides and salts thereof such as dimethylaminopropylmethacrylamide.

該重合体は、アニオン、カチオン、ノニオンのいずれの
タイプであってもよく、ホモポリマーでも、コポリマー
であっても良い。
The polymer may be anionic, cationic, or nonionic, and may be a homopolymer or a copolymer.

アクリルアマイド系重合体の重合方法は、一般的には通
常のフリーラジカル開始による重合であり、水溶液重合
の場合には15〜85重量%の上記単量体濃度の水溶液
に通常のラジカル開始剤、例えば過酸物量始剤、レドッ
クス開始剤及びアゾ系開始剤の中から1種または2種以
上を用い重合せしめる。尚、アクリルアマイド系重合体
は、重合完了後、各種の変性、例えばアルカリによる加
水分解反応を行わせ、陰イオン性カルボキシル基に変成
させる方法、マンニッヒ反応、ホフマン分解反応により
、カチオン性アミン基を導入させる方法等を行ったもの
でもよい0通常は、以上の方法により得られるポリマー
純分が20重量%以上の含水ゲル粒子を乾燥工程に導き
、乾燥させ、含水率20〜95重量%の含水ゲル粒子と
する。
The polymerization method for acrylamide-based polymers is generally polymerization by normal free radical initiation, and in the case of aqueous solution polymerization, a normal radical initiator, For example, one or more of peracid initiators, redox initiators, and azo initiators may be used for polymerization. After completion of polymerization, the acrylamide polymer can be modified to have cationic amine groups by various modifications, such as hydrolysis reaction with an alkali to convert it into anionic carboxyl groups, Mannich reaction, or Hofmann decomposition reaction. Usually, the hydrous gel particles with a polymer purity of 20% by weight or more obtained by the above method are introduced into a drying process, dried, and the water-containing gel particles with a water content of 20 to 95% by weight are obtained. Use gel particles.

本発明においては上記の如き含水ゲル粒子の乾燥工程の
途中で、アクリルアマイド系ポリマー純分50〜85重
量%、好ましくは60〜80重量%及び水分50〜15
重量%、好ましくは40〜20重量%のものを取り出し
、切断機により細粒化するか、またはせずに粒径2mm
以下の含水ゲル粒子を用い、これに界面活性剤水溶液ま
たは混合液を用いて加湿造粒する。乾燥は通常70〜1
00℃程度で行う。
In the present invention, during the drying process of the hydrogel particles as described above, the acrylamide polymer has a pure content of 50 to 85% by weight, preferably 60 to 80% by weight and a water content of 50 to 15% by weight.
% by weight, preferably 40 to 20% by weight, is taken out and made into fine particles with a cutting machine or without, to a particle size of 2 mm.
The following hydrogel particles are used and subjected to humidification and granulation using an aqueous surfactant solution or a mixed solution. Drying is usually 70-1
It is carried out at about 00℃.

この場合ポリマー純分が50重量%未満であると、水分
が多くなるので粉末粒子がケーキングを起こすと共に製
品輸送費が嵩むので好ましくない、一方ポリマー純分が
85重層%を超えると粉立ちが生じ、又、溶解時に「ま
−こ」になり易い。
In this case, if the polymer pure content is less than 50% by weight, it is undesirable because the water content increases, causing caking of the powder particles and increasing product transportation costs.On the other hand, if the polymer pure content exceeds 85% by weight, dusting occurs. Also, it tends to become "sticky" when dissolved.

尚粒径2層−以下とするのは溶解速度を大にする為であ
る。
The reason why the particle size is 2 layers or less is to increase the dissolution rate.

本発明においては、上記含水ゲル粒子に対し、ポリマー
純分当り、500〜20000ppmの界面活性剤を配
合するが、この界面活性剤の具体例としては、平均分子
量400以上のポリエチレングリコール、同じくポリプ
ロピレングリコール、又はポリオキシアルキルエーテル
、ポリオキシエチレンアルキルフェニルエーテル、ポリ
オキシエチレン脂肪酸エステル、ポリオキシエチレン争
ポリオキシプロピレンブロックボリマー、ポリオキシエ
チレンソルビタン脂肪酸エステル、ソルビタン脂肪%エ
ステル等の非イオン型界面活性剤が挙げられる。これら
の中特にソルビタンモノオレート、平均分子量tooo
以上のポリエチレングリコールが好ましい。界面活性剤
としてはさらにこれら以外の界面活性剤、無機塩、油類
等を含有させることができる。この界面活性剤は、含水
ゲル粒子の保存時のケーキングを防止する為であり、5
00PpH未満ではケーキング防止が不十分で、又、2
0000ppm超ではコスト高になると共に組成物がベ
タベタし、流動性が悪化し取扱い性が悪くなる。
In the present invention, 500 to 20,000 ppm of a surfactant is added to the hydrogel particles based on the pure polymer content. Specific examples of this surfactant include polyethylene glycol with an average molecular weight of 400 or more, and polypropylene glycol. , or nonionic surfactants such as polyoxyalkyl ether, polyoxyethylene alkylphenyl ether, polyoxyethylene fatty acid ester, polyoxyethylene polyoxypropylene block polymer, polyoxyethylene sorbitan fatty acid ester, sorbitan fat% ester, etc. can be mentioned. Among these, especially sorbitan monooleate, average molecular weight too
The above polyethylene glycols are preferred. As the surfactant, surfactants other than these, inorganic salts, oils, etc. can be further included. This surfactant is used to prevent caking during storage of hydrogel particles, and
If the pH is less than 00P, caking prevention is insufficient;
If it exceeds 0,000 ppm, the cost will increase and the composition will become sticky, resulting in poor fluidity and poor handling.

