JPS6047005A - Modification of polymer - Google Patents
Modification of polymerInfo
- Publication number
- JPS6047005A JPS6047005A JP15300083A JP15300083A JPS6047005A JP S6047005 A JPS6047005 A JP S6047005A JP 15300083 A JP15300083 A JP 15300083A JP 15300083 A JP15300083 A JP 15300083A JP S6047005 A JPS6047005 A JP S6047005A
- Authority
- JP
- Japan
- Prior art keywords
- polymer
- alkaline earth
- metal
- alkali
- 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.)
- Pending
Links
Landscapes
- Addition Polymer Or Copolymer, Post-Treatments, Or Chemical Modifications (AREA)
Abstract
Description
【発明の詳細な説明】
はアルカリ土類金属を除去してポリマーを改質する方法
に関し、更に詳しくはポリマー液状物に特定物質を接触
させて行う方法に於て、特定の条件下に行うことを特徴
とするポリマーの改質方法に関する。[Detailed Description of the Invention] relates to a method of modifying a polymer by removing alkaline earth metals, and more specifically, a method of bringing a specific substance into contact with a polymer liquid under specific conditions. The present invention relates to a polymer modification method characterized by:
各種のポリマーが、最近各種電子材料に又は焼結助剤と
しての需要が高まっている。Various polymers have recently been in increasing demand for various electronic materials or as sintering aids.
しかしこれらポリマーば、ラジカル重合による場合を除
いて、通常は、金属の塩あるいは有機金属化合物を用い
て重合するため、数十から数百1)plnに及ぶ金属残
渣を含有している。However, since these polymers are usually polymerized using metal salts or organometallic compounds, except when radical polymerization is used, they contain metal residues ranging from several tens to several hundred pln.
金属類特にアルカリ金属やアルカリ土類金属がポリマー
中に残存していると焼結体に残ることとなり、電気特性
を悪化させ又焼結体の特1生を損うこととなるので、こ
れらの金属の残留の少ないポリマーの実用的供給が要望
されていた。If metals, especially alkali metals and alkaline earth metals, remain in the polymer, they will remain in the sintered body, deteriorating the electrical properties and impairing the properties of the sintered body. There has been a demand for a practical supply of polymers with less residual metal.
本発明者等は、この点につきかねてより種々の検削を行
なって来たところ、前記特許請求の範囲に特定した方法
によって、これら金属の残留阻の極めて少ないポリマー
を得ることを見出し先に出願した(特願昭58−906
47)。The inventors of the present invention have been conducting various inspections regarding this point for some time, and have found that by the method specified in the above-mentioned claims, a polymer with extremely low residual impediment of these metals can be obtained. (Special application 1986-906)
47).
しかしながら、先に出願した方法では、金属残渣を除去
することはできるが繰り返し行うと、はとんど完全に除
去できる場合(i pJ)I+]程度)と、あまり除去
できない(101)I)111以上)場合があった。However, with the previously applied method, it is possible to remove metal residues, but when repeated, the metal residues can be removed almost completely (i pJ) I+] and in some cases cannot be removed very much (101) I) 111 above).
本発明者らは、更に再現性良く除去できる方法について
、詳細に検討した結果、特定の条件下で処112するこ
とによって、再現性よくほぼ完全に除去することが町n
しであることを見出し、本発明を完成しブこ。As a result of detailed study on a method that can remove the particles with better reproducibility, the present inventors have found that it is possible to remove them almost completely with good reproducibility by treating them under specific conditions112.
He discovered that this was the case, and completed the present invention.
本発明の目的は、アルカリ金属又はアルカリ土類金属を
効率よく除去する方法を提供することにある。An object of the present invention is to provide a method for efficiently removing alkali metals or alkaline earth metals.
