JPH06192432A - Production of granular water-soluble high-molecular compound - Google Patents

Production of granular water-soluble high-molecular compound

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Publication number
JPH06192432A
JPH06192432A JP3059767A JP5976791A JPH06192432A JP H06192432 A JPH06192432 A JP H06192432A JP 3059767 A JP3059767 A JP 3059767A JP 5976791 A JP5976791 A JP 5976791A JP H06192432 A JPH06192432 A JP H06192432A
Authority
JP
Japan
Prior art keywords
water
soluble polymer
silica
polymer compound
granular 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
JP3059767A
Other languages
Japanese (ja)
Other versions
JP3113687B2 (en
Inventor
Yukio Obana
幸生 小花
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.)
DIA FLOC KK
Dia Furotsuku Kk
Original Assignee
DIA FLOC KK
Dia Furotsuku Kk
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 DIA FLOC KK, Dia Furotsuku Kk filed Critical DIA FLOC KK
Priority to JP03059767A priority Critical patent/JP3113687B2/en
Publication of JPH06192432A publication Critical patent/JPH06192432A/en
Application granted granted Critical
Publication of JP3113687B2 publication Critical patent/JP3113687B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

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Abstract

PURPOSE:To obtain a compd. which does not allow undissolved lumps to occur when dissolved, is excellent in flowability, workability, and solubility, and hardly causes dusting by homogeneously mixing a specific granular water-sol. high- molecular compd. with a specific silica and thereby coating the compd. with the silica. CONSTITUTION:A granular water-sol. high-molecular compd. having a water content of 3-15% and a granule size of 2.0mm or lower (e.g. a copolymer of a quaternary salt of dimethylaminoethyl acrylate-methyl chloride with acrylamide) is homogeneously mixed with 0.1-5.0wt.% hydrophilic silica having a mean primary particle size of 5-50nm (e.g. Aerosil 300, a product of Nippon Aerosil) and thereby coated with the silica.

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【産業上の利用分野】本発明は、廃水処理、下水処理等
水処理に有用な粒状水溶性高分子化合物の製造方法に関
する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method for producing a granular water-soluble polymer compound useful for water treatment such as wastewater treatment and sewage treatment.

【0002】[0002]

【従来の技術】水溶性高分子化合物を取扱う場合、吸湿
による固結によって投入等の工程のトラブル、あるいは
微粉の飛散によって作業環境を悪化させる欠点を有す
る。水溶性高分子化合物の吸湿による固結の防止には、
特公昭59−45003公報に見られる如く、重合体分
子内にある塩型カルボキシル基が酸型であった場合に示
す重合体の解離恒数よりも大きい解離恒数を有する酸で
処理したり、特公昭58−51966公報、特公昭61
−48546公報に記載される如く、水溶性高分子重合
体粉末に硫酸水素アルカリ金属塩及び塩基性無機塩、さ
らに必要に応じて、硫酸マグネシウム含水塩及び/また
は吸湿剤を配合して、易分散性とともに固結対策にも効
果を発揮することが知られる。
2. Description of the Related Art When handling a water-soluble polymer compound, there is a drawback that the work environment is deteriorated due to troubles in the process such as charging due to solidification due to moisture absorption or scattering of fine powder. To prevent solidification due to moisture absorption of water-soluble polymer compounds,
As disclosed in JP-B-59-45003, treatment with an acid having a dissociation constant larger than the dissociation constant of the polymer shown when the salt-type carboxyl group in the polymer molecule is acid-type, Japanese Patent Publication 58-51966, Japanese Patent Publication 61
As described in JP-A-48546, a water-soluble polymer powder is mixed with an alkali metal hydrogensulfate and a basic inorganic salt, and if necessary, a magnesium sulfate hydrate and / or a hygroscopic agent to facilitate dispersion. It is known that it exerts an effect as a measure against caking together with the sex.

【0003】微粉の飛散による防塵対策としては、特開
昭57−85844公報では、水溶性粒状ポリマーに、
ポリエチレングリコールまたはポリプロピレングリコー
ルの1〜50重量%水溶液を前記ポリマーに対し、1〜
20重量%添加することが開示され、特公昭61−21
492公報では、水溶性高分子化合物粉末、水溶性無機
化合物粉末及び沸点150℃以上の常温液状有機化合物
を配合し、防塵処理による自由流動性の低下を防止する
事と、溶解時の水分散性を良好とした技術が知見として
得られている。以上の従来の技術では、水溶性高分子化
合物に対する添加剤の添加率が高く、有効分が極めて低
くなったり、処理するための工程の新設を要するなどの
問題点を有する。
As measures against dust due to scattering of fine powder, Japanese Patent Application Laid-Open No. 57-85844 discloses that a water-soluble granular polymer is used.
A 1 to 50% by weight aqueous solution of polyethylene glycol or polypropylene glycol is added to the polymer in an amount of 1 to
It is disclosed that 20% by weight is added.
In 492 publication, a water-soluble polymer compound powder, a water-soluble inorganic compound powder, and a room-temperature liquid organic compound having a boiling point of 150 ° C. or more are blended to prevent reduction of free-flowing property due to dustproof treatment, and water dispersibility during dissolution. Has been obtained as knowledge. The above-mentioned conventional techniques have problems that the addition rate of the additive to the water-soluble polymer compound is high, the effective content is extremely low, and a new process for treatment is required.

