JPH01165572A - Treatment of polymerizable powder - Google Patents

Treatment of polymerizable powder

Info

Publication number
JPH01165572A
JPH01165572A JP32281487A JP32281487A JPH01165572A JP H01165572 A JPH01165572 A JP H01165572A JP 32281487 A JP32281487 A JP 32281487A JP 32281487 A JP32281487 A JP 32281487A JP H01165572 A JPH01165572 A JP H01165572A
Authority
JP
Japan
Prior art keywords
powder
water
polymerizable
maleimide derivative
suspension
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Pending
Application number
JP32281487A
Other languages
Japanese (ja)
Inventor
Hideki Watabe
秀樹 渡部
Takeshi Ota
大田 毅
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.)
Denka Co Ltd
Original Assignee
Denki Kagaku Kogyo 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 Denki Kagaku Kogyo KK filed Critical Denki Kagaku Kogyo KK
Priority to JP32281487A priority Critical patent/JPH01165572A/en
Publication of JPH01165572A publication Critical patent/JPH01165572A/en
Pending legal-status Critical Current

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  • Addition Polymer Or Copolymer, Post-Treatments, Or Chemical Modifications (AREA)

Abstract

PURPOSE:To prevent various defects of powder, by suspending a maleimide derivative of polymerizable powder having no ring opening properties through hydrolysis with water into water in a specific blending ratio and transporting or weighing the polymerizable polymer as an inert and stable suspension. CONSTITUTION:A maleimide derivative shown by the formula (R1 and R2 are H, 1-4C alkyl, halogen or 1-4C halogenated alkyl; R2 is 1-12C alkyl, cycloalkyl or phenyl containing nonhydrolyzable substituent group) is dispersed into water in the ratio of 5-200 pts.wt., preferably 10-100 pts.wt. maleimide derivative based on 100 pts.wt. water to form a suspension, which is transported or weighed in a suspended state so that the polymerizable powder is treated. The method is used for raw material powder of heat-resistant plastic resin especially applicable to molding method such as injection molding or extrusion molding. Pollution of operation environment resulting from scattering of powder or toxicity is prevented and generation of static electricity is prevented.

Description

【発明の詳細な説明】 [産業上の利用分野] 本発明は重合性粉体の処理方法に関し、特に射出成形、
押出成形等の成形法に適用される耐熱性熱可塑性樹脂の
製造原料として用いられる重合性粉体の処理方法に関す
るものである。
[Detailed Description of the Invention] [Industrial Application Field] The present invention relates to a method for treating polymerizable powder, particularly injection molding,
The present invention relates to a method for treating polymerizable powder used as a raw material for producing heat-resistant thermoplastic resins applied to molding methods such as extrusion molding.

[従来の技術] 従来、耐熱性を向上した熱可塑性樹脂としてイミド化ポ
リマーかよく利用されている。具体的には、マレイミド
系誘導体単位をスチレン、メタクリル酸メチル、)!!
化ヒビニルのビニル系モノマーとJ(重合せしめたイミ
ド化ポリマーが用いられている。このようなイミド化ポ
リマーの製造方法としては、例えば無水マレイン酸とス
チレンを共重合し、アニリン等てイミド化する方法(特
公昭6O−4S642す公報)、および千ツマ−として
イミド化上ツマ−をそのまま共重合させる方法(特開昭
58−225145号公報)の2つの方法が報告されて
いる。
[Prior Art] In the past, imidized polymers have often been used as thermoplastic resins with improved heat resistance. Specifically, the maleimide derivative unit is styrene, methyl methacrylate, )! !
An imidized polymer obtained by polymerizing a vinyl monomer of vinyl chloride with J (J) is used. As a method for producing such an imidized polymer, for example, maleic anhydride and styrene are copolymerized, and then imidized with aniline, etc. Two methods have been reported: a method (Japanese Patent Publication No. 6O-4S642), and a method of directly copolymerizing an imidized polymer (Japanese Unexamined Patent Publication No. 58-225145).