以上のようにして得られたポリマー純分が50〜85重
量%の含水ゲル粒子のポリマー純分に対して500〜2
0000ppmの界面活性剤を含有させる。この界面活
性剤を含有させるには、これを水溶液、または混合液と
して、スプレー等により噴霧する添加手段により添加し
て捏和すればよい、このようにすると含水ゲル粒子は水
を吸ってゲル状となり、0.1■以下程度の細かい微粉
はくっつき合って造粒され、全体として約2+*+w以
下程度の粉立ちしない顆粒物が得られる。
500 to 2% of the polymer purity of the hydrogel particles with a polymer purity of 50 to 85% by weight obtained as described above.
0000 ppm of surfactant is included. To incorporate this surfactant, it can be added as an aqueous solution or a mixed solution using an adding means such as spraying, and kneaded.In this way, the hydrogel particles absorb water and form a gel. Therefore, fine powders of about 0.1 square centimeters or less stick together and are granulated, resulting in a non-dusty granule of about 2+*+w or less as a whole.

そして、その表面は界面活性剤によりほぼ被覆された状
態となり、これを長期間荷重下貯蔵してもケーキングが
防止され、発塵性が全くなく、溶解性のすぐれたもので
ある。
The surface is almost coated with the surfactant, and even if it is stored under load for a long period of time, caking is prevented, there is no dust generation, and it has excellent solubility.

実施例 以下実施例をあげて、さらに本発明を説明する。Example The present invention will be further explained below with reference to Examples.

実施例1 通常の製法によって得られたアクリルアマイドとアクリ
ル酸ソーダとのモル比がそれぞれ85:15の共重合体
含水ゲル(ポリマー純分30重量%、水分70重量%)
を乾燥工程に導き、温度80℃で乾燥させ、ポリマー純
分80重量%の含水ゲル粒子とした。
Example 1 A copolymer hydrogel with a molar ratio of acrylamide and sodium acrylate of 85:15, respectively, obtained by a conventional manufacturing method (polymer purity 30% by weight, water content 70% by weight)
was introduced into a drying step and dried at a temperature of 80° C. to obtain hydrogel particles having a polymer purity of 80% by weight.

これを回転ドラム型混合造粒機に1000 g仕込み回
転させながら界面活性剤水溶液を第1表に示すように変
えてスプレーにより噴霧し、30分間攪拌混合した。こ
れらの条件および評価結果を第1表に示す。
1000 g of this was placed in a rotating drum-type mixing granulator, and while the machine was being rotated, the surfactant aqueous solution was varied as shown in Table 1 and sprayed, followed by stirring and mixing for 30 minutes. These conditions and evaluation results are shown in Table 1.

実施例2 実施例1の乾燥工程から取り出す含水ゲルのポリマー純
分を第2表に示すものを用いた以外は実施例と同様に行
った。なお界面活剤はAを用いた。
Example 2 The same procedure as in Example 1 was carried out except that the polymer purity of the hydrogel taken out from the drying process of Example 1 was as shown in Table 2. Note that A was used as the surfactant.

(以下余白) 第1表の界面活性剤品名の記号は次のものを表わし、又
評価は次の方法によって行った。
(The following is a blank space) The symbols for the surfactant product names in Table 1 represent the following, and the evaluation was performed by the following method.

l)界面活性剤品名 A:ソルビタンモノラウレート(商品名レオドールSP
 −LIO) B:ポリエチレングリコールモノオレエート(商品名エ
マノーン4110) C:ポリオキシエチレン高級アルコールエーテル(商品
名エマルゲン707) D:ポリオキシエチレンソルビタンモノオレート(商品
名レオドールTW−0120)E:ポリオキシエチレン
ポリオキシプロピレンブロックポリマー(商品名エマル
ゲンPP−230)F:ポリエチレングリコール#40
0 G:       tt     #60002)評価
試験と評価基準 (1)粉立ちテスト サンプル100gを50cmの高さから落下させ、落下
点より30c■はなれた所に置いた5X5cmの水平ガ
ラス板上の光透過率を測定した。透過率は分光々度肝を
使用し、4日0n−で測定した。
l) Surfactant Product Name A: Sorbitan Monolaurate (Product Name Rheodol SP
-LIO) B: Polyethylene glycol monooleate (trade name Emanone 4110) C: Polyoxyethylene higher alcohol ether (trade name Emulgen 707) D: Polyoxyethylene sorbitan monooleate (trade name Rheodol TW-0120) E: Polyoxy Ethylene polyoxypropylene block polymer (trade name Emulgen PP-230) F: Polyethylene glycol #40
0 G: tt #60002) Evaluation test and evaluation criteria (1) Powder test A 100 g sample was dropped from a height of 50 cm, and the light transmittance was measured on a 5 x 5 cm horizontal glass plate placed 30 cm away from the drop point. was measured. The transmittance was measured using a spectrophotometer at 0n- for 4 days.