【0004】水溶性高分子化合物にシリカを応用した技
術としては、特開昭58−134106公報で成形され
た含水ケーキの表面を無水ケイ酸を主成分とする高分散
性軽質シリカ粉末で被覆した後乾燥することにより、乾
燥工程での相互接着の防止を行なうことが開示されてい
る。また、特開昭63−260928公報では、粉末状
の水溶性高分子化合物に対して、疎水性シリカを添加混
合することにより、易分散性水溶性ポリマーの製造を行
ない、いわゆる「まま粉」対策を行なっている。
As a technique of applying silica to a water-soluble polymer compound, the surface of a water-containing cake formed in JP-A-58-134106 is coated with a highly dispersible light silica powder containing silicic acid as a main component. It is disclosed that post-drying prevents mutual adhesion in the drying step. Further, in Japanese Patent Laid-Open No. 63-260928, a readily dispersible water-soluble polymer is produced by adding hydrophobic silica to a powdery water-soluble polymer compound, which is a so-called “as-is” measure. Are doing.

【0005】[0005]

【発明が解決しようとする課題】水溶性高分子化合物
は、その性質上湿度の高い環境下では速やかに吸湿し、
粒子同志が相互粘着を起こし、流動性を失い、さらには
ケーキングを生ずることとなり供給作業の際には、供給
装置のホッパーあるいはフィーダーを閉塞したり、溶解
時には「まま粉」を生じたりする現象が見られる。ま
た、水溶性高分子化合物は製造時乾燥後粉砕し、篩別工
程を通しているがそれでも供給作業時には、微粉の飛散
による作業環境悪化を生ずる。
The water-soluble polymer compound absorbs moisture quickly in an environment with high humidity due to its nature,
Particles stick to each other, lose fluidity, and cause caking, which may cause the hopper or feeder of the feeder to be clogged during the feeding operation, or "the powder remains" during the melting. Can be seen. Further, the water-soluble polymer compound is pulverized after being dried at the time of manufacturing, and is passed through a sieving process, but even during the supplying operation, the working environment is deteriorated due to scattering of fine powder.

【0006】本発明者は、粒状水溶性高分子化合物の吸
湿、防塵を更に自然流動性をも保持することを課題とし
検討を行なった。これらの問題を解決すれば工程の自動
化、省力化、究極的には無人化が可能となり、その上、
防塵できれば通常行なわれている微粉の篩別工程を省略
出来、このため製品の収率は向上し、収益にも寄与す
る。
The present inventor has conducted studies with the objective of maintaining moisture absorption and dust protection of the granular water-soluble polymer compound and also maintaining natural fluidity. If these problems are solved, it will be possible to automate the process, save labor, and ultimately unmanned.
If dust can be prevented, the usual fine powder sieving process can be omitted, which improves the product yield and contributes to profits.

【0007】[0007]

【課題を解決するための手段】本発明は、含有水分3〜
15%、粒径2.0mm以下の粒状水溶性高分子化合物
に一次粒子の平均径5〜50μmで親水性のシリカ0.
1〜0.5重量%を均一に混合し被覆することを特徴と
する粒状水溶性高分子化合物の製造方法にある。
SUMMARY OF THE INVENTION The present invention has a water content of 3 to 3.
15%, granular water-soluble polymer compound having a particle diameter of 2.0 mm or less, hydrophilic silica with an average primary particle diameter of 5 to 50 μm.
A method for producing a granular water-soluble polymer compound is characterized by uniformly mixing and coating 1 to 0.5% by weight.

【0008】本発明で対象とする水溶性高分子化合物と
しては次のものが挙げられる。 (1)(メタ)アクリルアミド (2)(メタ)アクリル酸 (3)2−アクリルアミド−2−メチルプロパンスルホ
ン酸 (4)(メタ)アクリル酸ジメチルアミノエチルの3級
塩、4級塩
The water-soluble polymer compounds targeted by the present invention include the following. (1) (meth) acrylamide (2) (meth) acrylic acid (3) 2-acrylamido-2-methylpropanesulfonic acid (4) tertiary salt of dimethylaminoethyl (meth) acrylate, quaternary salt

【0009】[0009]

【化1】 [Chemical 1]

【化2】 [Chemical 2]

【0010】(5)(メタ)アクリルアミドプロピルト
リメチルの3級塩、4級塩
(5) Tertiary salt of (meth) acrylamidopropyltrimethyl, quaternary salt

【化3】 (ここでR3 、R4 はHまたはCH3 ,XはCl、B
r,1/2 SO4 を表す。)から選ばれる単独重合体又は
共重合体であり、通常微粉状又は微粒子状をなしてお
り、一般にその粒径は、20mm以下である。
[Chemical 3] (Here, R 3 and R 4 are H or CH 3 , X is Cl, B
represents r, 1/2 SO 4 . 1) is a homopolymer or a copolymer, which is usually in the form of fine powder or fine particles, and generally has a particle size of 20 mm or less.