しかるに、前者の方法ては、最初に共重合工程を行ない
、その後にイミド化工程を行なう必要かあるために、工
程が複雑となり、生産性が低下する欠点がある。
However, the former method requires a copolymerization step first and then an imidization step, which complicates the process and reduces productivity.

他方、後者のイミド化上ツマ−をそのまま共重合せしめ
る方法では、イミド化モノマー中の重合性粉体の取り扱
い等の処理方法において欠点がある。すなわち、一般に
マレイミド系誘導体の七ツマ−は粉体であり、工業スケ
ールでこのようなモノマーを正確に計量し、その後重合
缶に投入するという操作は未だ確立されていない。例え
ば、フレコンパツクに入った重合性粉体を重合缶の仕込
み口の上方に吊し、フレコンパツクの下方の取り出し口
より重合缶に直接供給する方法、貯蔵タンク等に直結し
たパイプに空気を流すニューマチックコンベアーを利用
する方法、スクリューコンベアを用いて推力輸送を利用
する方法等が考えられるか、いずれの方法も計量を正確
に行なうことがてきない。
On the other hand, the latter method of directly copolymerizing the imidized polymer has drawbacks in processing methods such as handling of the polymerizable powder in the imidized monomer. That is, in general, monomers of maleimide derivatives are powders, and the operation of accurately weighing such monomers on an industrial scale and then charging them into a polymerization reactor has not yet been established. For example, the polymerizable powder contained in a flexible container pack is suspended above the loading port of the polymerization can, and the polymerization can is supplied directly from the outlet at the bottom of the flexible container pack, or the air is flowed through a pipe directly connected to a storage tank, etc. Possible methods include using a pneumatic conveyor and using thrust transport using a screw conveyor, but none of these methods allow for accurate weighing.

また、マレイミド系誘導体の多くは人体に対し毒性を有
し、かつマレイミド系誘導体の製品形状が粉体もしくは
フレーク状であるため、」−記のような輸送方法ては粒
体か周囲に飛散しやすく、人体を保護するための設備か
必要となる。
In addition, many maleimide derivatives are toxic to the human body, and the product shape of maleimide derivatives is powder or flakes, so transportation methods such as those described above do not allow for granules to be scattered around. Equipment to protect the human body is required.

さらに、マレイミド系誘導体のような有機化合物を輸送
する際には静電気か発生しやすいため、工場内において
、別の重合反応か行なわれ、その原料である他の液状上
ツマ−の蒸気か発生しやすい重合缶の周辺で、このよう
な重合性粉体を取り扱う操作を実施することは、作業の
安全性を考えると好ましくない。
Furthermore, when transporting organic compounds such as maleimide derivatives, static electricity is likely to be generated, so another polymerization reaction is carried out in the factory, and vapor from other liquid materials, which are the raw materials, is generated. Considering the safety of the work, it is not preferable to carry out operations that involve handling such polymerizable powder in the vicinity of the polymerization can where the polymerization can be easily carried out.

他方、重合性粉体であるマレイミド系誘導体の千ツマ−
の処理方法として、メタクリル酸メチルやスチレンのよ
うな常温て液状のビニル系モノマーに溶解して輸送する
方法や、反応に対し不活性な有機溶剤に溶解する方法等
か挙げられるか、前者てはマレイミド系誘導体か前記の
ビニル系モノマーと極めて反応性が大きいため一般の貯
蔵用設備ては長期間保存することかてきず、保冷てきる
設備か必要となること、また後者ては溶剤の回収工程か
必要となること等によりいずれも実用性に乏しい。
On the other hand, a large amount of maleimide derivatives, which are polymerizable powders,
Treatment methods include transporting it by dissolving it in a vinyl monomer that is liquid at room temperature, such as methyl methacrylate or styrene, or dissolving it in an organic solvent that is inert to the reaction. Because maleimide derivatives are extremely reactive with the above-mentioned vinyl monomers, they cannot be stored for long periods using general storage equipment, and require equipment that can keep them cool. Both of these methods are impractical due to the necessity of

