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JPS5815481B2 - Method for producing water-soluble polymer gel - Google Patents
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JPS5815481B2 - Method for producing water-soluble polymer gel - Google Patents

Method for producing water-soluble polymer gel

Info

Publication number
JPS5815481B2
JPS5815481B2 JP49146877A JP14687774A JPS5815481B2 JP S5815481 B2 JPS5815481 B2 JP S5815481B2 JP 49146877 A JP49146877 A JP 49146877A JP 14687774 A JP14687774 A JP 14687774A JP S5815481 B2 JPS5815481 B2 JP S5815481B2
Authority
JP
Japan
Prior art keywords
polymerization
polymer
gel
soluble polymer
wall
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.)
Expired
Application number
JP49146877A
Other languages
Japanese (ja)
Other versions
JPS5173583A (en
Inventor
禎彦 安藤
昭 矢田
寛 秋野
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.)
Toagosei Co Ltd
Original Assignee
Toagosei Co Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Toagosei Co Ltd filed Critical Toagosei Co Ltd
Priority to JP49146877A priority Critical patent/JPS5815481B2/en
Publication of JPS5173583A publication Critical patent/JPS5173583A/en
Publication of JPS5815481B2 publication Critical patent/JPS5815481B2/en
Expired legal-status Critical Current

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  • Physical Or Chemical Processes And Apparatus (AREA)
  • Polymerisation Methods In General (AREA)

Description

【発明の詳細な説明】 本発明は水溶性ポリマーゲルの製造方法に係るもので、
その目的は剥離性の追好な重合器材質を使用して水溶性
ポリマーゲルの製造を容易ならしめんとするものである
[Detailed Description of the Invention] The present invention relates to a method for producing a water-soluble polymer gel.
The purpose is to facilitate the production of a water-soluble polymer gel by using a polymerizer material with good peelability.

高い重合度のアクリル酸塩メタクリル酸塩もしくはアク
リルアミド等を含む高濃度の含水重合体は通常ゴム弾性
を有するゲルとして得られる。
A highly concentrated water-containing polymer containing a high degree of polymerization such as acrylate, methacrylate or acrylamide is usually obtained as a gel having rubber elasticity.

重合体は重合の進行と共にわずかに収縮するが重合完結
時には重合器壁と完全に密着する。
The polymer shrinks slightly as the polymerization progresses, but when the polymerization is completed, it completely adheres to the wall of the polymerization vessel.

この密着面積が犬となるにつれゲル状重合体を重合器壁
から剥離することは次第に困難となり、密着面積が大き
くなると重合器とゲル体の剥離はほとんど不可能である
As the adhesion area increases, it becomes increasingly difficult to separate the gel-like polymer from the wall of the polymerization vessel, and as the adhesion area increases, it becomes almost impossible to separate the gel body from the polymerization vessel.

本発明者らはこの点に関する各種材質のテストを実施し
た結果ナイロン及び含弗素樹脂のいずれかで被覆した金
属を使用した場合にのみ極めて容易に剥離が容易に行わ
れることを見出して本発明を完成したのである。
The present inventors conducted tests on various materials in this regard, and found that peeling was extremely easy only when using metal coated with either nylon or fluorine-containing resin, and developed the present invention. It was completed.

通常これらポリマーゲルと重合器壁との間には少しも間
隙はなく密着しているが、ゲルと器壁との接着強度は弱
い。
Usually, these polymer gels and the wall of the polymerization vessel are in close contact with each other without any gaps, but the adhesive strength between the gel and the wall of the vessel is weak.

したがって密着面積の小さい小型重合器に於てはゲルと
器壁との剥離は容易であるから問題はない。
Therefore, in a small polymerization vessel with a small adhesion area, there is no problem because the gel and vessel wall can easily be peeled off.

しかるにポリマーゲルを工業的に大規模に製造する場合
に於ては、この密着性は装置上極めて困難な問題を提起
する。
However, when producing polymer gels on a large scale industrially, this adhesion poses extremely difficult equipment problems.

即ち重合体が流動性のないゲルを形成する場合ゲルの熱
伝導度が低いためにゲル内部には重合熱が著積して高温
となり、重合度が低下し、あるいは重合率が低下する。
That is, when a polymer forms a gel with no fluidity, the thermal conductivity of the gel is low, so the heat of polymerization accumulates inside the gel, resulting in a high temperature, resulting in a decrease in the degree of polymerization or a decrease in the polymerization rate.

これをさけるために重合器の伝熱面積を大きくすること
は、不可欠であり、通常その伝熱面積は重合体ゲル単位
立方米当り、20〜40平方米にも達する。
In order to avoid this, it is essential to increase the heat transfer area of the polymerization vessel, and usually the heat transfer area reaches 20 to 40 square meters per unit cubic meter of polymer gel.