【0011】粒状の水溶性高分子化合物を工業的に製造
する場合、(1)乾燥直後に粉砕し梱包する方法と、
(2)乾燥後、一時貯蔵した後、粉砕し梱包する方法が
ある。乾燥は、通常50〜120℃の温度範囲で行なわ
れるが、乾燥直後は粒子表面の水分は極めて低く、中心
部は高く粒子内で水分の分布を生じている。水分の分布
は高分子化合物を構成するモノマーの種類組成により異
なるが、放置すれば水分は粒子内で均一となり、表面に
水分が含まれる様になると考えられる。
When industrially producing a granular water-soluble polymer compound, (1) a method of crushing and packing immediately after drying,
(2) After drying, there is a method of temporarily storing, then crushing and packing. Drying is usually performed in a temperature range of 50 to 120 ° C., but immediately after the drying, the water content on the surface of the particles is extremely low, the central portion is high, and the water distribution is generated within the particles. The distribution of water varies depending on the type and composition of the monomers constituting the polymer compound, but it is considered that if left to stand, the water becomes uniform in the particles and the surface contains water.

【0012】本発明は、粉状を含めた粒状の水溶性高分
子化合物にシリカを均一に混合し、高分子粒子を被覆す
る。使用するシリカとしては親水性シリカを用いる。シ
リカには表面のシラノール基を有機珪素ハロゲン化物等
によって疎水性にした製品もあるが、水溶性高分子化合
物は親水性であるため親水性シリカとの相互作用は強い
と考えられる。
In the present invention, silica is uniformly mixed with a granular water-soluble polymer compound including powder to coat polymer particles. Hydrophilic silica is used as silica. Some silicas have a silanol group on the surface thereof made hydrophobic by an organic silicon halide or the like, but since the water-soluble polymer compound is hydrophilic, it is considered that the interaction with the hydrophilic silica is strong.

【0013】疎水性シリカと粒子状水溶性高分子化合物
を混合し、表面を均一に被覆するには、親水性シリカよ
り強い混合を要し固結、防塵の効果を発現させるために
は添加量を多く要する。しかも疎水性シリカの欠点は、
高分子化合物を水に溶解するため投入した際、粒子が疎
水性のため浮遊しやすく、撹拌してもフロック状態とな
り、親水性シリカの場合より可成の長時間を要するので
親水性シリカより高価な疎水性シリカの使用は好ましく
ない。
In order to mix the hydrophobic silica and the particulate water-soluble polymer compound and uniformly coat the surface, stronger mixing than that of the hydrophilic silica is required, and the addition amount is required in order to exert the effect of consolidation and dust prevention. Takes a lot. Moreover, the disadvantage of hydrophobic silica is
It is more expensive than hydrophilic silica because when it is added to dissolve a high molecular compound in water, the particles tend to float because of its hydrophobicity, and it becomes a floc state even if it is stirred, and it takes a longer period of time than hydrophilic silica. The use of transparent hydrophobic silica is not preferred.

【0014】使用する親水性シリカの一次粒子の平均粒
径は5〜50nmの範囲のものである。シリカは二次粒
子となっているが水溶性高分子と混合するときシェアー
により、より小さな二次粒子となる。このとき新たなシ
リカ表面のシラノール基の水素原子が水溶性高分子と結
合または粘着により水溶性高分子粒子を被覆する。シリ
カの粒径が大きくなると水溶性高分子を被覆するシリカ
の量を多く要し、又、付着、粘着状態を保持できなくな
る。
The average particle size of the primary particles of the hydrophilic silica used is in the range of 5 to 50 nm. Silica is a secondary particle, but when mixed with a water-soluble polymer, it becomes a smaller secondary particle due to shear. At this time, a new hydrogen atom of the silanol group on the surface of silica covers the water-soluble polymer particles by binding or adhering with the water-soluble polymer. If the particle size of silica is large, a large amount of silica is required to coat the water-soluble polymer, and it becomes impossible to maintain the state of adhesion and adhesion.

【0015】親水性シリカを添加混合する時期はシリカ
表面のSi・OHが水溶性高分子化合物の粒子表面の水
分と相互作用をし、付着させる必要があるのでシリカの
混合により、微粉の飛散防止効果を発現させるためには
乾燥直後より、10分以上好ましくは30分以上放置し
た後混合する。又この方が混合に要する動力は小さくな
る。
At the time of adding and mixing the hydrophilic silica, Si.OH on the surface of the silica interacts with the water on the surface of the particles of the water-soluble polymer compound, and it is necessary to attach them. Therefore, by mixing the silica, the fine powder is prevented from scattering. In order to bring out the effect, the mixture is left for 10 minutes or more, preferably 30 minutes or more immediately after drying and then mixed. Also, this requires less power for mixing.

【0016】処理時の水溶性高分子化合物の含有水分
は、高いほど親水性シリカ添加の効果が明確となるが、
3%以下は熱負荷が大きく5%程度以上が好ましい。
又、高分子化合物の種類に依存する所は大きいが、略々
15%以下、通常取り扱われる製品で10%程度以下が
好ましい。従って、乾燥直後に粉砕する方法では粉砕後
に、乾燥後一時貯蔵後粉砕する方法の場合には粉砕時、
あるいは粉砕後に混合することが効果的である。
The higher the water content of the water-soluble polymer compound during treatment, the more clearly the effect of adding hydrophilic silica becomes,
If it is 3% or less, the heat load is large, and it is preferably about 5% or more.
Although it depends largely on the kind of the polymer compound, it is preferably about 15% or less, and about 10% or less for the products usually handled. Therefore, in the method of crushing immediately after drying, after crushing, in the case of the method of crushing after temporary storage after drying, during crushing,
Alternatively, mixing after crushing is effective.