[発明か解決しようとする問題点] 本発明は、上記の様な従来の欠点を改善するためになさ
れたものであり、重合性粉体のマレイミド系誘導体とそ
の他のビニル系モノマーを共重合せしめて耐熱性の熱可
塑性樹脂を製造する方法において、水によって加水開環
性のない重合性粉体のマレイミド系誘導体を特定の配合
割合て水に懸濁させ、不活性て安定な懸濁液として輸送
または計量を行なうことにより、粉体であるために取り
扱い上多くの12!7題を有するマレイミド系誘導体の
輸送性を大幅に改良すると共に計量を正確に制御するこ
とを可能とし、また従来、問題とされていたマレイミド
系誘導体の粉体か飛散しその毒性により作業環境を汚染
することを防止し、さらに静電気の発生を防止した重合
性粉体の処理方法を提供することを目的とするものであ
る。
[Problems to be solved by the invention] The present invention has been made to improve the above-mentioned conventional drawbacks, and is a method of copolymerizing maleimide derivatives of polymerizable powder with other vinyl monomers. In a method for producing a heat-resistant thermoplastic resin, a maleimide derivative, which is a polymerizable powder that does not have hydrolytic ring-opening properties, is suspended in water at a specific mixing ratio to form an inert and stable suspension. By transporting or weighing, it is possible to greatly improve the transportability of maleimide derivatives, which have many problems in handling because they are powders, and to accurately control the weighing. The purpose is to prevent the problematic maleimide derivative powder from scattering and contaminating the working environment due to its toxicity, and to provide a method for processing polymerizable powder that prevents the generation of static electricity. It is.

[問題点を解決するための手段] すなわち、本発明は、下記−最大[I]■ (式中、R,、R2は水素原子、炭素原子数1〜4のア
ルキル基、ハロゲン原子または炭素原子数1〜4のハロ
ゲン化アルキル基、R3は炭素原子数l〜12のアルキ
ル基、シクロアルキル基または加水分解性のない置換基
を有するフェニル基を示す)て表わされるマレイミド系
誘導体5〜200重j龜部を水 100重量部に分散し
て生成した懸濁液を、懸濁状態で輸送または計量するこ
とを特徴とする重合性粉体の処理方法に係わるものであ
る。
[Means for Solving the Problems] That is, the present invention provides the following - maximum [I] 5 to 200 maleimide derivatives represented by a halogenated alkyl group of numbers 1 to 4, R3 is an alkyl group having 1 to 12 carbon atoms, a cycloalkyl group, or a phenyl group having a non-hydrolyzable substituent The present invention relates to a method for treating polymerizable powder, which comprises transporting or weighing a suspension produced by dispersing J. porridge in 100 parts by weight of water.

以下、本発明の詳細な説明する。The present invention will be explained in detail below.

本発明は、熱可塑性樹脂の耐熱性を向上せしめる目的で
重合性粉体であるマレイミド系誘導体の千ツマ−をスチ
レン、メタクリル酸メチル、塩化ビニル等のビニル系モ
ノマーと共重合反応を行ないイミド化ポリマーを製造す
る方法において、I′rg記重合性粉体であるマレイミ
ド系誘導体のモノマーを取り扱う処理方法に広く適用す
ることかできる。
In order to improve the heat resistance of thermoplastic resins, the present invention involves copolymerizing maleimide derivatives, which are polymerizable powders, with vinyl monomers such as styrene, methyl methacrylate, and vinyl chloride to imidize them. In the method of producing a polymer, it can be widely applied to a treatment method that handles a monomer of a maleimide derivative, which is a polymerizable powder described in I'rg.