このような壁面積を有する重合器に於て重合体と器壁が
わずかに接着するとその剥離は至難であり、強い力で強
制的に剥離を行えばゴム弾性を有する重合体は母材破壊
して一部が器壁に残りくりかえし操作に重大な支障とな
り、工業的装置として使用に耐えないものとなる。
In a polymerization vessel with such a wall area, if the polymer and the vessel wall are slightly adhered, it is extremely difficult to separate them, and if the polymer is forcibly removed with strong force, the rubber-elastic polymer will break the base material. A part of the product remains on the wall of the container, causing a serious hindrance to repeated operations, making it unusable as an industrial device.

本発明者らはこの問題を解決するべく、多方面にわたる
検討の結果、重合器の壁材としてナイロンもしくは弗素
含有樹脂で被覆せしめた金属板を使用して構成した重合
装置にあっては、特異的にポリマーゲルの剥離が容易に
行われ、かつくりかえし使用に当って何ら支障なく、重
合操作が実施出来ることを見出した。
In order to solve this problem, the present inventors conducted extensive studies and found that a polymerization apparatus using a metal plate coated with nylon or fluorine-containing resin as the wall material of the polymerization vessel has a unique feature. It has been found that the polymer gel can be easily peeled off, and that the polymerization operation can be carried out without any problems when reusing it.

本発明者らは多くの材質について工業的規模でテストを
実施したが、本発明の効果は実施例にも示される如く極
めて著しいものである。
The present inventors have conducted tests on many materials on an industrial scale, and the effects of the present invention are extremely remarkable, as shown in the Examples.

ナイロン及び弗素含有樹脂が特異的に良好な剥離性をま
ず理由は必ずしも明確ではないが両者共、これに密着す
るポリマーゲル表面に極めて薄い低重合ポリマ一層を生
じ、これがゲルと器壁との間で潤滑剤として作用してい
るところから見て樹脂表面に吸着もしくは吸蔵された微
量の酸素が器壁界面での七ツマ−の重合を阻害し、この
結果、すぐれた剥離効果が得られるものと推定される。
The reason why nylon and fluorine-containing resin have particularly good releasability is not necessarily clear, but both produce an extremely thin layer of low polymerization polymer on the surface of the polymer gel that adheres to it, and this creates a layer of low polymerization between the gel and the vessel wall. The small amount of oxygen adsorbed or occluded on the resin surface, acting as a lubricant, inhibits the polymerization of the 7-mer at the vessel wall interface, resulting in an excellent peeling effect. Presumed.

これに対し器壁界面に多くの酸素が存在する壁材、たと
えば独立微小気泡を有するポリエチレン粉体塗装ライニ
ングでは器壁附近におけるモノマーの重合速度が遅く厚
さ2〜3mmにわたって高度の粘着性を有する液として
残るためゲルの剥離は困難となり、また壁材がステンレ
ス鋼板の場合にはモノマーは器壁界面でも重合して高重
合度ポリマーとなるため強く接着するものと考えられ、
又シリコン樹脂被膜のステンレス鋼板への焼付けの場合
にはこの被膜自体が剥離し易く、繰返しの使用に困難性
がある。
On the other hand, in wall materials where a large amount of oxygen exists at the vessel wall interface, such as polyethylene powder coating lining with closed microbubbles, the polymerization rate of the monomer near the vessel wall is slow, resulting in a high degree of stickiness over a thickness of 2 to 3 mm. It is difficult to remove the gel because it remains as a liquid, and if the wall material is a stainless steel plate, the monomer polymerizes at the wall interface as well, forming a highly polymerized polymer, which is thought to cause strong adhesion.
Furthermore, when a silicone resin coating is baked onto a stainless steel plate, the coating itself tends to peel off, making repeated use difficult.

本発明方法はアクリル酸、メタクリル酸及びそれらのア
ルカリ金属塩もしくはアンモニウム塩やアクリルアミド
等の水溶性モノマーの重合に有用であり、これらは凝集
剤、増粘剤、沈降剤等の用途に不可欠のものである。
The method of the present invention is useful for the polymerization of water-soluble monomers such as acrylic acid, methacrylic acid, their alkali metal or ammonium salts, and acrylamide, which are essential for use as flocculants, thickeners, sedimentation agents, etc. It is.

これらの重合に於て重合中の重合体温度は低い方が好ま
しいが、極度に低い場合は重合速度が低下するから、概
ね50℃以上が好ましい。
In these polymerizations, the polymer temperature during polymerization is preferably low, but if it is extremely low, the polymerization rate will decrease, so it is preferably about 50° C. or higher.

モノマー濃度が高くなるにつれて許容される上限温度も
高くなるが濃度35係のモノマー水溶液の重合において
は概ね85℃以下が好ましく、これ以上では高重合度の
重合体は得られない。
As the monomer concentration increases, the allowable upper limit temperature also increases, but in the case of polymerizing an aqueous monomer solution with a concentration of 35%, it is generally preferred to be 85° C. or lower, and a polymer with a high degree of polymerization cannot be obtained above this temperature.

したがって重合器材質としては剥離性と共は伝熱性が良
好であることは不可欠である。
Therefore, it is essential that the polymerization vessel material has good heat transfer properties as well as peelability.

以下に実施例及び比較例を掲げて説明する。Examples and comparative examples will be described below.