【0017】シリカの添加量は粒子状水溶性高分子化合
物の平均粒子径を1.0mmとし、シリカを10nmと
すると、重量で約0.02%の添加で単粒子で被覆する
ことになるが、シリカはフロック状で特に強いシェアー
を掛けていないため、必要添加量は微分の飛散防止の為
には0.05%以上好ましくは0.1%以上が必要であ
り、吸湿しても固結防止あるいは自然流動性保持の為に
は0.2%以上、好ましくは0.5%以上を要する。し
かし、約5%以上の添加では効果の向上が現われず、更
に多くすればシリカ単独で混存することになり好ましく
ない。本発明の実施に好適に用いることのできる親水性
シリカとしては、日本アエロジル株式会社製のアエロジ
ル、シオノギ製薬株式会社製のカープレックス#80,
#67,XR等である。
If the average particle diameter of the particulate water-soluble polymer compound is 1.0 mm and the silica is 10 nm, about 0.02% by weight of silica will be added to cover the particles with single particles. Since silica is a floc and does not have a particularly strong shear, the necessary addition amount is required to be 0.05% or more, preferably 0.1% or more for preventing differential scattering, and even if moisture is absorbed, the solidification occurs. 0.2% or more, preferably 0.5% or more is required to prevent or maintain natural fluidity. However, addition of about 5% or more does not improve the effect, and if the amount is further increased, silica alone is present as a mixture, which is not preferable. Hydrophilic silica that can be preferably used in the practice of the present invention includes Aerosil manufactured by Nippon Aerosil Co., Ltd., Carplex # 80 manufactured by Shionogi Pharmaceutical Co., Ltd.,
# 67, XR, etc.

【0018】粒状の水溶性高分子化合物は、親水性シリ
カで被覆する前に、液状の消泡剤で処理しておくと本発
明の効果を一層高めることができる。消泡剤を添加被覆
しておくと、親水性シリカとの漏れがよくなり、粒状水
溶性高分子化合物の使用時、煙状となって飛散する微粒
子が発生するのを防止し、作業性、作業環境の改善を果
すことができる。
If the granular water-soluble polymer compound is treated with a liquid defoaming agent before being coated with hydrophilic silica, the effect of the present invention can be further enhanced. When an antifoaming agent is added and coated, leakage with hydrophilic silica is improved, and when using a granular water-soluble polymer compound, it is possible to prevent generation of fine particles that become smoke-like and scatter, and workability, The working environment can be improved.

【0019】使用できる消泡剤としてはポリエーテル
型、エマルション型、鉱油配合型の何れでもよく、これ
らは例えばダイヤフロック株式会社製AF103、旭電
化工業株式会社製アデカノールLG678、アデカネー
トB556の商品名で市販されている。
As the defoaming agent which can be used, any of a polyether type, an emulsion type and a mineral oil blending type may be used, and these are, for example, AF103 manufactured by Diafloc Co., Ltd., Adekanol LG678 manufactured by Asahi Denka Kogyo Co., Ltd., and Adecanate B556. It is commercially available.

【0020】本発明は、粒状の水溶性高分子化合物を親
水性シリカで被覆処理する前に、水溶性高分子化合物に
界面活性剤を添加被覆することを包含する。界面活性剤
の付着量は純分で0.01〜1.0重量%になるようそ
の水溶液を水溶性高分子化合物製造時に添加する。
The present invention includes adding a surfactant to the water-soluble polymer compound before coating the granular water-soluble polymer compound with the hydrophilic silica. The aqueous solution of the surfactant is added at the time of producing the water-soluble polymer compound so that the amount of the attached surfactant is 0.01 to 1.0% by weight in pure content.

【0021】使用する界面活性剤は、カルボン酸塩、ス
ルホン酸塩、硫酸エステル塩の陰イオン系、脂肪族の4
級アンモニウム塩の陽イオン系、エーテル型、エーテル
エステル型、エステル型の非イオン系の界面活性剤であ
る。これらは何れも水溶液の形で用いる。界面活性剤を
水溶性高分子を製造する工程で添加しておくと、高含水
分で水溶性高分子化合物を粗砕する工程で高分子化合物
同志の付着を防止すると共に、親水性シリカと水溶性高
分子の濡れを良くし、均一混合を助長する。界面活性剤
は消泡剤と同時に用いてもよい。
The surfactants used are carboxylate, sulfonate, sulfate ester salt anionic, and aliphatic 4
It is a cationic, ether-type, ether-ester, or ester-type nonionic surfactant of a primary ammonium salt. All of these are used in the form of an aqueous solution. If a surfactant is added in the step of producing a water-soluble polymer, the adhesion of polymer compounds will be prevented and the hydrophilic silica and water Improves the wetting of the polymer and promotes uniform mixing. The surfactant may be used together with the defoaming agent.