本発明においては、粉体であるマレイミド系誘導体を木
に分散して均一て安定な懸濁液を生成し、該懸濁液をイ
ミド化ポリマーの共重合反応に使用するか、懸濁液の濃
度は水100重量部に対し前記−最大[I]て表わされ
るマレイミド系誘導体を5〜200重に部、好ましくは
10〜100重量部の割合て配合したものが望ましい。
In the present invention, a powdered maleimide derivative is dispersed in wood to form a uniform and stable suspension, and this suspension is used in a copolymerization reaction of an imidized polymer, or The concentration is preferably 5 to 200 parts by weight, preferably 10 to 100 parts by weight of the maleimide derivative represented by -maximum [I] per 100 parts by weight of water.

!g7Qさせるマレイミド系誘導体か5重量部未満ては
濃度が低いために輸送効率か悪くなり、200重量部を
こえると懸濁液の濃度が高くなり輸送性が著しく低下す
る。
! If the concentration of the maleimide derivative that causes g7Q is less than 5 parts by weight, the transport efficiency will be poor due to the low concentration, and if it exceeds 200 parts by weight, the concentration of the suspension will be high and the transportability will be significantly reduced.

また、懸濁させるマレイミド系誘導体としては、前記−
最大[I]て表わされる水によって加水開環性のない化
合物が用いられる。−最大[I]において、R,、R2
は水素原子、メチル基。
In addition, as the maleimide derivative to be suspended, the above-mentioned -
A compound having no hydrolytic ring-opening property with water represented by [I] at most is used. - at maximum [I] R,, R2
is a hydrogen atom, a methyl group.

エチル基等の炭素原子数1〜4のアルキル基、塩素、臭
素等のハロゲン原子、またはトリクロロメチル基等の炭
素原子数1〜4のハロゲン化アルキル基が好ましい。
Preferred are alkyl groups having 1 to 4 carbon atoms such as ethyl group, halogen atoms such as chlorine and bromine, or halogenated alkyl groups having 1 to 4 carbon atoms such as trichloromethyl group.

R3はエチル基、ノルマルオクチル基等の炭素原子数1
〜12のアルキル基、シクロヘキシル基。
R3 has 1 carbon atom such as ethyl group or normal octyl group
~12 alkyl groups, cyclohexyl groups.

4−メチルシクロヘキシル基等のシクロアルキル基、ま
たは0−クロロフェニル基、2.6−シメチルフエニル
基等の加水分解性のない置換基を有するフェニル基が好
ましい。
A cycloalkyl group such as 4-methylcyclohexyl group, or a phenyl group having a non-hydrolyzable substituent such as 0-chlorophenyl group or 2,6-dimethylphenyl group is preferable.

この様な本発明に用いられるマレイミド系誘導体の具体
例を示すと、フェニルマレイミドのような加水開環反応
性か大きな千ツマ−はマレイミド本来の性質を損なわせ
るため好ましくなく、エチルマレイミド、オクチルマレ
イミド、シクロへキシルマレイミド、2,6−シメチル
フエニルマレイミト等の水中においても比較的安定なマ
レイミドか好ましい。
Specific examples of the maleimide derivatives used in the present invention include phenylmaleimide, which has a large hydrolytic ring-opening reactivity, and is undesirable because it impairs the inherent properties of maleimide; , cyclohexylmaleimide, 2,6-dimethylphenylmaleimide, and other maleimides that are relatively stable even in water are preferred.

マレイミド系誘導体の懸濁液の調製方法は、特に限定す
るすることなく通常の粉体を水に均一に分散する方法を
適用することがてき、例えば、攪拌下に水の中にマレイ
ミド系誘導体の粉末を添加するか、またはマレイミド系
誘導体の粉末に水を攪拌しなから添加していく方法、等
により行なうことかてきる。
The method for preparing a suspension of a maleimide derivative is not particularly limited, and a conventional method of uniformly dispersing powder in water can be applied. This can be carried out by adding powder, or by adding water to the maleimide derivative powder without stirring.