実施例及び比較例 組立てによって形成された内部が下記材料の被膜で形成
された(被膜無処理の場合も含む)交換可能な二枚の1
000mmX1000mm100Oの側板と、七ツマー
注入口を具えた厚さ50mm巾60mmの鉄製枠を組立
て、中空で偏平な1000mmX1000mmX100
Oの箱を構成し、鉄製枠の1端を下に注入口が上部にく
るよう垂直に固定した。
Example and Comparative Example Two replaceable sheets 1 whose interior formed by assembling was formed with a coating of the following material (including cases without coating)
Assemble a 50mm thick and 60mm wide iron frame with a side plate of 000mm x 1000mm x 100mm and a seven-piece inlet to form a hollow, flat 1000mm x 1000mm x 100mm.
A box of O was constructed, and one end of the iron frame was fixed vertically so that the injection port was at the top.

内部を高純度N2ガスで充したのち、予め十分に脱酸素
し過硫酸アンモニウム50ppmを含む20係アクリル
酸ナトリウム、15%のアクリルアミドを含む水溶液8
0kgを仕込んで重合中は両側板に20℃の冷却水を全
面に吹きつけつつ重合せしめ重合完了後一方の側板を理
解して重合体から入力で引きはがした。
After filling the interior with high-purity N2 gas, the aqueous solution 8 containing 20% sodium acrylate containing 50 ppm of ammonium persulfate and 15% acrylamide was sufficiently deoxidized in advance.
0 kg was charged, and during polymerization, cooling water at 20° C. was sprayed over the entire surface of both side plates, and after polymerization was completed, one side plate was separated from the polymer by input.

この時の剥離状況を下記に示す。(す)のライニング厚
みは0.03mmであった。
The peeling situation at this time is shown below. The lining thickness of (S) was 0.03 mm.

剥離性評価結果のうち ×は1人の人力によって剥離が不可能であったことを示
す。
Among the peelability evaluation results, × indicates that peeling was impossible by one person's manual labor.

△は人力による剥離は可能であるが重合器を45°に傾
けた状態で自然剥離が起らないことを示す。
△ indicates that manual peeling is possible, but natural peeling does not occur when the polymerization vessel is tilted at 45°.

■は重合器を45度に傾斜せしめるだけで自然に剥離す
ることを示す。
(2) indicates that the polymer peels off naturally simply by tilting the polymerization vessel at 45 degrees.

Claims (1)

【特許請求の範囲】[Claims] 1 仕込み水溶性単量体水溶液との接触部がナイロンも
しくは弗素含有樹脂で被覆された金属よりなる重合装置
を使用して前記水溶性単量体の水溶液重合を行うことを
特徴とする水溶性ポリマーゲルの製造方法。
1. A water-soluble polymer characterized in that the aqueous solution polymerization of the water-soluble monomer is carried out using a polymerization apparatus in which the contact portion with the charged water-soluble monomer aqueous solution is made of nylon or a metal coated with a fluorine-containing resin. Method of manufacturing gel.
JP49146877A 1974-12-23 1974-12-23 Method for producing water-soluble polymer gel Expired JPS5815481B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP49146877A JPS5815481B2 (en) 1974-12-23 1974-12-23 Method for producing water-soluble polymer gel

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP49146877A JPS5815481B2 (en) 1974-12-23 1974-12-23 Method for producing water-soluble polymer gel

Publications (2)

Publication Number Publication Date
JPS5173583A JPS5173583A (en) 1976-06-25
JPS5815481B2 true JPS5815481B2 (en) 1983-03-25

Family

ID=15417576

Family Applications (1)

Application Number Title Priority Date Filing Date
JP49146877A Expired JPS5815481B2 (en) 1974-12-23 1974-12-23 Method for producing water-soluble polymer gel

Country Status (1)

Country Link
JP (1) JPS5815481B2 (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2006199862A (en) * 2005-01-21 2006-08-03 Nippon Shokubai Co Ltd Method for producing water absorbent resin

Families Citing this family (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE3222002A1 (en) * 1982-06-11 1983-12-15 Röhm GmbH, 6100 Darmstadt CONTINUOUS EMULSION POLYMERIZATION PROCESS
JPS59168007A (en) * 1983-03-15 1984-09-21 Mitsui Toatsu Chem Inc Production of vinyl chloride resin
DE3773189D1 (en) * 1987-03-25 1991-10-24 Sekisui Chemical Co Ltd RESIN FOR USE ON MAGNETIC RECORDING CARRIERS AND METHOD FOR THE PRODUCTION THEREOF.
US5028676A (en) * 1989-06-26 1991-07-02 Sekisui Kagaku Kogyo Kabushiki Kaisha Resin for magnetic recording media from vinyl chloride with quanternary and phosphoric monomers

Family Cites Families (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS506346B2 (en) * 1972-01-14 1975-03-13

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2006199862A (en) * 2005-01-21 2006-08-03 Nippon Shokubai Co Ltd Method for producing water absorbent resin

Also Published As

Publication number Publication date
JPS5173583A (en) 1976-06-25

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