【0022】[0022]

【実施例】次に、実施例で本発明を説明する。なお、実
施例中「部」とあるのは重量部を意味する。 〔実施例1〕容器に79%のジメチルアミノエチルアク
リレートのメチルクロライド4級塩水溶液890部、5
0%アクリルアミド水溶液155部、純水255部を採
取した。光重合開始剤としてベンゾインエチルエーテル
を30ppm、エチレンジアミン4酢酸2ナトリウム塩
を50ppm、花王(株)製サニーゾールB−50を純
分で1000ppm、ダイヤフロック(株)製消泡剤A
F−103を500ppm(いずれも単量体溶液に対
し)を添加した。20℃に保持し撹拌しながら10N硫
酸を加え、pHを4.5±0.1に調整し、次いで窒素
置換を20分間行なった。
EXAMPLES Next, the present invention will be explained with reference to examples. In addition, "part" in an Example means a weight part. [Example 1] 890 parts of an aqueous solution of 79% dimethylaminoethyl acrylate quaternary salt in a container, 5
155 parts of 0% acrylamide aqueous solution and 255 parts of pure water were collected. As a photopolymerization initiator, 30 ppm of benzoin ethyl ether, 50 ppm of ethylenediamine tetraacetic acid disodium salt, 1000 ppm of Saniosol B-50 manufactured by Kao Co., Ltd. in pure content, Defoamer A manufactured by Diafloc Co., Ltd.
F-103 was added at 500 ppm (both to the monomer solution). The pH was adjusted to 4.5 ± 0.1 by adding 10N sulfuric acid while maintaining the temperature at 20 ° C. with stirring, and then performing nitrogen replacement for 20 minutes.

【0023】次にステンレス板に深さが20mmとなる
ような堰を作り、底面が約23cm×2cmの容器と
し、側面、底面をポリエチレンテフタレートフィルム
(厚さ12μ)で覆い、上記の溶液を注ぎその上をポリ
エチレンテレフタレートフィルム(厚さ12μ)にポリ
塩化ビニルデンを塗布(厚さ4μ)したフィルムで覆っ
た。下方より20℃の水を霧状として吹き付け、上方よ
り三菱電機(株)製蛍光ケミカルランプを用い、2W/
2 の照射強度で、溶液表面温度が4℃上昇するまで照
射しその後0.5W/m2 の照射強度で50分、その後
60W/m2 で10分間紫外線を照射した。重合体を容
器より取り出し、鋏で約3mm×5mm×40mmの棒
状に切断し、60℃で12時間乾燥し、ウィレー型粉砕
機で粉砕しサンプルとした。200mlのポリエチレン
製広口ビンに表1記載の所定量のシリカ(日本アエロジ
ル(株)製アエロジル300)を採取し、所定量の上記
ポリマーを採取し、蓋をし、手で激しく2分間振盪した
後アルミ皿上に5.0gを採取し均一に広げ室内に放置
し水分、サンプルの性状を観察した。その結果を表1に
示した。水分は吸収するが固結は完全に防止されている
ことが確認された。また、シリカ無添加と1%添加の物
につき安息角を測定したところ無添加で41.0度が3
6.0度となり、自然流動性は向上することが確認され
た。
Next, a weir having a depth of 20 mm was formed on the stainless steel plate to make a container having a bottom of about 23 cm × 2 cm, the side and bottom were covered with a polyethylene terephthalate film (thickness 12 μ), and the above solution was added. After pouring, the film was covered with a film of polyvinyl terephthalate film (thickness 12 μm) coated with polyvinylidene chloride (thickness 4 μm). Spray water of 20 ° C as a mist from below and use a fluorescent chemical lamp from Mitsubishi Electric Corp. from above to 2W /
In the irradiation intensity of m 2, followed by irradiation to the surface of the solution temperature rises 4 ° C. 50 minutes at an irradiation intensity of 0.5 W / m 2, and then irradiated for 10 minutes ultraviolet rays 60 W / m 2. The polymer was taken out of the container, cut into a rod shape having a size of about 3 mm × 5 mm × 40 mm with scissors, dried at 60 ° C. for 12 hours, and pulverized with a Willey pulverizer to obtain a sample. A predetermined amount of silica (Aerosil 300 manufactured by Nippon Aerosil Co., Ltd.) shown in Table 1 was collected in a 200 ml polyethylene wide-mouthed bottle, and a predetermined amount of the above polymer was collected, covered with a cap, and vigorously shaken by hand for 2 minutes. 5.0 g was sampled on an aluminum dish, spread uniformly, and allowed to stand in a room to observe water and sample properties. The results are shown in Table 1. It was confirmed that water was absorbed but caking was completely prevented. In addition, the angle of repose was measured for the product with no added silica and the product with 1% added.
It was 6.0 degrees, and it was confirmed that the natural fluidity was improved.