また、マレイミド系誘導体の粉末を水に懸濁させる場合
、一部水面に浮遊することもあるが、この様な場合には
重合反応に影響な午えない範囲内て周知の界面活性剤、
有機・無機系の分散安定剤などを添加する方法か均一な
懸濁液を得るのに効果的である。
In addition, when suspending maleimide derivative powder in water, some of it may float on the water surface, but in such cases, well-known surfactants,
Adding an organic or inorganic dispersion stabilizer is effective for obtaining a uniform suspension.

さらに、前記−最大[I]で表わされるマレイミド系誘
導体は常温て固体であり、固体状態ては屯独重合性はな
いため、例えばベンゾイルパーオキサイド、ジクミルパ
ーオキサイドのような固体もしくは粒体の重合開始剤を
@濁液に混合してもよい。また、マレイミド系誘導体の
懸濁液には重合工程あるいは加工工程において必要な添
加剤て、懸濁液中に均一に分散可能なもの、かつ、この
時点て添加しても後の工程に影響を与えないもの等も混
合可能である。
Furthermore, the maleimide derivative represented by the maximum [I] above is solid at room temperature and has no self-polymerizability in the solid state. A polymerization initiator may be mixed into the suspension. In addition, the suspension of maleimide derivatives must contain additives that are necessary during the polymerization process or processing process, and must be able to be uniformly dispersed in the suspension, and that adding them at this point will not affect subsequent processes. Items that are not given can also be mixed.

[作用] 本発明の重合性粉体の処理方法は、前記−最大[I]て
表わされるマレイミド系誘導体5〜200重j、1部を
水100重量部に分散して懸濁せしめることにより、不
活性で安定な懸濁液を生成し、該懸濁液を懸濁状f、G
て輸送または計量することにより共重合反応工程中にお
ける取り扱いを容易にすると共に計!、11を正確に制
御することか可能となる。
[Function] The method for treating polymerizable powder of the present invention includes dispersing and suspending 5 to 200 parts by weight of the maleimide derivative represented by the above-mentioned maximum [I] in 100 parts by weight of water. producing an inert and stable suspension;
By transporting or weighing it, you can easily handle it during the copolymerization reaction process, and also make it easier to handle it during the copolymerization reaction process. , 11 can be accurately controlled.

[実施例] 以下、実施例を示し本発明をさらに具体的に説IIする
。但し、下記の実施例において示す装置類は例示にすぎ
ず、本発明の内容を限定するものてはない。
[Examples] Hereinafter, the present invention will be explained in more detail with reference to Examples. However, the devices shown in the following examples are merely illustrative and do not limit the content of the present invention.

実施例1 第1図は本発明の重合性粉体であるマレイミド系誘導体
の懸濁液の処理方法に使用する装置の一例を示す説明図
である。同第1図に示す装置を使用して、以下に示す方
法によりマレイミド系誘導体を共重合用玉舎缶に供給し
た。
Example 1 FIG. 1 is an explanatory view showing an example of an apparatus used in the method for treating a suspension of a maleimide derivative, which is a polymerizable powder, according to the present invention. Using the apparatus shown in FIG. 1, a maleimide derivative was supplied to the Tamasha can for copolymerization by the method shown below.

