JPH11156299A - Method for classifying granular hydrophilic polymer and sieve - Google Patents
Method for classifying granular hydrophilic polymer and sieveInfo
- Publication number
- JPH11156299A JPH11156299A JP9329797A JP32979797A JPH11156299A JP H11156299 A JPH11156299 A JP H11156299A JP 9329797 A JP9329797 A JP 9329797A JP 32979797 A JP32979797 A JP 32979797A JP H11156299 A JPH11156299 A JP H11156299A
- Authority
- JP
- Japan
- Prior art keywords
- hydrophilic polymer
- sieving
- sieve
- sieve mesh
- classification
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Pending
Links
Landscapes
- Addition Polymer Or Copolymer, Post-Treatments, Or Chemical Modifications (AREA)
- Combined Means For Separation Of Solids (AREA)
Abstract
Description
【0001】[0001]
【発明の属する技術分野】本発明は、粒子状親水性重合
体の分級方法およびふるい分け装置に関する。さらに詳
しくは、凝集剤、凝結剤、土壌改良剤、土壌安定剤、増
粘剤等に好適に用いられる水溶性重合体や、生理用ナプ
キン、紙おむつ等の衛生材料用吸収剤として、あるいは
農園芸用分野、土木業分野において保水剤、脱水剤等と
して幅広い用途に応用されている吸水性樹脂などの粒子
状親水性重合体を、高い精度で生産性よく粒度分級する
方法および該粒度分級に適したふるい分け装置に関す
る。TECHNICAL FIELD The present invention relates to a method for classifying a particulate hydrophilic polymer and a sieving apparatus. More specifically, as a water-soluble polymer suitably used as a flocculant, a coagulant, a soil conditioner, a soil stabilizer, a thickener, etc., or as an absorbent for sanitary materials such as sanitary napkins, disposable diapers, or agriculture and horticulture. In the field of application and civil engineering, water-retaining agents, dewatering agents, etc., are suitable for wide-ranging applications such as water-absorbent resins, which are widely used as water-absorbing resins, with high accuracy and high productivity. It relates to a sieving device.
【0002】[0002]
【従来の技術】一般に粉粒体の分級操作に際しては、風
力分級やふるい分け等の乾式分級が採用されている。例
えば300μm以下の小さい粉粒体の分級には風力分級
が適しているといわれるが、風力分級には大きい装置が
必要であるという問題がある。一方、ふるい分けは、風
力分級に比較してコンパクトな装置ですむが、例えば3
00μm以下の小さい粉粒体を分級するには分級効率が
低かったり、分級能力が小さくなったりするという問題
がある。2. Description of the Related Art Generally, dry classification such as air classification or sieving is employed in the classification operation of powder and granules. For example, air classification is said to be suitable for classifying small powders of 300 μm or less, but there is a problem that a large apparatus is required for air classification. On the other hand, sieving requires only a device that is more compact than air classification,
There are problems that the classification efficiency is low and the classification ability is low when classifying small powders having a size of 00 μm or less.
【0003】中でも、粒子状親水性重合体を分級する際
に従来の方法でふるい分けを行うと、短時間の操作でふ
るい網面が閉塞し分級効率および分級能力が低下する場
合があった。また、分離粒子径が300μm以下と小さ
い場合には、ふるい網面を通過した細かい粒子径のもの
からなる製品の中に大きな粒子径のものが混入するとい
う問題が生じた。特に近年開発されたアルガイヤ(Al
lgaier)社のタンブラシフタ(Tumbler−
Screening machines)のような、ふ
るい網面を螺旋状に動かすふるい分け装置は分級能力が
高く、細かい粒子の分級に有効なものであるが、かかる
分級能力の高いふるい分け装置ほど上記の問題が顕著で
あり、本来有している高い分級能力を発揮させることが
できないという問題があった。[0003] Above all, when sieving is performed by a conventional method when classifying a particulate hydrophilic polymer, the screen surface of the sieve may be closed by a short operation, and the classification efficiency and the classification capacity may be reduced. Further, when the separation particle size is as small as 300 μm or less, there is a problem that a product having a large particle size is mixed in a product having a fine particle size which has passed through a sieve mesh surface. In particular, Algaia (Al
lgaier) Tumbler lid (Tumbler-
A sieving device that moves a sieving mesh surface in a helical manner, such as a screening machine, has a high classification ability and is effective for classifying fine particles. However, there is a problem that the inherently high classifying ability cannot be exhibited.
【0004】[0004]
【発明が解決しようとする課題】したがって、本発明の
課題は、細かい分離粒子径での分級を効率よく行うこと
ができ、ふるい分け装置の本来有している分級能力を発
揮できるような粒子状親水性重合体の分級方法およびふ
るい分け装置を提供することにある。SUMMARY OF THE INVENTION Accordingly, an object of the present invention is to provide a method for efficiently classifying particles with a fine separation particle diameter and a particle-like hydrophilic particle capable of exhibiting the inherent classification ability of a sieving apparatus. An object of the present invention is to provide a method for classifying a conductive polymer and a sieving apparatus.