(2)溶解時のま\こ発生 静止水1000ai中に1gのサンプルを一時に投下し
、その後400rp■X60分攪拌し未溶解分を150
メツシユ・金網で濾過し評価。
(2) Bulk generation during dissolution 1 g of the sample was dropped into 1000 ai of still water, and then stirred at 400 rpm for 60 minutes to remove undissolved matter by 150 ai.
Filtered through mesh/wire mesh and evaluated.

(3)ケーキング サンプル200gをポリ袋に充填、密封し、100g/
cm2の加重を1週間加え、−度粒状化したものが加重
により団結化する状態を観察。
(3) Fill 200g of the cake sample into a plastic bag, seal it, and
A load of cm2 was applied for one week, and the state in which the -degree granules became agglomerated due to the load was observed.

0・・・全く固結せず 0・・・わずかにブロック状になっているが、かるく触
れただけで崩壊する。
0: Not solidified at all. 0: Slightly blocky, but will disintegrate if lightly touched.

Δ・・・固結が見られ押しつぶすことで崩壊する。Δ: Consolidation is observed and collapses when crushed.

×・・・完全なブロックで解きほぐすのは困難。×...Difficult to unravel with complete blocks.

(4)溶解性 40Orpmで攪拌している1000−の水にサンプル
1gを加え、90分溶解後150メツシュ金網にて濾過
、不溶解舒を観察。
(4) Solubility: 1 g of sample was added to 1000-ml water being stirred at 40 rpm, dissolved for 90 minutes, filtered through a 150-mesh wire mesh, and undissolved particles were observed.

発明の効果 本発明によれば、従来技術では得られなかった高分子量
で且つ水溶性の良好なアクリルアマイド系重合体を主成
分とする水溶性高分子組成物が、非常に簡単で、しかも
安価に得られる。
Effects of the Invention According to the present invention, a water-soluble polymer composition containing an acrylamide polymer as a main component that has a high molecular weight and good water solubility, which could not be obtained using conventional techniques, can be produced in a very simple and inexpensive manner. can be obtained.

また本発明組成物は荷重下長期保存しても、ケーキング
が生じないこと、使用時には粉立ちが全くなく取扱い易
いこと、水に溶解時ま\こになりにくいことなど発明の
効果は顕著である。
Furthermore, the composition of the present invention has remarkable effects such as not causing caking even when stored under load for a long period of time, being easy to handle with no powdering when used, and not easily becoming lumpy when dissolved in water. .

Claims (1)

【特許請求の範囲】[Claims] 含水ゲル粒子と界面活性剤とを含有した水溶性アクリル
アマイド系重合体の製造法において、通常の製法により
得られた含水ゲル粒子を乾燥工程に導き、この含水ゲル
粒子中のポリマー純分が50〜85重量%含有する状態
になる迄乾燥した後、これを微粉化するか、または微粉
化せずに、界面活性剤水溶液を用いて加湿造粒すること
を特徴とする発塵性と溶解性の改良された水溶性アクリ
ルアマイド系重合体の製造方法。
In a method for producing a water-soluble acrylamide polymer containing hydrogel particles and a surfactant, hydrogel particles obtained by a normal manufacturing method are led to a drying process, and the polymer purity in the hydrogel particles is 50%. After drying to a state containing ~85% by weight, it is pulverized or, without pulverization, it is humidified and granulated using an aqueous surfactant solution. A method for producing an improved water-soluble acrylamide polymer.
JP17182986A 1986-07-23 1986-07-23 Method for producing improved water-soluble acrylic amide polymer Expired - Lifetime JPH0680087B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP17182986A JPH0680087B2 (en) 1986-07-23 1986-07-23 Method for producing improved water-soluble acrylic amide polymer

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP17182986A JPH0680087B2 (en) 1986-07-23 1986-07-23 Method for producing improved water-soluble acrylic amide polymer

Publications (2)

Publication Number Publication Date
JPS6330506A true JPS6330506A (en) 1988-02-09
JPH0680087B2 JPH0680087B2 (en) 1994-10-12

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Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2000011267A1 (en) * 1998-08-19 2000-03-02 Betzdearborn Inc. A process to improve the drainage rate and retention of fines during papermaking

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2000011267A1 (en) * 1998-08-19 2000-03-02 Betzdearborn Inc. A process to improve the drainage rate and retention of fines during papermaking

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JPH0680087B2 (en) 1994-10-12

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