5i3の攪拌ズ付きタンクlに水100重量部に対しシ
クロへキシルマレイミド30重ら1部を懸濁させた@濁
液(密度1.01 g/cm’)を攪拌下て4s3仕込
み、バルブ5,6,8.9を開き、バルブ7、IOを閉
じた状態てダイヤフラムポンプ2を用いて懸濁液を重合
化4に輸送した。約10分間経過後、積算型の回転流量
計3の指示値か2m3増加したところで、バルブ7を開
け、バルブ8を閉じた。次に、バルブIOを開け、ライ
ン中に残った懸濁液を重合化4に送入した。
4s3 of a suspension (density 1.01 g/cm') prepared by suspending 1 part of 30 parts of cyclohexylmaleimide in 100 parts of water to 100 parts by weight of water was charged into a 5i3 tank with a stirring bowl under stirring. , 6, 8.9 were opened and the diaphragm pump 2 was used to transport the suspension to the polymerization 4 with valves 7 and IO closed. After about 10 minutes had elapsed, when the reading on the integrating rotary flow meter 3 increased by 2 m3, the valve 7 was opened and the valve 8 was closed. Next, valve IO was opened and the suspension remaining in the line was sent to polymerization 4.

タンクlに残った懸濁液を攪拌し、またライン中に残つ
たスラリー中のシクロへキシルマレイミドの沈降を防ぐ
ためにダイヤフラムポンプ2てスラリーを循環させなが
ら2週間放置しく内温20〜30°C)、赤外線スペク
トルを用いて分析を行ったが、仕込み時と組成に変化は
なかった。
While stirring the suspension remaining in tank 1 and circulating the slurry using diaphragm pump 2 to prevent precipitation of cyclohexylmaleimide in the slurry remaining in the line, the internal temperature was kept at 20 to 30°C. ) was analyzed using infrared spectroscopy, but there was no change in the composition compared to when it was prepared.

比較例1 実施例1と同じタンクにシクロへキシルマレイミド−ス
チレンのシクロへキシルマレイミドか20重量%の溶液
を4113仕込み、実施例1と同じ操作を行なった。
Comparative Example 1 In the same tank as in Example 1, 4113 cyclohexylmaleimide-styrene cyclohexylmaleimide or 20% by weight solution was charged, and the same operation as in Example 1 was performed.

2週間放置した溶液をメタノール中に析出させ、ポリマ
ー分を分析すると、30%かポリマーとなっていた。
The solution left for two weeks was precipitated in methanol, and the polymer content was analyzed and found to be 30% polymer.

比較例2 シクロへキシルマレイミド粉末20kg入り容器30缶
(合計600 kg)を容器より直接重合化4へ投入し
た。投入に要した時間は缶の開放・後始末を合せ40分
間であった。また、仕込み終了直後の重合化の周辺はシ
クロへキシルマレイミドの粉n1かたちこめていた。
Comparative Example 2 Thirty containers containing 20 kg of cyclohexylmaleimide powder (total 600 kg) were directly charged into Polymerization 4 from the container. The time required for adding the can was 40 minutes including opening and cleaning up the can. In addition, cyclohexylmaleimide powder n1 was packed around the polymerization area immediately after the completion of the preparation.

比較例3 第2図に示す装置を使用して重合化にシクロへキシルマ
レイミドを供給した。
Comparative Example 3 Cyclohexylmaleimide was fed into the polymerization using the apparatus shown in FIG.

空気圧縮fill″t’N2ガスを配管13へ通しなが
ら。
While passing the air compressed fill''t'N2 gas into the pipe 13.

供給mtzヘシクロへキシルマレイミド:l00kgを
フレコンハックから落下させ、供給機下のロータリーハ
ルツからバクフィルター14に送った。ハクフィルター
14の出口の排気N2ガス付近及び供給機12付近ては
、シクロへキシルマレイミドの粉立ちか観察された。
Supplied mtz hecyclohexylmaleimide: 100 kg was dropped from a flexible container hack and sent to the back filter 14 from the rotary Harz under the feeder. Powdering of cyclohexylmaleimide was observed near the exhaust N2 gas at the outlet of the Haku filter 14 and near the feeder 12.