【0005】[0005]
【課題を解決するための手段】本発明者らは、粒子状親
水性重合体、特に分離粒子径が小さいものの分級の際に
上記の問題が生じる原因について鋭意検討を重ねた結
果、粒子状親水性重合体に含まれる水分により、ふるい
網面を粒子が通過する前後で凝集物が形成されることを
見出した。すなわち、ふるい網面を通過した粒子状親水
性重合体が、水分によってふるい分け装置の内壁面に付
着し、さらには大きな凝集物を形成し、ふるい分け装置
の振動によって該凝集物が剥がれ落ちるために、分離粒
子径よりも大きな粒子径のものが製品に混入するのであ
る。また、ふるい網面を通過する前に凝集が起きた場合
には、ふるい網面の目づまりの原因となる。Means for Solving the Problems The present inventors have conducted intensive studies on the causes of the above-mentioned problems in the classification of particulate hydrophilic polymers, particularly those having a small separation particle diameter, and as a result, have found that they It has been found that agglomerates are formed before and after the particles pass through the sieve mesh surface due to the moisture contained in the conductive polymer. That is, the particulate hydrophilic polymer that has passed through the sieve mesh surface adheres to the inner wall surface of the sieving device due to moisture, and further forms a large aggregate, and the aggregate is peeled off by the vibration of the sieving device. Particles having a particle size larger than the separated particle size are mixed into the product. In addition, if agglomeration occurs before passing through the sieve mesh surface, it may cause clogging of the sieve mesh surface.
【0006】そこで、本発明者らは、粒子状親水性重合
体に含まれる水分による凝集を抑えるべく粒子状親水性
重合体の温度および粒子状親水性重合体とふるい分け装
置とが接触する面の材質を検討した結果、上記問題点が
改善されることを見出し、本発明に到達した。[0006] In view of the above, the present inventors have studied the temperature of the particulate hydrophilic polymer and the surface of the contact surface between the particulate hydrophilic polymer and the sieving device in order to suppress aggregation due to moisture contained in the particulate hydrophilic polymer. As a result of examining the material, it was found that the above problems were improved, and the present invention was reached.
【0007】すなわち、本発明は粒子状親水性重合体を
ふるい分け装置を用いて乾式粒度分級する方法であっ
て、粒子状親水性重合体の温度が30〜100℃であ
り、ふるい網面以外で粒子状親水性重合体とふるい分け
装置とが接触する面の少なくとも一部が、水に対する接
触角が60度以上で、かつ70℃以上の熱変形温度を有
する材質であることを特徴とする粒子状親水性重合体の
分級方法、および粒子をふるい分けにより乾式粒度分級
する装置であって、ふるい網面以外で粒子とふるい分け
装置とが接触する面の少なくとも一部が、水に対する接
触角が60度以上で、かつ70℃以上の熱変形温度を有
する材質であることを特徴とするふるい分け装置であ
る。That is, the present invention relates to a method for dry particle classification of a particulate hydrophilic polymer using a sieving apparatus, wherein the temperature of the particulate hydrophilic polymer is 30 to 100 ° C. At least a part of the surface where the particulate hydrophilic polymer and the sieving device are in contact with each other is a material having a contact angle with water of 60 ° or more and a heat deformation temperature of 70 ° C or more. A method for classifying a hydrophilic polymer, and a device for dry particle size classification by sieving particles, wherein at least a part of the surface where the particles and the sieving device are in contact other than the sieve mesh surface has a contact angle with water of 60 degrees or more. And a material having a heat distortion temperature of 70 ° C. or more.
【0008】本発明は、ふるい分け装置が、45μm〜
300μmのふるい網目開きのふるい網面を有する場合
に有効である。According to the present invention, the sieving apparatus is preferably used in the range of 45 μm
This is effective when a screen having a sieve mesh opening of 300 μm is used.
【0009】[0009]
【発明の実施の形態】以下、本発明をさらに詳しく説明
する。BEST MODE FOR CARRYING OUT THE INVENTION Hereinafter, the present invention will be described in more detail.
【0010】本発明において粒子状親水性重合体として
は、水溶性の重合性不飽和基含有単量体、例えば、(メ
タ)アクリル酸、(無水)マレイン酸、フマール酸、ク
ロトン酸、イタコン酸、2−(メタ)アクリロイルエタ
ンスルホン酸、2−(メタ)アクリロイルプロパンスル
ホン酸、2−(メタ)アクリルアミド−2−メチルプロ
パンスルホン酸、ビニルスルホン酸、スチレンスルホン
酸、等のアニオン性単量体やその塩、(メタ)アクリル
アミド、N−置換(メタ)アクリルアミド、2−ヒドロ
キシエチル(メタ)アクリレート、2−ヒドロキシプロ
ピル(メタ)アクリレート、メトキシポリエチレングリ
コール(メタ)アクリレート、ポリエチレングリコール
(メタ)アクリレート、等のノニオン性親水性基含有単
量体、N,N−ジメチルアミノエチル(メタ)アクリレ
ート、N,N−ジメチルアミノプロピル(メタ)アクリ
レート、N,N−ジメチルアミノプロピル(メタ)アク
リルアミド、等のアミノ基含有不飽和単量体やそれらの
4級化物等、を重合して得られる水溶性重合体の乾燥粉
砕物や、該水溶性の重合性不飽和基含有単量体と、重合
時に架橋構造を形成させる架橋剤、例えば、分子内に重
合性不飽和二重結合を2個以上有する化合物、水溶性の
不飽和基含有単量体が有する酸基、ヒドロキシル基、ア
ミノ基等の官能基と反応する基を分子内に2個以上有す
る化合物、分子内に不飽和結合および単量体の官能基と
反応する基をそれぞれ1個以上有する化合物、分子内に
単量体の官能基と反応する点を2個以上有する化合物、
または単量体成分が重合する際にグラフト結合等により
架橋構造を形成し得る親水性高分子等とを重合して得ら
れる吸水性樹脂の乾燥粉砕物が挙げられる。これらの粒
子状親水性重合体は、一般に乾燥粉砕物として市販もさ
れており、通常1000μm以下の粒子径を有してい
る。本発明において粒子状とは、任意形状の粒子であれ
ばよく、球状、立方体状、柱状、板状、りんぺん状、棒
状、針状、繊維状、および不定形状等のものが挙げられ
る。本発明における該粒子の粒子径としては、1000
μm以下、好ましくは850μm以下のものを対象とす