【0024】[0024]

【表1】 [Table 1]

【0025】〔実施例2〕80%のジメチルアミノエチ
ルメタアクリレートのメチルクロライド4級塩水溶液1
300部を採取した。光重合開始剤としてベンゾインエ
チルエーテルを100ppm、エチレンジアミン4酢酸
2ナトリウム塩を50ppmを単量体溶液に添加した。
30℃に保持し撹拌しながら10N硫酸を加え、pHを
5.0±0.5に調整し、次いで窒素置換を30分間行
なった。冷却水を30℃とする以外は実施例1と同様に
して重合し、容器より取り出し室温まで冷却した後、粗
砕し80℃で8時間乾燥し、ウィレー型粉砕機で粉砕し
サンプルとした。200mlのポリエチレン製広口ビン
に所定量のシリカを実施例1と同様に採取し、所定量の
上記ポリマーを採取し蓋をし、手で激しく2分間振盪し
た直後に蓋をとり微粉の飛散状況を観察した。その結果
を表2に示した。比較のためシリカ無添加と、1%添加
したサンプルの粒度分布を測定した。その結果を表3に
示した。超微粉のシリカを1%添加したにもかかわらず
100メッシュ通過分は、むしろ減少し、粒径の大なる
方は激しい振盪中に粉砕されているものと判断でき、防
塵効果は絶大なものである。
[Example 2] 80% dimethylaminoethyl methacrylate methyl chloride quaternary salt aqueous solution 1
300 parts were collected. As a photopolymerization initiator, 100 ppm of benzoin ethyl ether and 50 ppm of ethylenediaminetetraacetic acid disodium salt were added to the monomer solution.
The pH was adjusted to 5.0 ± 0.5 by adding 10N sulfuric acid while maintaining the temperature at 30 ° C. with stirring, and then nitrogen substitution was performed for 30 minutes. Polymerization was carried out in the same manner as in Example 1 except that the cooling water was changed to 30 ° C., taken out of the container, cooled to room temperature, roughly crushed, dried at 80 ° C. for 8 hours, and crushed by a Wiley crusher to obtain a sample. A predetermined amount of silica was sampled in a 200 ml polyethylene wide-mouthed bottle in the same manner as in Example 1, a predetermined amount of the above polymer was sampled, the lid was covered, and immediately after shaking vigorously for 2 minutes by hand, the lid was removed and the fine powder was scattered. I observed. The results are shown in Table 2. For comparison, the particle size distributions of the sample without silica addition and the sample with 1% addition were measured. The results are shown in Table 3. Even though 1% of ultrafine silica was added, the amount passing through 100 mesh was rather reduced, and the one with a larger particle size can be judged to have been crushed during vigorous shaking, and the dustproof effect is great. is there.

【0026】[0026]

【表2】 [Table 2]

【0027】[0027]

【表3】 [Table 3]

【0028】〔実施例3〕粒状水溶性高分子であるダイ
ヤフロック(株)製凝集剤、KP−500,KP−12
01B,KP−1207B,NP−800,AP−74
1を入手、ウィレー型粉砕機で2回粉砕し微分の発生す
るサンプルを作り、実施例1で用いたと同じ親水性シリ
カ0.5重量%添加したものと無添加のものとの微粉の
飛散状況を判定した結果を表4に示した。KP500に
ついては親水性シリカを1%添加しても全く飛散は見ら
れなかった。
Example 3 Flocculant KP-500, KP-12 manufactured by Diafloc Co., Ltd., which is a granular water-soluble polymer.
01B, KP-1207B, NP-800, AP-74
1 was obtained, and the sample was pulverized twice with a Willey-type pulverizer to produce a sample in which differentiation occurs, and the same fine powder as in Example 1 with 0.5% by weight of hydrophilic silica added and without addition of fine powder Table 4 shows the result of the judgment. Regarding KP500, no scattering was observed even when 1% of hydrophilic silica was added.

【0029】 表 4 水溶性高分子化合物 シリカ無添加 0.5%シリカ添加 銘 柄 KP−500 可成の飛散が見られる 極々僅かに飛散が見られる KP−1201B 僅かに飛散する 全く飛散しない KP−1207B 少し飛散する 同 上 NP−800 同 上 同 上 AP−741 同 上 同 上Table 4 Water-soluble polymer compound No silica added 0.5% silica added Brand KP-500 A slight amount of scattering is observed KP-1201B A slight amount of scattering is observed KP-120B A slight amount of scattering KP- 1207B Slightly scattered Same as above NP-800 Same as above Same as above AP-741 Same as above Same as above

【0030】〔実施例4〕実施例2で得た重合体に、固
形分に対し純分が0.5%重量となるように ダイヤフロック(株)製消泡剤AF−103 花王(株)製カチオン界面活性剤サニゾールB−50 を表面に塗布した後、実施例2と同様にサンプルを作成
した。夫々のサンプルに日本アエロジル(株)製アエロ
ジル300を0.2%を混合し、微粉の飛散状況を観察
した結果を表5に示す。
[Example 4] The polymer obtained in Example 2 was mixed so that the pure content was 0.5% by weight based on the solid content. Defoamer AF-103 manufactured by Diafloc Co., Ltd. Kao Corporation. A cationic surfactant Sanizole B-50 was applied to the surface, and then a sample was prepared in the same manner as in Example 2. Table 5 shows the results obtained by mixing 0.2% of Aerosil 300 manufactured by Nippon Aerosil Co., Ltd. into each sample and observing the dispersion state of fine powder.