[発明の効果] 本発明によれば、マレイミド系誘導体のような重合性粉
体な水に懸濁し懸濁状態で輸送または計量することによ
り、粉体であるために取り扱いL多くの問題を有してい
たマレイミド系誘導体の輸送性を大幅に改良すると共に
計量を正確に制御することが可能となり、作業性が大幅
に改善される。
[Effects of the Invention] According to the present invention, polymerizable powders such as maleimide derivatives are suspended in water and transported or weighed in a suspended state. This greatly improves the transportability of maleimide derivatives, which had previously been used, and makes it possible to accurately control metering, resulting in a significant improvement in workability.

更には、マレイミド系誘導体の粉体が飛散しその毒性に
より作業環境を汚染することを防止し、また静電気の発
生の問題も解決される。
Furthermore, the powder of the maleimide derivative is prevented from scattering and contaminating the working environment due to its toxicity, and the problem of static electricity generation is also solved.

また、単に懸濁液として使用する上記の利点だけでなく
、さらに実施例に示したような方法をとればシーケンス
制御による遠隔操作も可能である。
In addition to the above-mentioned advantages of simply using it as a suspension, if the method shown in the example is used, remote control by sequence control is also possible.

【図面の簡単な説明】[Brief explanation of the drawing]

第1図は本発明の重合性粉体であるマレイミド系誘導体
の懸濁液の処理方法に使用する装置の一例を示す説明図
および第2図は従来の重合性粉体の重合化への供給装置
を示す説明図である。 l・・・タンク 2・・・ダイヤフラムポンプ 3・・・積算型の回転流量計 4・・・重合化 5.6,7,8,9.10・・・ハルツ11・・・空気
圧縮a    12・・・供給機13・・・配管   
   14・・・バグフィルタ−15・・・受はタンク 出願人  電気化学工業株式会社 代理人  渡  辺  徳  廣 手続補正書 昭和63年番月手日 特許庁長官 小 川 邦 夫 殿 1、・1¥件の表示 昭和52年特許願第 322814  号2、発明の名
称 重合性粉体の処理方法 3、補正をする者 事件との関係 ・ 特許出願人 東京都千代11区有楽町1丁目4番1号(329)電気
化学工業株式会社 代表者  篠  原    晃 4、代理人 東京都雷鳥区北大塚2丁r]11番5号乎和堂ビル40
3号室 電話03(9]8)6686渡辺特許事務所 (6901)弁理士 渡  辺  徳  廣5、補正の
対象 明細書の「発IJIの詳細な説明」、「図面の簡単な説
明」の欄および図面 6、補正の内容 6−1発明の詳細な説明を下記の通り訂正する。 (1)明細3第4頁9行目 「作業の」を削除する。 (2)明細占第11頁1行目 [密度1.01g/c1Jを「密度1.2g/c+s’
 Jに訂正する。 (3)明細書第1+頁3行目、第1t頁11行目「ダイ
ヤプラムポンプ」を「ポンプ」に訂正する。 6−2図面の簡単な説明を下記の通り訂正する。 (1)明細占第14頁1行目 [ダイヤフラムポンプ」を「ポンプ」に訂正する。 6−:+l′54面を別紙の通り訂正する。 (1)第1図の「2タイヤフラムポンプ」を「2ポンプ
」に訂正する。子2后lJ湧鰯Hすnt−nl:/勾−
’II≦藪とγ私6
Figure 1 is an explanatory diagram showing an example of an apparatus used in the method for treating a suspension of a maleimide derivative, which is the polymerizable powder of the present invention, and Figure 2 is a conventional feed for polymerization of polymerizable powder. It is an explanatory view showing a device. l...Tank 2...Diaphragm pump 3...Integrating type rotary flow meter 4...Polymerization 5.6, 7, 8, 9.10...Hartz 11...Air compression a 12 ...Feeder 13...Piping
14...Bag filter-15...Receiver is tank Applicant: Representative for Denki Kagaku Kogyo Co., Ltd. Norihiro Watanabe Procedural amendment 1986 Date of Patent Office Commissioner Kunio Ogawa 1, 1 yen Indication of the matter Patent Application No. 322814 of 1972 2, Name of the invention Process for treating polymerizable powder 3, Relationship with the person making the amendment case - Patent applicant 1-4-1 Yurakucho, Chiyo 11-ku, Tokyo ( 329) Denki Kagaku Kogyo Co., Ltd. Representative Akira Shinohara 4, Agent Kita-Otsuka 2-chome, Raicho-ku, Tokyo] 11-5 Nwado Building 40
Room 3 Telephone: 03 (9] 8) 6686 Watanabe Patent Office (6901) Patent Attorney Norihiro Watanabe 5, "Detailed explanation of IJI" and "Brief explanation of drawings" columns of the specification subject to amendment, and Drawing 6 and Contents of Amendment 6-1 The detailed description of the invention is corrected as follows. (1) Delete "of work" in line 9 of page 4 of specification 3. (2) Specification, page 11, line 1 [density 1.01g/c1J is "density 1.2g/c+s'"
Correct to J. (3) In the specification, page 1+, line 3, and page 1t, line 11, "diaphragm pump" is corrected to "pump." 6-2 The brief description of the drawing is corrected as follows. (1) In the first line of page 14 of the specification, [diaphragm pump] was corrected to "pump". 6-: Correct side 54 of +l' as shown in the attached sheet. (1) Correct the "2-tire flamm pump" in Figure 1 to "2 pumps." 2nd child lJ spring sardine Hsnt-nl:/grade-
'II≦Yabu and γ me 6