る。In the present invention, the particulate hydrophilic polymer includes a water-soluble polymerizable unsaturated group-containing monomer such as (meth) acrylic acid, (anhydride) maleic acid, fumaric acid, crotonic acid, itaconic acid. And anionic monomers such as 2- (meth) acryloylethanesulfonic acid, 2- (meth) acryloylpropanesulfonic acid, 2- (meth) acrylamido-2-methylpropanesulfonic acid, vinylsulfonic acid and styrenesulfonic acid And its salts, (meth) acrylamide, N-substituted (meth) acrylamide, 2-hydroxyethyl (meth) acrylate, 2-hydroxypropyl (meth) acrylate, methoxypolyethylene glycol (meth) acrylate, polyethylene glycol (meth) acrylate, Nonionic hydrophilic group-containing monomers such as N, N-di Amino group-containing unsaturated monomers such as tylaminoethyl (meth) acrylate, N, N-dimethylaminopropyl (meth) acrylate, N, N-dimethylaminopropyl (meth) acrylamide, and quaternized products thereof; And a water-soluble polymer obtained by polymerizing a dried and pulverized product, and the water-soluble polymerizable unsaturated group-containing monomer, and a crosslinking agent that forms a crosslinked structure during polymerization, for example, a polymerizable unsaturated compound in the molecule. Compounds having two or more double bonds, compounds having two or more groups in a molecule that react with functional groups such as an acid group, a hydroxyl group, and an amino group of a water-soluble unsaturated group-containing monomer, A compound having at least one group that reacts with an unsaturated bond and a functional group of a monomer, a compound having two or more points that react with a functional group of a monomer in a molecule,
Alternatively, a dry and pulverized water-absorbent resin obtained by polymerizing a hydrophilic polymer or the like capable of forming a crosslinked structure by graft bonding or the like when a monomer component is polymerized may be used. These particulate hydrophilic polymers are generally commercially available as dry and pulverized products, and usually have a particle size of 1000 μm or less. In the present invention, the particle shape may be any shape particle, and examples include a spherical shape, a cubic shape, a columnar shape, a plate shape, a phosphorus shape, a rod shape, a needle shape, a fiber shape, and an irregular shape. The particle diameter of the particles in the present invention is 1000
μm or less, preferably 850 μm or less.
【0011】本発明は、分級操作の中の粒度分級、すな
わち粉粒体を粒子径によって、二つまたはそれ以上の粒
子群に分ける操作に関するもので、その中の溶剤を用い
ずに分級を行う乾式分級に関するものである。乾式分級
には、主に風力分級とふるい分けとがあるが、本発明は
ふるい網面を有するふるい分け装置を使用する分級操作
に関する。The present invention relates to a particle size classification in a classification operation, that is, an operation of dividing a granular material into two or more particle groups according to a particle diameter, and performs classification without using a solvent therein. It relates to dry classification. Dry classification mainly includes air classification and sieving. The present invention relates to a classification operation using a sieving apparatus having a sieve mesh surface.
【0012】本発明に用いられるふるい分け装置は、ふ
るい網面を有するものであれば特に限定されず、例え
ば、バイブレーティングスクリーンやシフタに分類され
るものが挙げられる。バイブレーティングスクリーンに
は、傾斜形、ローヘッド(Low−head)形、ハム
マー(Hum−mer)、レーブン(Rhewum)、
タイロック(Ty−Rock)、ジャイレックス(Gy
rex)、および楕円振動(Eliptex)等があ
り、シフタにはレシプロ(Reciprocatin
g)形、Exolon−grader、Travers
ator−sieb、Sauer−meyer、ジャイ
レトリーシフタ(Gyratory)、ジャイロシフ
タ、およびローテックススクリーン(Ro−tex)等
がある。これらは、網面の運動形状:円、楕円、直
線、円弧、擬似楕円、スパイラル、振動方式:自由振
動、強制振動、駆動方法:偏心軸、不平衡重錘、電磁
石、インパクト、網面の傾斜:水平式、傾斜式、設
置方法:床置式、吊り下げ式、等によって細分類されて
いる。中でも、アルガイヤ(Allgaier)社のタ
ンブラシフタ(Tumbler−Screening
machines)のように、ラジアル傾斜(中央から
周辺に材料を分散させるふるい網の傾斜)やタンジェン
シャル傾斜(網上の排出スピードをコントロールするふ
るい網の傾斜)の組み合わせによりふるい網面を螺旋状
に動かすふるい分け装置は、比較的細かい粒子の分級に
非常に有効であるが、これを粒子状親水性重合体の分級
に用いると前記の凝集などの問題が顕著で本来有してい
る分級能力を発揮できない。したがって、本発明を適用
することが極めて有効である。タンブラシフタのような
ふるい分け装置に本発明を適用することによって、粒子
状親水性重合体を分級する際にもタンブラシフタ本来の
比較的細かい粒子の分級に有効であるという特徴を発揮
させることができるとともに、ふるい網面の目づまりの
問題や、ふるい網面を通過した粒子がふるい分け装置の
内面側壁に付着し、さらには大きな凝集物を形成し、ふ
るい分け装置の振動によって該凝集物が剥がれ落ち、製
品に混入するという問題を防止することができる。この
ようなふるい分け装置のふるい網面に超音波振動を与え
ることにより、さらに分級効率を高めることができる。The sieving apparatus used in the present invention is not particularly limited as long as it has a sieving screen, and examples thereof include those classified into a vibrating screen and a shifter. The vibrating screen includes an inclined type, a low-head type, a Hum-mer, a Raven,
Tylock (Ty-Rock), Gyrex (Gy)
rex), elliptical vibration (Eliptex), etc., and the shifter is Reciprocatin.
