JPS6217051A - Glass tube collecting agent - Google Patents

Glass tube collecting agent

Info

Publication number
JPS6217051A
JPS6217051A JP15230885A JP15230885A JPS6217051A JP S6217051 A JPS6217051 A JP S6217051A JP 15230885 A JP15230885 A JP 15230885A JP 15230885 A JP15230885 A JP 15230885A JP S6217051 A JPS6217051 A JP S6217051A
Authority
JP
Japan
Prior art keywords
glass tube
cyclopentadiene
polymer
agent
sizing agent
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
JP15230885A
Other languages
Japanese (ja)
Inventor
Arihiro Wada
和田 有弘
Takashi Toda
隆司 戸田
Michihiro Kumagai
熊谷 道裕
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.)
Idemitsu Petrochemical Co Ltd
Original Assignee
Idemitsu Petrochemical 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 Idemitsu Petrochemical Co Ltd filed Critical Idemitsu Petrochemical Co Ltd
Priority to JP15230885A priority Critical patent/JPS6217051A/en
Publication of JPS6217051A publication Critical patent/JPS6217051A/en
Pending legal-status Critical Current

Links

Abstract

PURPOSE:To obtain the titled collecting agent having excellent thermal stability and inodorousness in melting and further having excellent solubility in solvents by hydrogenating the cyclopentadiene polymer as the agent for collecting glass tubes which are combined with semiconductors in the circuit element for electrical and electronic equipment. CONSTITUTION:The titled agent consists of the hydrogenation product of a cyclopentadiene polymer and/or a cyclopentadiene compd.-vinyl-substituted aromatic hydrocarbon copolymer. The collecting agent is the hydrogenated polymer and/or the hydrogenated copolymer obtained by hydrogenating the polymer or the copolymer with the use of a catalyst such as Pd and Ni or their mixture. When the collecting agent is used, a bundle of plural glass tubes is dipped in the melt of the collecting agent, pulled up, cut in prescribed length and washed with a solvent such as toluene to dissolve and remove the collecting agent and the glass tube having desired length is obtained.

Description

【発明の詳細な説明】 [産業上の利用分野] 本発明は、ガラス管収束剤に関し、さらに詳しくは、溶
融時の熱安定性および無臭性、ならびに、溶剤に対する
溶解性に優れたガラス管収束剤に関する。
Detailed Description of the Invention [Industrial Application Field] The present invention relates to a glass tube binding agent, and more specifically, a glass tube binding agent that has excellent thermal stability and odor when melted, and excellent solubility in solvents. Regarding drugs.

[従来技術〕 電子・電気機器に用いられるダイオード等の回路素子の
中には、シリコン(Si)もしくはゲルマニウム(Ge
)などの半導体と外径0.5〜1.5mm 、長さ 1
〜3hm程度の極細ガラス管とを組み合わせたものがあ
る。
[Prior art] Some circuit elements such as diodes used in electronic and electrical equipment are made of silicon (Si) or germanium (Ge).
) and other semiconductors with an outer diameter of 0.5 to 1.5 mm and a length of 1
There is a combination with an ultra-thin glass tube of about 3 hm.

このようなガラス管は、外径0.5〜10mm程度のガ
ラス管を所望の長さに切断することによって製造される
が、このとき、製造効率を向上させるために次のような
方法を適用することが一般的である。すなわち、複数本
のガラス管を溶融したガラス管収束剤中に浸漬したのち
、取り出して冷却して該ガラス管収束剤により収束固着
し、この収束体ごと所定長さに切断する。しかるのち、
収束剤を適当な溶剤により溶解除去せしめることにより
、目的とする寸法のガラス管を得る。
Such glass tubes are manufactured by cutting glass tubes with an outer diameter of about 0.5 to 10 mm into desired lengths, but at this time, the following method is applied to improve manufacturing efficiency. It is common to do so. That is, after a plurality of glass tubes are immersed in a molten glass tube binding agent, they are taken out, cooled, and fixed by the glass tube binding agent, and the bundle is cut into a predetermined length. Afterwards,
By dissolving and removing the sizing agent with a suitable solvent, a glass tube of the desired size is obtained.