Claims (1)

【特許請求の範囲】 下記一般式[ I ] ▲数式、化学式、表等があります▼[ I ] (式中、R_1、R_2は水素原子、炭素原子数1〜4
のアルキル基、ハロゲン原子または炭素原子数1〜4の
ハロゲン化アルキル基、R_3は炭素原子数1〜12の
アルキル基、シクロアルキル基または加水分解性のない
置換基を有するフェニル基を示す)で表わされるマレイ
ミド系誘導体5〜200重量部を水100重量部に分散
して生成した懸濁液を、懸濁状態で輸送または計量する
ことを特徴とする重合性粉体の処理方法。
[Claims] The following general formula [I] ▲There are mathematical formulas, chemical formulas, tables, etc.▼ [I] (In the formula, R_1 and R_2 are hydrogen atoms, and the number of carbon atoms is 1 to 4.
an alkyl group, a halogen atom or a halogenated alkyl group having 1 to 4 carbon atoms, R_3 represents an alkyl group having 1 to 12 carbon atoms, a cycloalkyl group, or a phenyl group having a non-hydrolyzable substituent). 1. A method for treating polymerizable powder, which comprises transporting or weighing a suspension prepared by dispersing 5 to 200 parts by weight of the maleimide derivative shown above in 100 parts by weight of water.
JP32281487A 1987-12-22 1987-12-22 Treatment of polymerizable powder Pending JPH01165572A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP32281487A JPH01165572A (en) 1987-12-22 1987-12-22 Treatment of polymerizable powder

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP32281487A JPH01165572A (en) 1987-12-22 1987-12-22 Treatment of polymerizable powder

Publications (1)

Publication Number Publication Date
JPH01165572A true JPH01165572A (en) 1989-06-29

Family

ID=18147911

Family Applications (1)

Application Number Title Priority Date Filing Date
JP32281487A Pending JPH01165572A (en) 1987-12-22 1987-12-22 Treatment of polymerizable powder

Country Status (1)

Country Link
JP (1) JPH01165572A (en)

Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5430157A (en) * 1977-08-12 1979-03-06 Mitsui Toatsu Chem Inc Stable aqueous dispersion of maleimide compound

Patent Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5430157A (en) * 1977-08-12 1979-03-06 Mitsui Toatsu Chem Inc Stable aqueous dispersion of maleimide compound

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