g) Form, Exolon-grader, Travers
Attor-sieb, Sauer-meyer, Gyratory shifter (Gyratory), Gyro shifter, and Lotex screen (Ro-tex). These are the movement shapes of the mesh surface: circle, ellipse, straight line, arc, pseudo-ellipse, spiral, vibration method: free vibration, forced vibration, driving method: eccentric shaft, unbalanced weight, electromagnet, impact, inclination of mesh surface : Horizontal type, inclined type, installation method: It is subdivided into floor type, hanging type, etc. Among them, Tumbler-Screening lid of Allgaier company
helical mesh surface by a combination of radial inclination (inclination of a sieve mesh that disperses material from the center to the periphery) and tangential inclination (inclination of a sieve mesh that controls the discharge speed on the mesh), as in “machines”. The moving sieving apparatus is very effective for classifying relatively fine particles.However, when this is used for classifying a particulate hydrophilic polymer, the problems such as the agglomeration described above are remarkable and the original classifying ability is exhibited. Can not. Therefore, it is extremely effective to apply the present invention. By applying the present invention to a sieving device such as a tan brush lid, it is possible to exhibit the characteristic that the tan brush lid is effective in classifying relatively fine particles inherent in the tan brush lid when classifying the hydrophilic polymer, The problem of clogging of the sieve mesh surface, particles passing through the sieve mesh surface adhere to the inner side wall of the sieving device, and further form large aggregates.The aggregates are peeled off by the vibration of the sieving device and mixed into the product. Can be prevented. By applying ultrasonic vibration to the sieve mesh surface of such a sieving apparatus, the classification efficiency can be further increased.
【0013】本発明は、粒子状親水性重合体の温度が3
0〜100℃であり、ふるい網面以外で粒子状親水性重
合体とふるい分け装置とが接触する面が、水に対する接
触角が60度以上で、かつ70℃以上の熱変形温度を有
する材質であることを必須とする。つまり、ふるい分け
装置の粒子状親水性重合体と接触する部分、特にふるい
網面の側壁を特定の特性を有する材質にすること、およ
び粒子状親水性重合体の温度が30〜100℃に調節す
ることより、粒子状親水性重合体の凝集を抑えられるの
で、ふるい網面の目づまりを有効に防止することがで
き、分級効率および分級能力の低下を防止できる。ま
た、ふるい網面を通過した粒子状親水性重合体が、ふる
い分け装置の内面側壁に付着し、さらには大きな凝集物
を形成し、ふるい分け装置の振動によって該凝集物が剥
がれ落ち、製品に混入するということを防止できる。ふ
るい網ではなく、ふるい網を固定している型わくの側壁
を本発明の材質とすることが好ましく、さらに分級の最
終ふるい網面の側壁の材質を本発明のものとすることが
特に好ましい。In the present invention, the temperature of the particulate hydrophilic polymer is 3
0-100 ° C., and the surface of the non-sieving mesh surface other than the sieve mesh which is in contact with the particulate hydrophilic polymer and the sieving device is made of a material having a contact angle to water of 60 ° or more and a heat deformation temperature of 70 ° C. or more. It is mandatory. In other words, the portion of the sieving device that comes into contact with the particulate hydrophilic polymer, particularly the side wall of the sieve mesh surface, is made of a material having specific characteristics, and the temperature of the particulate hydrophilic polymer is adjusted to 30 to 100 ° C. Accordingly, aggregation of the particulate hydrophilic polymer can be suppressed, so that clogging of the sieve mesh surface can be effectively prevented, and a reduction in classification efficiency and classification ability can be prevented. In addition, the particulate hydrophilic polymer that has passed through the sieve mesh surface adheres to the inner side wall of the sieving device, and further forms large aggregates.The aggregates are peeled off by the vibration of the sieving device and mixed into the product. That can be prevented. It is preferable that the material of the present invention is not the sieve mesh but the side wall of the mold that fixes the sieve mesh, and it is particularly preferable that the material of the side wall of the final screen of the classification is that of the present invention.
【0014】本発明において、粒子状親水性重合体は、
従来公知の方法で加熱することにより30〜100℃の
温度に調整される。該温度が、30℃未満であると、粒
子状親水性重合体同士が凝集しやすくなり、分級操作に
不都合を生じる。一方、100℃を越える温度にして
も、本発明の効果が大きくなるわけではなく、かえっ
て、親水性重合体自体の温度劣化を生じたり、経済的に
不利であるというマイナスになる場合がある。好ましく
は40〜100℃であり、さらに好ましくは40〜90
℃である。In the present invention, the particulate hydrophilic polymer is
The temperature is adjusted to 30 to 100 ° C. by heating by a conventionally known method. If the temperature is lower than 30 ° C., the particulate hydrophilic polymers tend to aggregate with each other, which causes a problem in the classification operation. On the other hand, even if the temperature exceeds 100 ° C., the effect of the present invention is not increased, but rather, the temperature of the hydrophilic polymer itself may be deteriorated, or it may be disadvantageous that it is economically disadvantageous. Preferably it is 40-100 degreeC, More preferably, it is 40-90.