[発明が解決しようとする問題点] かかるガラス管収束剤としては、従来、松ヤニにパラフ
ィンを配合してなるものが使用されていた。この収束剤
はガラス管固着能を有するものの、松ヤニが天然産であ
るため原料供給量が不安定であること、および、収束剤
を除去する際に、該収束剤の溶剤に対する溶解性が低い
という問題がある。
[Problems to be Solved by the Invention] As such a glass tube sizing agent, a mixture of pine tar and paraffin has conventionally been used. Although this sizing agent has the ability to fix glass tubes, since pine tar is a natural product, the supply of raw materials is unstable, and when the sizing agent is removed, the solubility of the sizing agent in the solvent is low. There is a problem.

そこで、これに代わるガラス管収束剤として。Therefore, as an alternative glass tube convergence agent.

シクロペンタジェン重合体またはシクロベンタジエン−
スチレン共重合体よりなるものが提案されている。しか
しながら、この収束剤は、溶融時の熱安定性が良好でな
く、しかも溶融時に悪臭が発生するという点で、未だ改
良の余地を残すものであった・ 本発明は、従来のかかる問題点を解消し、高いガラス管
固着能を有することは勿論のこと、溶融時の熱安定性な
らびに無臭性に優れ、しかも、溶媒に対する溶解性に優
れたガラス管収束剤の提供を目的とする。
Cyclopentadiene polymer or cyclobentadiene-
One made of styrene copolymer has been proposed. However, this sizing agent does not have good thermal stability when melted and also generates a bad odor when melted, so there is still room for improvement.The present invention solves these conventional problems. The purpose of the present invention is to provide a glass tube binding agent which not only has a high ability to fix glass tubes, but also has excellent thermal stability and odorlessness during melting, as well as excellent solubility in solvents.

[問題点を解決するための手段] 木発明者らは、上記目的を達成すべく鋭意研究を重ねた
結果、後述するように、従来のガラス管収束剤を水素添
加して得られたものが、ガラス管収束剤として要求され
る特性をすべて満足するものであることを見出して本発
明を完成するに到った。
[Means for Solving the Problems] As a result of extensive research in order to achieve the above object, the inventors discovered that, as will be described later, a product obtained by hydrogenating a conventional glass tube sizing agent was The present invention was completed based on the discovery that it satisfies all the properties required for a glass tube sizing agent.

すなわち、本発明のガラス管収束剤は、シクロペンタジ
ェン系共重合体および/またはシクロペンタジェン系化
合物−ビニル置換芳香族炭化水素共重合体の水素添加物
よりなることを特徴とする。
That is, the glass tube sizing agent of the present invention is characterized by comprising a hydrogenated product of a cyclopentadiene copolymer and/or a cyclopentadiene compound-vinyl-substituted aromatic hydrocarbon copolymer.

[具体的説明] 本発明のガラス管収束剤は、前述したように。[Specific explanation] The glass tube sizing agent of the present invention is as described above.

シクロペンタジェン系重合体の水素添加物もしくはシク
ロペンタジェン系化合物−ビニル置換芳香族炭化水素共
重合体の水素添加物、あるいはこれら2つの混合物であ
る。
It is a hydrogenated product of a cyclopentadiene-based polymer, a hydrogenated product of a cyclopentadiene-based compound-vinyl-substituted aromatic hydrocarbon copolymer, or a mixture of these two.

まず、シクロペンタジェン系重合体としては、シクロペ
ンタジェン、メチルシクロペンタジェン、エチルシクロ
ペンタジェン、または、これらの二量体、三量体あるい
はこれらの間の共二量体などのシクロペンタジェン系化
合物の重合体があげられ、なかでも、シクロペンタジェ
ン重合体、ジシクロペンタジェン重合体は好ましいもの
である。また、前記シクロペンタジェン系化合物として
は石油の熱分解などで得られる混合留分を使用してもよ
い、なお、仕込みの際に該シクロペンタジェンをそのま
ま使用してもよいが、ジシクロペンタジェンを使用して
共重合反応時にこれを分解せしめ、シクロペンタジェン
としテモよい。
First, the cyclopentadiene polymers include cyclopentadiene, methylcyclopentadiene, ethylcyclopentadiene, dimers, trimers, and codimers thereof. Examples include polymers of such compounds, and among them, cyclopentadiene polymers and dicyclopentadiene polymers are preferred. Further, as the cyclopentadiene compound, a mixed fraction obtained by thermal decomposition of petroleum may be used.The cyclopentadiene may be used as it is during the preparation, but dicyclopentadiene may be used as it is. This can be decomposed during the copolymerization reaction to form cyclopentadiene.