【0031】 表 5 サンプル 微粉飛散状況 無添加 極僅か粉立ちする程度 AF−103 全く粉立ちしない サニゾールB−50 同 上Table 5 Samples Fine powder scattering status Additive-less powdery degree AF-103 No powdery Sanizole B-50 Same as above

【0032】[0032]

【発明の効果】本発明は、粒状水溶性高分子化合物の製
造時、保管時、使用時に於ける作業環境の改善、製造工
程の安定化、省力化に寄与すると共に、粒状水溶性高分
子化合物の収率向上をもたらす。即ち微粒子を篩別する
ことなく親水性シリカで粒子表面を被覆するので微粒子
の飛散がなく、又、篩別工程を省略できそのため製品の
収率が向上する。収率の上昇は高分子化合物の種類、組
成によって異なるが約0.3%から10%程度期待でき
る。親水性シリカで被覆された粒状水溶性高分子化合物
は、粒子相互の付着を生せず、安息角、流動性が向上す
る。このため保管、移送中流動性を保ち溶解時に「まま
粉」を生ずることもなく、作業性がよく、又、微粉の発
生が少ないので作業環境を良好に保つ等優れた効果を奏
しその価値は大である。
INDUSTRIAL APPLICABILITY The present invention contributes to improvement of the working environment during production, storage and use of a granular water-soluble polymer compound, stabilization of the production process, and labor saving. Yield improvement. That is, since the surface of the particles is coated with the hydrophilic silica without sieving the particles, the particles are not scattered, and the sieving step can be omitted, so that the product yield is improved. The increase in yield depends on the type and composition of the polymer compound, but can be expected to be about 0.3% to 10%. The granular water-soluble polymer compound coated with hydrophilic silica does not cause mutual adhesion of particles, and improves repose angle and fluidity. For this reason, it retains fluidity during storage and transfer, does not generate "as-is powder" during dissolution, has good workability, and produces little fine powder, so it has excellent effects such as maintaining a good working environment and its value. Is large.

─────────────────────────────────────────────────────
─────────────────────────────────────────────────── ───

【手続補正書】[Procedure amendment]

【提出日】平成3年5月10日[Submission date] May 10, 1991

【手続補正1】[Procedure Amendment 1]

【補正対象書類名】明細書[Document name to be amended] Statement

【補正対象項目名】0007[Correction target item name] 0007

【補正方法】変更[Correction method] Change

【補正内容】[Correction content]

【0007】[0007]

【課題を解決するための手段】本発明は、含有水分3〜
15%、粒径2.0mm以下の粒状水溶性高分子化合物
に一次粒子の平均径5〜50nmで親水性のシリカ0.
1〜5.0重量%を均一に混合し被覆することを特徴と
する粒状水溶性高分子化合物の製造方法にある。
SUMMARY OF THE INVENTION The present invention has a water content of 3 to 3.
15%, granular water-soluble polymer compound having a particle size of 2.0 mm or less, hydrophilic silica with an average primary particle size of 5 to 50 nm .
A method for producing a granular water-soluble polymer compound is characterized in that 1 to 5.0 % by weight is uniformly mixed and coated.

【手続補正2】[Procedure Amendment 2]

【補正対象書類名】明細書[Document name to be amended] Statement

【補正対象項目名】0010[Correction target item name] 0010

【補正方法】変更[Correction method] Change

【補正内容】[Correction content]

【0010】(5)(メタ)アクリルアミドプロピルト
リメチルの3級塩、4級塩
(5) Tertiary salt of (meth) acrylamidopropyltrimethyl, quaternary salt

【化3】(ここでR、RはHまたはCH、XはC
l,Br,1/2SOを表す。)から選ばれる単独重
合体又は共重合体であり、通常微粉状又は微粒子状をな
しており、一般にその粒径は、2mm以下である。
Embedded image (wherein R 3 and R 4 are H or CH 3 , and X is C
1, Br, and 1 / 2SO 4 . 1) is a homopolymer or a copolymer, which is usually in the form of fine powder or fine particles, and generally has a particle size of 2 mm or less.

【手続補正3】[Procedure 3]

【補正対象書類名】明細書[Document name to be amended] Statement

【補正対象項目名】0018[Correction target item name] 0018

【補正方法】変更[Correction method] Change

【補正内容】[Correction content]

【0018】粒状の水溶性高分子化合物は、親水性シリ
カで被覆する前に、液状の消泡剤で処理しておくと本発
明の効果を一層高めることができる。消泡剤を添加被覆
しておくと、親水性シリカとの濡れがよくなり、粒状水
溶性高分子化合物の使用時、煙状となって飛散する微粒
子が発生するのを防止し、作業性、作業環境の改善を果
すことができる。
If the granular water-soluble polymer compound is treated with a liquid defoaming agent before being coated with hydrophilic silica, the effect of the present invention can be further enhanced. When an antifoaming agent is added and coated, the wettability with hydrophilic silica is improved, and when using a granular water-soluble polymer compound, it is possible to prevent generation of fine particles that become smoke-like and scatter, and workability, The working environment can be improved.

【手続補正4】[Procedure amendment 4]

【補正対象書類名】明細書[Document name to be amended] Statement

【補正対象項目名】0028[Correction target item name] 0028

【補正方法】変更[Correction method] Change

【補正内容】[Correction content]

【0028】〔実施例3〕粒状水溶性高分子であるダイ
ヤフロック(株)製凝集剤、KP−500,KP−12
01B,KP−1207B,NP−800,AP−74
1を入手、ウィレ−型粉砕機で2回粉砕し微分の発生す
るサンプルを作り、実施例1で用いたと同じ親水性シリ
カ0.5重量%添加したものと無添加のものとの微粉の
飛散状況を判定した結果を表4に示した。KP500に
ついては親水性シリカを1%添加すれば全く飛散は見ら
れなくなった。
Example 3 Flocculant KP-500, KP-12 manufactured by Diafloc Co., Ltd., which is a granular water-soluble polymer.
01B, KP-1207B, NP-800, AP-74
1 was obtained, and the sample was crushed twice with a Wille-type crusher to produce a sample in which a differential was generated, and the same fine powder as that used in Example 1 with 0.5% by weight of hydrophilic silica added and no added powder scattering The results of judging the situation are shown in Table 4. Completely scattered be added hydrophilic Silica 1% for KP500 was Kuna' such observed.