本発明は、特許請求の範囲に記載の通りであるが、その
要点はポリマーを液体状で処理すること、液体状である
ポリマーを特定の物質で処理することであり、この特定
物質での処理を水の不存在下で行うことを必須条件と1
.、次いで特定物質がら−を溶融させた物のい名゛れも
含まれる。い羞′れの場合にも当然の事ながら粘度が低
い方が処理が容易である。The present invention is as described in the claims, but the gist of the invention is to treat a polymer in a liquid state, to treat the liquid polymer with a specific substance, and to treat the polymer in a liquid state with a specific substance. The essential condition is that 1) be carried out in the absence of water.
.. Next, it also includes the names of products made by melting specific substances. Naturally, the lower the viscosity, the easier the treatment in the case of stains.
本発明の改質方法に用いる特定の物質とは、化学・物質
としての特許請求の範囲1)(1)に記載の物は勿論、
これら化合物を構成成分とする鉱物類を含み、更に陽イ
オン交換樹脂を含んでいる。容易に理jQイしうる通り
、こhらは混合物であってもよい。ごれらを具体的に示
ずと、8I、02、M、o、Aノ203、aoo、My
(OH)2、Ai(o++)3、co、(011);
B、八’ly O03、A12(003) 3、aQ、
co、、、ハイドロタルサイト、カオリン、モンモリロ
ン石、ベントナイト等でこれらは天然物か合成物かを問
わない。使用時に活性化処理することは好ましい。陽イ
オン交換樹脂としては、市販品で例えばアンバーリスト
(商品名)、ダイヤイオン(商品名)など充分使用しう
る。The specific substances used in the reforming method of the present invention include those described in claim 1)(1) as chemicals and substances, as well as
It contains minerals containing these compounds as constituent components, and further contains a cation exchange resin. As can be easily understood, these may be a mixture. If you don't specify them, 8I, 02, M, o, Aノ203, aoo, My
(OH)2, Ai(o++)3, co, (011);
B, 8'ly O03, A12 (003) 3, aQ,
co, hydrotalcite, kaolin, montmorillonite, bentonite, etc., and these may be natural or synthetic. It is preferable to perform activation treatment upon use. As the cation exchange resin, commercially available products such as Amberlyst (trade name) and Diaion (trade name) can be used.
これらの使用液ば、被処理物に含まれるアルカリ金属及
びアルカリ土類金属の量の10乃至1000倍であるが
、通常は10乃至100倍でよい。ポリマー中に含まれ
ているこれら金属類の含量としては、数円)Illから
数十回〕11]に及ぶ範囲に亘って本発明は適用可能で
ある。稀釈度を高くしたポリマー液を処理する場合には
、液!1Fの0001〜01程度用℃・て効果的な場合
がある。The amount of these liquids to be used is 10 to 1000 times the amount of alkali metals and alkaline earth metals contained in the object to be treated, but usually 10 to 100 times is sufficient. The present invention is applicable to a range in which the content of these metals contained in the polymer ranges from a few yen) to several tens of yen]11]. When processing highly diluted polymer liquids, liquid! Temperatures of 0001 to 01°C at 1F may be effective.
本発明に於ては、」二記特定物質と液状物ポリマーとの
接触槽E!Jiは、水の不存在下で行う。水分の1桂と
しては少なければ少ない方が良く、好ましくはポリマー
浴液に対して0.1 wt%以下で行なうのが良い。具
体的には、液状物ポリマー中の水の量を少ない量に保ち
、又上記・特定物質から処理の際に水を遊離しない条件
、即ち、通常好ましくは、脱水処理を施して使用するこ
とである。In the present invention, in the contact tank E! Ji is performed in the absence of water. The smaller the amount of water, the better, and preferably 0.1 wt% or less relative to the polymer bath solution. Specifically, it is necessary to keep the amount of water in the liquid polymer to a small amount and to ensure that water is not released from the above-mentioned specific substances during treatment, i.e., it is usually preferable to perform dehydration treatment before use. be.