一方、シクロペンタジェン系化合物−ビニル置換芳香族
炭化水素共重合体は、上に列挙したシクロペンタジェン
系化合物と、ビニル置換芳香族炭化水素との共重合体で
ある。このビニル置換芳香族炭化水素としては、とくに
限定されるものではなく、例えば、スチレン、α−メチ
ルスチレン、ビニルトルエン、などをあげることができ
る、このうち、スチレンは好ましいものである。
On the other hand, the cyclopentadiene-based compound-vinyl-substituted aromatic hydrocarbon copolymer is a copolymer of the above-listed cyclopentadiene-based compound and a vinyl-substituted aromatic hydrocarbon. The vinyl-substituted aromatic hydrocarbon is not particularly limited, and includes, for example, styrene, α-methylstyrene, vinyltoluene, etc. Among these, styrene is preferred.

かかる2つの共重合成分の構成比は、とくに制限される
ものではないが、例えば、シクロペンタジェン系化合物
が95〜5重量%、さらには、80〜50重量%、ビニ
ル置換芳香族炭化水素が5〜85重量%、さらには20
〜50重量%で合計 100重量%となるようにそれぞ
れの使用量を設定することが好ましい。
The composition ratio of these two copolymerization components is not particularly limited, but for example, the cyclopentadiene compound is 95 to 5% by weight, more preferably 80 to 50% by weight, and the vinyl substituted aromatic hydrocarbon is 95 to 5% by weight. 5-85% by weight, even 20
It is preferable to set the usage amount of each of them so that the total amount is 100% by weight at 50% by weight.

これらの重合体および共重合体は次のようにして製造さ
れる。
These polymers and copolymers are produced as follows.

すなわち、シクロペンタジェン系化合物単独で、もしく
は、シクロペンタジェン系化合物とビニル置換芳香族炭
化水素を所定割合で仕込み、重合反応を行なわせる0反
応に際しては、必要に応じて溶媒を使用してもよい。使
用する溶媒としては、とくに限定されるものではないが
、例えば、芳香族系、ナフテン系もしくはパラフィン系
炭化水素が好適なものとしてあげられる。また、溶媒の
使用量は、シクロペンジエン系化合物もしくはシクロペ
ンタジェン系化合物とビニル置換芳香族炭化水素との混
合物100重量部に対して、0〜500重量部、好まし
くは、5〜200重量部に設定される。なお0反応温度
は250〜300℃、さらには260〜280℃、反応
時間は0.5〜10時間、好ましくは、 1〜5時間に
それぞれ設定することが好ましい。
That is, in the zero reaction in which a cyclopentadiene compound alone or a cyclopentadiene compound and a vinyl-substituted aromatic hydrocarbon are charged in a predetermined ratio and a polymerization reaction is carried out, a solvent may be used as necessary. good. The solvent to be used is not particularly limited, but suitable examples include aromatic, naphthenic, or paraffinic hydrocarbons. The amount of the solvent used is 0 to 500 parts by weight, preferably 5 to 200 parts by weight, based on 100 parts by weight of the mixture of the cyclopendiene compound or cyclopentadiene compound and the vinyl-substituted aromatic hydrocarbon. is set to The reaction temperature is preferably set at 250 to 300°C, more preferably 260 to 280°C, and the reaction time is preferably set at 0.5 to 10 hours, preferably 1 to 5 hours.