° C.
【0015】本発明において、ふるい網面以外で粒子状
親水性重合体とふるい分け装置とが接触する面が、水に
対する接触角が60度以上で、かつ70℃以上の熱変形
温度を有する材質である。接触面の材質の水に対する接
触角が60度未満であると、粒子状親水性重合体がふる
い分け装置の内面側壁等に付着しやすくなり、分級操作
に不都合をきたす。また、付着した親水性重合体は凝集
し、ふるい分け装置の振動によって該凝集物が剥がれ落
ち、製品に混入するという不都合も生じる。また、接触
面の材質の熱変形温度が70度未満であると、加熱され
温度の高い粒子状親水性重合体の分級操作に耐えられ
ず、そのために安定した分級操作を長時間継続すること
ができなくなる。In the present invention, the surface other than the sieve mesh surface, which is in contact with the particulate hydrophilic polymer and the sieving device, is made of a material having a contact angle with water of 60 ° or more and a heat deformation temperature of 70 ° C. or more. is there. If the contact angle of the material of the contact surface to water is less than 60 degrees, the particulate hydrophilic polymer tends to adhere to the inner side wall of the sieving apparatus, which causes inconvenience in the classification operation. In addition, the attached hydrophilic polymer is aggregated, and the vibration of the sieving device causes the aggregate to be peeled off and mixed into the product. Further, if the thermal deformation temperature of the material of the contact surface is less than 70 degrees, it is not possible to withstand the classification operation of the heated and high-temperature particulate hydrophilic polymer, so that the stable classification operation can be continued for a long time. become unable.
【0016】上記の特性を満足する材質としては、例え
ば、ポリエチレン、ポリプロピレン、ポリエステル、ポ
リアミド、フッ素樹脂、ポリ塩化ビニル、エポキシ樹
脂、およびシリコン樹脂のような合成樹脂、あるいはガ
ラス、グラファイト、ブロンズ、およびモリブデンジサ
ルファイドのような無機充填剤、あるいはポリイミドの
ような有機充填剤で複合体を作り増強した前記合成樹脂
等が挙げられる。中でも、ポリエチレンテトラフルオラ
イド、ポリエチレントリフルオライド、ポリエチレント
リフルオロクロライド、エチレンテトラフルオライド−
エチレンコポリマー、エチレントリフルオロクロライド
−エチレンコポリマー、プロピレンペンタフルオライド
−エチレンテトラフルオライドコポリマー、パーフルオ
ロアルキルビニルエーテル−エチレンテトラフルオライ
ドコポリマー、およびポリフッ化ビニルのようなフッ素
樹脂が特に好ましい。Materials satisfying the above characteristics include, for example, synthetic resins such as polyethylene, polypropylene, polyester, polyamide, fluororesin, polyvinyl chloride, epoxy resin, and silicone resin, or glass, graphite, bronze, and the like. Examples include the above-mentioned synthetic resin in which a composite is formed and strengthened with an inorganic filler such as molybdenum disulfide or an organic filler such as polyimide. Among them, polyethylene tetrafluoride, polyethylene trifluorofluoride, polyethylene trifluorochloride, ethylene tetrafluoride-
Fluororesins such as ethylene copolymers, ethylene trifluorochloride-ethylene copolymers, propylene pentafluoride-ethylene tetrafluoride copolymers, perfluoroalkyl vinyl ether-ethylene tetrafluoride copolymers, and polyvinyl fluoride are particularly preferred.
【0017】本発明において、ふるい分け装置は、加熱
した状態および/または保温した状態で操作されること
がより好ましい。例えば、加熱手段として、電気あるい
は蒸気で加熱できるジャケットを設ける、発熱抵抗体を
巻き付ける等したり、保温手段として断熱材(保温材)
を巻き付ける等することにより該状態を達成できる。In the present invention, it is more preferable that the sieving apparatus is operated in a heated state and / or a warm state. For example, as a heating means, a jacket which can be heated by electricity or steam is provided, a heating resistor is wound, and a heat insulating material (heat insulating material) is used as a heat insulating means.
The above state can be achieved by winding or the like.
【0018】本発明は、45μm〜300μmのふるい
網目開きのふるい網面を有するふるい分け装置に適用す
ることが有効である。粒子状親水性重合体は、その粒子
径が小さくなるにつれてふるい網面を閉塞させやすくな
る傾向があり、分級効率および分級能力を低下させやす
い。また、ふるい網面を通過した粒子状親水性重合体が
ふるい分け装置の内面側壁に付着し、さらには大きな凝
集物を形成し、ふるい分け装置の振動によって該凝集物
が剥がれ落ち、製品に混入するということも起こりやす
い。したがって、本発明は、45μm〜300μmのふ
るい網目開きのふるい網面を有するふるい分け装置に適
用すると効果が著しい。さらには45〜250μmのふ
るい網目開きのふるい網面を有するふるい分け装置に適
用することが有効である。The present invention is effective when applied to a sieving apparatus having a sieve mesh screen having a sieve mesh of 45 μm to 300 μm. As the particle size of the particulate hydrophilic polymer decreases, the sieve mesh surface tends to be easily blocked, and the classification efficiency and the classification ability tend to decrease. In addition, the particulate hydrophilic polymer that has passed through the sieve mesh surface adheres to the inner side wall of the sieving device, further forms large aggregates, and the aggregates are peeled off by the vibration of the sieving device and mixed into the product. Things are easy to happen. Therefore, when the present invention is applied to a sieving apparatus having a sieving screen having a sieve mesh of 45 μm to 300 μm, the effect is remarkable. Further, it is effective to apply the present invention to a sieving device having a sieve mesh surface having a sieve mesh size of 45 to 250 μm.