又、液状物ポリマーの好ましい製造形態ではIF合u、
77よ、水の不存在−「に行われるため、触媒失活の際
に水を用℃・ず、水の混入しない条件下で処理を行えば
良い。In addition, in a preferred production form of the liquid polymer, IF u,
77, in the absence of water. Therefore, water is not used at the time of catalyst deactivation, and the treatment can be carried out under conditions where no water is mixed.
本発明の方法を用いることにより極めて簡tJIHに金
属残渣の少ないポリマーを再現性良<8えることが可能
となり、工業的に意義がある。By using the method of the present invention, it is possible to produce polymers with less metal residue in an extremely simple JIH manner with good reproducibility of <8, which is industrially significant.
以下、実施例により本発明の詳細な説明する。Hereinafter, the present invention will be explained in detail with reference to Examples.
実施例1及び比較例1
1eのフラスコに窒素雰囲気下で調製したスチレン50
g、トルエンろoom、lの混合液に7+−ブチルリチ
ウムを0.2.9 (14,5%7L−ヘキサンm液で
装入)を入れ撹拌した、重合熱で80゛Cまで温度が上
昇した。50′Cに降温し、無水エタノール1me加え
よ(攪拌し、半量はそのまま;1j過し、半量は次いで
こまかくすりつぶしたキョーワ〜1・′500(協和化
学(株)製合成・・イドロタルザイト、200℃で1時
間焼成したもの)3.?を加え、それぞれ10分間攪拌
した後、沢過しポリマー溶液とした。このポリマー溶液
からそれぞれトルエン及び少量の未反応モノマーを減圧
蒸留し、残渣としてポリマーを得た。ポリマー中の14
,7は炎光分先発度法で分析したところ、キヨーワード
を加えたものは0.51)l]+1であり、加えなかっ
たものは420I)pIYlであった。Example 1 and Comparative Example 1 Styrene 50 prepared under nitrogen atmosphere in flask 1e
0.2.9 g of 7+-butyllithium (charged with 14.5% 7L-hexane m solution) was added to a mixed solution of g, toluene oom, and l, and the temperature rose to 80°C due to the heat of polymerization. did. Lower the temperature to 50'C, and add 1me of absolute ethanol (stir, leave half as is; 1j filtered, then half finely ground Kyowa~1.500 (synthesized by Kyowa Kagaku Co., Ltd.), Idrotalzite, 200℃ After stirring for 10 minutes, each polymer solution was filtered to obtain a polymer solution.Toluene and a small amount of unreacted monomer were distilled under reduced pressure from each polymer solution to obtain a polymer as a residue. 14 in the polymer
, 7 was analyzed by the flame light fraction initiator method, and the result was 0.51)l]+1 with the keyword added, and 420I)pIYl without the keyword added.
比較例2
実捲例1において、失活剤としてエタノール1mlのか
わりに水1 mlを用いた他は実施例1と同様に処理し
たところ、得られたポリマー中の玩は42 ppmであ
った。Comparative Example 2 The same procedure as in Example 1 was repeated except that 1 ml of water was used instead of 1 ml of ethanol as the deactivator in Rolling Example 1, and the amount of carbon in the obtained polymer was 42 ppm.
実施例2
1eのフラスゴに窒素雰囲気下でトルエン50m1、α
−メチルスチレン’room1..ジグライム2m1.
.71.−ブチルリチウム0.39を加え、60゛Cで
2時間攪拌した。次いで無水メタノール1 ml加え触
媒活性を失活さぜ、さらにこまかく粉砕(、たシリカゲ
ル2gを加え、10分間撹拌した後、p過してポリマー
溶液を得た。次いでポリマー溶液を24のメタノール中
に投じてポリマーを析出させた。Example 2 50ml of toluene, α in a 1e flask under nitrogen atmosphere
-Methylstyrene'room1. .. Diglyme 2m1.
.. 71. -Butyl lithium (0.39 g) was added, and the mixture was stirred at 60°C for 2 hours. Next, 1 ml of anhydrous methanol was added to deactivate the catalyst activity, and 2 g of finely ground silica gel was added, stirred for 10 minutes, and filtered through p-filter to obtain a polymer solution.Then, the polymer solution was poured into 24 methanol. to precipitate the polymer.