【手続補正5】[Procedure Amendment 5]

【補正対象書類名】明細書[Document name to be amended] Statement

【補正対象項目名】化3[Name of item to be corrected]

【補正方法】変更[Correction method] Change

【補正内容】[Correction content]

【化3】 [Chemical 3]

【手続補正書】[Procedure amendment]

【提出日】平成6年3月8日[Submission date] March 8, 1994

【手続補正5】[Procedure Amendment 5]

【補正対象書類名】明細書[Document name to be amended] Statement

【補正対象項目名】0010[Correction target item name] 0010

【補正方法】変更[Correction method] Change

【補正内容】[Correction content]

【0010】(5)(メタ)アクリルアミドプロピルト
リメチルの3級塩、4級塩
(5) Tertiary salt of (meth) acrylamidopropyltrimethyl, quaternary salt

【化3】 [Chemical 3]

Claims (3)

【特許請求の範囲】[Claims] 【請求項1】 含有水分3〜15%、粒径2.0mm以
下の粒状水溶性高分子化合物に一次粒子の平均径5〜5
0nmで親水性のシリカ0.1〜5.0重量%を均一に
混合し被覆することを特徴とする粒状水溶性高分子化合
物の製造方法。
1. A granular water-soluble polymer compound having a water content of 3 to 15% and a particle diameter of 2.0 mm or less, and an average diameter of primary particles of 5 to 5
A process for producing a granular water-soluble polymer compound, characterized in that 0.1 to 5.0% by weight of hydrophilic silica at 0 nm is uniformly mixed and coated.
【請求項2】 粒状水溶性高分子化合物の表面を0.0
1〜1.0重量%の液体の消泡剤で被覆した後、親水性
のシリカを混合し被覆することを特徴とする請求項1の
粒状水溶性高分子化合物の製造方法。
2. The surface of the granular water-soluble polymer compound is 0.0
2. The method for producing a granular water-soluble polymer compound according to claim 1, which comprises coating with 1 to 1.0% by weight of a liquid antifoaming agent and then mixing and coating hydrophilic silica.
【請求項3】 粒状水溶性高分子化合物の表面を界面活
性剤の純成分が0.01〜1.0重量%となるように界
面活性剤の水溶液で被覆した後、親水性のシリカを混合
し被覆することを特徴とする請求項1の粒状水溶性高分
子化合物の製造方法。
3. The surface of the granular water-soluble polymer compound is coated with an aqueous solution of a surfactant so that the pure component of the surfactant is 0.01 to 1.0% by weight, and then hydrophilic silica is mixed. The method for producing the granular water-soluble polymer compound according to claim 1, wherein the method is a coating method.
JP03059767A 1991-03-01 1991-03-01 Method for producing granular water-soluble polymer compound Expired - Lifetime JP3113687B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP03059767A JP3113687B2 (en) 1991-03-01 1991-03-01 Method for producing granular water-soluble polymer compound

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP03059767A JP3113687B2 (en) 1991-03-01 1991-03-01 Method for producing granular water-soluble polymer compound

Publications (2)

Publication Number Publication Date
JPH06192432A true JPH06192432A (en) 1994-07-12
JP3113687B2 JP3113687B2 (en) 2000-12-04

Family

ID=13122766

Family Applications (1)

Application Number Title Priority Date Filing Date
JP03059767A Expired - Lifetime JP3113687B2 (en) 1991-03-01 1991-03-01 Method for producing granular water-soluble polymer compound

Country Status (1)

Country Link
JP (1) JP3113687B2 (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2004535167A (en) * 2001-04-02 2004-11-25 ジェネンコー・インターナショナル・インク Granules with reduced potential for dust generation
JP2006111711A (en) * 2004-10-14 2006-04-27 Japan Exlan Co Ltd Flyable fine particle
JP2019522062A (en) * 2016-04-14 2019-08-08 ビーエーエスエフ ソシエタス・ヨーロピアBasf Se Coated polymer particles comprising a water swellable polymer core and a sol-gel coating

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2004535167A (en) * 2001-04-02 2004-11-25 ジェネンコー・インターナショナル・インク Granules with reduced potential for dust generation
JP2006111711A (en) * 2004-10-14 2006-04-27 Japan Exlan Co Ltd Flyable fine particle
JP4752235B2 (en) * 2004-10-14 2011-08-17 日本エクスラン工業株式会社 Flying fine particles
JP2019522062A (en) * 2016-04-14 2019-08-08 ビーエーエスエフ ソシエタス・ヨーロピアBasf Se Coated polymer particles comprising a water swellable polymer core and a sol-gel coating

Also Published As

Publication number Publication date
JP3113687B2 (en) 2000-12-04

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