【0019】粒子状親水性重合体のなかで近年その使用
量が非常に増大している吸水性樹脂において、該吸水性
樹脂中の微粉が、性能面および作業環境面で好ましくな
い成分であることは当業界においてよく知られているこ
とである。したがって、本発明の方法を粒子状吸水性樹
脂の製造プロセスに組み入れることで、大量の製品中か
ら効率よく微粉を除去することができるようになるの
で、その有用性は非常に大きい。In a water-absorbent resin whose use has been greatly increased in recent years among the particulate hydrophilic polymers, the fine powder in the water-absorbent resin is an unfavorable component in terms of performance and working environment. Is well known in the art. Therefore, by incorporating the method of the present invention into a process for producing a particulate water-absorbent resin, fine powder can be efficiently removed from a large amount of products, and its utility is extremely large.
【0020】本発明にかかるふるい分け装置は前述の特
定の特性を有する材質を備えるものであり、上記の粒子
状親水性重合体の分級方法に有効であるが、他の従来公
知の粉粒体全ての分級にも好ましく使用することができ
る。例えば、小麦製粉等の穀類、肥料等の農薬品、医薬
品、セラミックス、セメント、炭酸カルシウム等の無機
塩類、染料、顔料、樹脂ペレット等が挙げられる。The sieving apparatus according to the present invention is provided with a material having the above-mentioned specific properties, and is effective for the above-mentioned method for classifying a particulate hydrophilic polymer. Can also be used preferably for classification. Examples include grains such as wheat flour, agricultural chemicals such as fertilizers, pharmaceuticals, ceramics, cement, inorganic salts such as calcium carbonate, dyes, pigments, resin pellets, and the like.
【0021】なお、本発明における接触角は、接触角計
CA−DT−A型(協和界面科学株式会社製)を使用
し、液適法にて計測した。また、熱変形温度は、ASTM
D−648(4.6kg/cm2)の方法により計測
した。The contact angle in the present invention was measured by a liquid angle method using a contact angle meter CA-DT-A (manufactured by Kyowa Interface Science Co., Ltd.). The heat distortion temperature is ASTM
It was measured by the method of D-648 (4.6 kg / cm2).
【0022】[0022]
【実施例】以下、実施例および比較例により本発明をさ
らに詳細に説明するが、本発明はこれに限定されるもの
ではない。The present invention will be described in more detail with reference to the following Examples and Comparative Examples, but the present invention is not limited thereto.
【0023】実施例1 アクリル酸およびアクリル酸ナトリウムとトリメチロー
ルプロパントリアクリレートとを水溶液重合し、得られ
た含水ゲル状重合体を乾燥粉砕して、平均粒子径300
μmの吸水性樹脂粉末を得た。Example 1 Acrylic acid, sodium acrylate and trimethylolpropane triacrylate were polymerized in an aqueous solution, and the resulting hydrogel polymer was dried and pulverized to give an average particle diameter of 300.
As a result, a water-absorbent resin powder of μm was obtained.
【0024】約40℃の吸水性樹脂粉末を、100kg
/hでふるい分け装置に供給した。ふるい分け装置とし
ては、ふるい網目開き850μmのふるい網面と210
μmのふるい網面とを重ねたふるい分け装置(タンブラ
シフタTSM−1600・Allgaier社製)を用
いた。ふるい分け装置と吸水性樹脂粉末とが接触するふ
た、ふるい網枠、および底部をチューコーフロー粘着テ
ープAGF-100(中興化成工業株式会社製、フッ素樹脂(ホ゜リ
テトラフルオロエチレン 接触角114度、熱変形温度121℃)
とカ゛ラスクロスからなる粘着テーフ゜)で覆った。8時間の分級
操作中にトラブルはなく、ふるい網目開き210μmの
ふるい網面を通過した吸水性樹脂粉末の製品が得られ
た。ふるい網側壁およびふるい網への付着はほとんど見
られず、分級後の製品に凝集物の混入もなかった。100 kg of the water-absorbent resin powder at about 40 ° C.
/ H to the sieving apparatus. As the sieving device, a sieving mesh surface having a sieve mesh opening of 850 μm and a
A sieving apparatus (tan brush lid TSM-1600, manufactured by Allgaier) having a mesh screen of μm was used. The lid, sieve mesh frame, and bottom part where the sieving device and the water-absorbent resin powder are in contact with each other are coated with Chukoh Flow adhesive tape AGF-100 (manufactured by Chuko Kasei Kogyo Co., Ltd. 121 ° C)
And an adhesive tape made of glass cloth. There was no trouble during the classifying operation for 8 hours, and a product of the water-absorbent resin powder which passed through the sieve mesh having a sieve mesh of 210 μm was obtained. Almost no adhesion to the sieve mesh side wall and sieve mesh was observed, and the classified product was free of aggregates.