得られたポリマーについて実施例1と同様に分析したど
ころ0.2 plMnのリチウムしか含有していなかっ
た。When the obtained polymer was analyzed in the same manner as in Example 1, it contained only 0.2 plMn of lithium.
比較例ろ
実施例2において、失活剤としてメタノール1mlのか
わりに水1 mlを用いた他は実施例2と同様に処理し
たところ、ポリマー中のリチウムは13ppmであった
。Comparative Example The same procedure as in Example 2 was carried out except that 1 ml of water was used instead of 1 ml of methanol as a deactivator, and the lithium content in the polymer was 13 ppm.
実brM例6
実施例1において、触媒としてすトリウムナフタレン0
2gとし、キヨーワード500の焼成時間を60分とし
た他は実施例1と同様に重合し、同様に処理を行ったと
ころ、ポリマー中のNoは2 ppmであった。Actual brM Example 6 In Example 1, thorium naphthalene 0 was used as a catalyst.
Polymerization was carried out in the same manner as in Example 1, except that the amount of polymer was 2 g and the firing time for Kyoward 500 was 60 minutes, and the same treatment was carried out, and the No. content in the polymer was 2 ppm.
実施例4〜7
実施例1において、添加物として、こまかくすりつぶし
たモレキーラーシーブ3A(実施例4)、M、0(実施
例5)、ベントナイト(実施例6)、こまかくすりつぶ
した活性アルミナ(実施例7)を用いた他は実施例1と
同様に処理した。ただし添加に先だって、トルエン50
0m1加えてポリマー液を稀釈して行った。得られたポ
リマー中のLj含量はそれぞれ1 ppm、0.4 p
pm、0.05 pp磨 0.02pI]ηであった。Examples 4 to 7 In Example 1, finely ground Molecule Sieve 3A (Example 4), M,0 (Example 5), bentonite (Example 6), finely ground activated alumina (Example The process was carried out in the same manner as in Example 1, except that Example 7) was used. However, before addition, toluene 50
The polymer solution was diluted by adding 0ml. The Lj contents in the obtained polymers were 1 ppm and 0.4 p, respectively.
pm, 0.05 pp polishing 0.02 pI] η.
Claims (1)
マーの液状物に、 (1) sA 、 M、、Aノ又はCα原子の酸化物、
水酸化物又は炭酸塩の一種以上、 (2)上記化学成分を実質的に有効成分として含有する
鉱物質、又は (ろ)陽イオン交換樹脂、 のいづれか一種以上を接触させた後に分離するポリマー
の改質方法に於て、水の不存在下で上記接触処理を行う
ことを特徴とするポリマーの改質方法。 2)ポリマーがオレフィン及び/又はジエン化合物を有
機金属化合物を用いて得たポリマーであることを特徴と
する特許請求の範囲第一項に記載の方法。[Scope of Claims] 1) A polymer liquid containing an alkali metal or an alkaline earth metal, (1) an oxide of sA, M,, A or Cα atoms;
(2) a mineral material containing substantially the above chemical component as an active ingredient; or (2) a cation exchange resin; A method for modifying a polymer, characterized in that the above-mentioned contact treatment is carried out in the absence of water. 2) The method according to claim 1, wherein the polymer is a polymer obtained from an olefin and/or diene compound using an organometallic compound.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP15300083A JPS6047005A (en) | 1983-08-24 | 1983-08-24 | Modification of polymer |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP15300083A JPS6047005A (en) | 1983-08-24 | 1983-08-24 | Modification of polymer |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| JPS6047005A true JPS6047005A (en) | 1985-03-14 |
Family
ID=15552754
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP15300083A Pending JPS6047005A (en) | 1983-08-24 | 1983-08-24 | Modification of polymer |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS6047005A (en) |
-
1983
- 1983-08-24 JP JP15300083A patent/JPS6047005A/en active Pending
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