【0025】比較例1 実施例1において、チューコーフロー粘着テープAGF-10
0を用いないふるい分け装置を使用し、20℃の吸水性
樹脂粉末を供給した以外は実施例1と同様の操作を行っ
た。ふるい網側壁およびふるい網への付着が見られ、分
級後の製品に凝集物が混入していた。Comparative Example 1 In Example 1, Chukoh Flow adhesive tape AGF-10
The same operation as in Example 1 was performed except that a water-absorbing resin powder at 20 ° C. was supplied using a sieving apparatus not using 0. Adhesion to the sieve mesh side wall and the sieve mesh was observed, and aggregates were mixed in the classified product.
【0026】[0026]
【発明の効果】本発明によると、粒子状親水性重合体の
分級に際し、ふるい網面が閉塞して分級効率や分級能力
が低下するという問題が生じない。また、分離粒子径が
200μm以下と小さい場合にも、ふるい網面を通過し
た細かい粒子状親水性重合体がふるい分け装置の内壁面
に付着し、さらには大きな凝集物を形成し、ふるい分け
装置の振動によって該凝集物が剥がれ落ちるために、分
離粒子径よりも大きな粒子径のものが製品に混入すると
いう問題も生じない。したがって、従来安定した分級が
困難であった分離粒子径での分級が極めて効率よく行
え、ふるい分け装置の本来有している分級能力を十分に
発揮できる。According to the present invention, when classifying a particulate hydrophilic polymer, there is no problem that the sieve mesh surface is closed and the classification efficiency and the classification ability are reduced. Further, even when the separation particle diameter is as small as 200 μm or less, the fine particulate hydrophilic polymer that has passed through the sieve mesh surface adheres to the inner wall surface of the sieving device, further forms large aggregates, and the vibration of the sieving device As a result, the aggregates are peeled off, so that there is no problem that particles having a particle size larger than the separation particle size are mixed into the product. Therefore, classification at the separation particle diameter, which has conventionally been difficult to classify stably, can be performed very efficiently, and the classification capability inherent in the sieving apparatus can be sufficiently exhibited.
Claims (3)
用いて乾式粒度分級する方法であって、粒子状親水性重
合体の温度が30〜100℃であり、ふるい網面以外で
粒子状親水性重合体とふるい分け装置とが接触する面の
少なくとも一部が、水に対する接触角が60度以上で、
かつ70℃以上の熱変形温度を有する材質であることを
特徴とする粒子状親水性重合体の分級方法。1. A method of dry-type particle classification of a particulate hydrophilic polymer using a sieving apparatus, wherein the temperature of the particulate hydrophilic polymer is 30 to 100 ° C. At least a part of the surface where the conductive polymer and the sieving device are in contact, the contact angle with water is 60 degrees or more,
And a material having a heat distortion temperature of 70 ° C. or more.
mのふるい網目開きのふるい網面を有する請求項1に記
載の粒子状親水性重合体の分級方法。2. The method according to claim 1, wherein the sieving apparatus has a size of 45 μm to 300 μm.
The method for classifying a particulate hydrophilic polymer according to claim 1, which has a sieve mesh screen having a sieve mesh opening of m.
る装置であって、ふるい網面以外で粒子とふるい分け装
置とが接触する面の少なくとも一部が、水に対する接触
角が60度以上で、かつ70℃以上の熱変形温度を有す
る材質であることを特徴とするふるい分け装置。3. An apparatus for classifying dry particles by sieving, wherein at least a part of a surface other than a sieve mesh surface where the particles come into contact with the sieving apparatus has a contact angle with water of 60 degrees or more and 70% or more. A sieving apparatus characterized by being made of a material having a heat distortion temperature of at least ℃.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP9329797A JPH11156299A (en) | 1997-12-01 | 1997-12-01 | Method for classifying granular hydrophilic polymer and sieve |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP9329797A JPH11156299A (en) | 1997-12-01 | 1997-12-01 | Method for classifying granular hydrophilic polymer and sieve |
Publications (1)
Publication Number | Publication Date |
---|---|
JPH11156299A true JPH11156299A (en) | 1999-06-15 |
Family
ID=18225369
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP9329797A Pending JPH11156299A (en) | 1997-12-01 | 1997-12-01 | Method for classifying granular hydrophilic polymer and sieve |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH11156299A (en) |
Cited By (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO2010032694A1 (en) | 2008-09-16 | 2010-03-25 | 株式会社日本触媒 | Water-absorbent resin manufacturing method and liquid permeability improvement method |
WO2011034147A1 (en) | 2009-09-16 | 2011-03-24 | 株式会社日本触媒 | Method for producing water absorbent resin powder |
WO2011115216A1 (en) | 2010-03-17 | 2011-09-22 | 株式会社日本触媒 | Method of producing absorbent resin |
JP2012519737A (en) * | 2009-02-18 | 2012-08-30 | ビーエーエスエフ ソシエタス・ヨーロピア | Method for producing water-absorbing polymer particles |
US8946305B2 (en) | 2011-12-22 | 2015-02-03 | Industrial Technology Research Institute | Method for crosslinking a colloid, and crosslinked colloid therefrom |
US10099254B2 (en) | 2007-03-26 | 2018-10-16 | Nippon Shokubai Co., Ltd. | Classification method of particulate water absorbent resin |
-
1997
- 1997-12-01 JP JP9329797A patent/JPH11156299A/en active Pending
Cited By (12)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US10099254B2 (en) | 2007-03-26 | 2018-10-16 | Nippon Shokubai Co., Ltd. | Classification method of particulate water absorbent resin |
WO2010032694A1 (en) | 2008-09-16 | 2010-03-25 | 株式会社日本触媒 | Water-absorbent resin manufacturing method and liquid permeability improvement method |
JP2012519737A (en) * | 2009-02-18 | 2012-08-30 | ビーエーエスエフ ソシエタス・ヨーロピア | Method for producing water-absorbing polymer particles |
WO2011034147A1 (en) | 2009-09-16 | 2011-03-24 | 株式会社日本触媒 | Method for producing water absorbent resin powder |
WO2011034146A1 (en) | 2009-09-16 | 2011-03-24 | 株式会社日本触媒 | Method for producing water absorbent resin powder |
WO2011115216A1 (en) | 2010-03-17 | 2011-09-22 | 株式会社日本触媒 | Method of producing absorbent resin |
WO2011115221A1 (en) | 2010-03-17 | 2011-09-22 | 株式会社日本触媒 | Method of producing absorbent resin |
JP5739412B2 (en) * | 2010-03-17 | 2015-06-24 | 株式会社日本触媒 | Method for producing water absorbent resin |
JP5744840B2 (en) * | 2010-03-17 | 2015-07-08 | 株式会社日本触媒 | Method for producing water absorbent resin |
US9453091B2 (en) | 2010-03-17 | 2016-09-27 | Nippon Shokubai Co., Ltd. | Method of producing water absorbent resin |
US9624322B2 (en) | 2010-03-17 | 2017-04-18 | Nippon Shukubai Co., Ltd. | Method of producing water absorbent resin |
US8946305B2 (en) | 2011-12-22 | 2015-02-03 | Industrial Technology Research Institute | Method for crosslinking a colloid, and crosslinked colloid therefrom |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
JP3875757B2 (en) | Method for classifying particulate hydrophilic polymer and sieving device | |
JP5871803B2 (en) | Post-humidification method for surface post-crosslinked water-absorbing polymer particles | |
JP6157534B2 (en) | Classification method of water-absorbing polymer particles | |
JP5766913B2 (en) | Classification method of water-absorbing polymer particles | |
CN100448919C (en) | Method for production of water-absorbent resin and plow-shaped mixing device | |
CN102898662B (en) | Production method for water-absorbing resin composition | |
EP0450922B1 (en) | Method for production of fluid stable aggregate | |
JP5383647B2 (en) | Method for coating water-absorbing polymer particles | |
JP6577572B2 (en) | Method for producing particulate water-absorbing agent mainly composed of polyacrylic acid (salt) water-absorbing resin | |
JPH04214734A (en) | Method for carrying out surface treatment of water-absorbing resin | |
JPH09235378A (en) | Water-absorbing agent, its production and production apparatus therefor | |
JP2004300425A (en) | Process for surface crosslinking treatment of water-absorbing resin powder | |
WO2011099586A1 (en) | Process for producing water-absorbing resin powder | |
JP3016879B2 (en) | Method for producing superabsorbent resin | |
CN1572818A (en) | Method for sizing of water-absorbent resin | |
JP2004002145A (en) | Mixture of hydrogel forming polymer and building material | |
JP5850841B2 (en) | Post-humidification method for surface post-crosslinked water-absorbing polymer particles | |
JPH11156299A (en) | Method for classifying granular hydrophilic polymer and sieve | |
CN1105925A (en) | Process for granulating highly water-absorptive resin | |
JP2004352941A (en) | Preparation process of water-absorbing resin | |
TWI806887B (en) | Classification process for superabsorbent polymer particles | |
JP3970818B2 (en) | Granulated particles of water absorbent resin, absorbent article containing the same, and method for producing granulated particles of water absorbent resin | |
JP5150717B2 (en) | Method for coating water-absorbing polymer particles | |
JP5150718B2 (en) | Method for coating water-absorbing polymer particles | |
CN104411731A (en) | Method for the production of water-absorbing polymer particles |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
FPAY | Renewal fee payment (prs date is renewal date of database) |
Free format text: PAYMENT UNTIL: 20080908 Year of fee payment: 8 |
|
FPAY | Renewal fee payment (prs date is renewal date of database) |
Free format text: PAYMENT UNTIL: 20080908 Year of fee payment: 8 |
|
FPAY | Renewal fee payment (prs date is renewal date of database) |
Free format text: PAYMENT UNTIL: 20090908 Year of fee payment: 9 |
|
FPAY | Renewal fee payment (prs date is renewal date of database) |
Year of fee payment: 9 Free format text: PAYMENT UNTIL: 20090908 |
|
FPAY | Renewal fee payment (prs date is renewal date of database) |
Year of fee payment: 10 Free format text: PAYMENT UNTIL: 20100908 |
|
FPAY | Renewal fee payment (prs date is renewal date of database) |
Year of fee payment: 11 Free format text: PAYMENT UNTIL: 20110908 |
|
FPAY | Renewal fee payment (prs date is renewal date of database) |
Free format text: PAYMENT UNTIL: 20120908 Year of fee payment: 12 |
|
FPAY | Renewal fee payment (prs date is renewal date of database) |
Year of fee payment: 13 Free format text: PAYMENT UNTIL: 20130908 |