ついで、このようにして得られた重合体もしくは共重合
体に水素添加せしめることにより、水素添加重合体もし
くは水素添加共重合体を得る。この反応において、使用
する触媒としては1例えば、Pd、Ni、Pt系の触媒
をあげることができる。
Next, the thus obtained polymer or copolymer is hydrogenated to obtain a hydrogenated polymer or copolymer. In this reaction, examples of catalysts used include Pd, Ni, and Pt-based catalysts.

触媒の使用量はとくに制限されるものではないが、上述
した重合体もしくは共重合体100重量部に対して、 
1〜10重量部、好ましくは3〜7重量部に設定される
。また、反応に際しては、必要に応じて溶媒を使用する
ことができる。溶媒の具体例としては、例えば、ナフテ
ン系もしくは、パラフィン系炭化水素、エーテル類、ケ
トン類又はエステル類などをあげることができる。かか
る溶媒の使用量はとくに制限されるものではないが、重
合体もしくは共重合体100重量部に対して、0〜50
0重量部、好ましくは、50〜150重量部に設定すれ
ばよい。
The amount of catalyst used is not particularly limited, but based on 100 parts by weight of the above-mentioned polymer or copolymer,
The amount is set at 1 to 10 parts by weight, preferably 3 to 7 parts by weight. Moreover, a solvent can be used as necessary during the reaction. Specific examples of the solvent include naphthenic or paraffinic hydrocarbons, ethers, ketones, and esters. The amount of such a solvent used is not particularly limited, but is 0 to 50 parts by weight based on 100 parts by weight of the polymer or copolymer.
The amount may be set to 0 parts by weight, preferably 50 to 150 parts by weight.

この水素添加反応において、水素圧はlO〜100kg
/ ad、さらには、30〜50 kg/adに設定す
ることが好ましく、また、反応温度は 100〜250
℃、さらには 120〜200℃、反応時間は0.5〜
lO時間、さらには 1〜8時間にそれぞれ設定するこ
とが好ましい。
In this hydrogenation reaction, the hydrogen pressure is 1O~100kg
/ ad, more preferably set to 30 to 50 kg/ad, and the reaction temperature is 100 to 250 kg/ad.
℃, even 120~200℃, reaction time 0.5~
It is preferable to set each time to 10 hours, more preferably 1 to 8 hours.

このようにして得られた重合体もしくは共重合体の諸性
質はおおよそ次のようになる。すなわち、蒸気圧測定法
による分子量:500〜1500、臭素価= θ〜lO
g/100g、軟化点=50〜200℃、酸化: 1以
下、色相(ガードナー色度):l以下である。また、共
重合体におけるスチレン骨格含有率は、5〜60重量%
、さらには、20〜40重量%程度であることが好まし
い。
The properties of the polymer or copolymer thus obtained are approximately as follows. That is, molecular weight by vapor pressure measurement method: 500 to 1500, bromine number = θ to lO
g/100g, softening point = 50 to 200°C, oxidation: 1 or less, hue (Gardner chromaticity): 1 or less. In addition, the styrene skeleton content in the copolymer is 5 to 60% by weight.
, and more preferably about 20 to 40% by weight.

本発明のガラス管収束剤は、上記のシクロペンタジェン
系重合体の水素添加物もしくはシクロペンタジェン系化
合物−ビニル置換芳香族炭化水素共重合体の水素添加物
そのものであるか、又は。
The glass tube sizing agent of the present invention is a hydrogenated product of the above-mentioned cyclopentadiene-based polymer or a hydrogenated product of a cyclopentadiene-based compound-vinyl-substituted aromatic hydrocarbon copolymer, or.

両者を任意の割合で混合してなるものである。It is made by mixing both in an arbitrary ratio.

このガラス管収束剤は例えば次のようにして使用する。This glass tube sizing agent is used, for example, in the following manner.

すなわち、まず、容器内でこのガラス管収束剤を溶融せ
しめる。溶融温度はガラス管収束剤の軟化点より高いこ
とが必要であり、通常 130〜180℃である。つい
で、このガラス管収束剤の融液に、複数本のガラス管の
束を例えば1〜30分間浸漬し、ガラス管を引き上げた
のち収束剤を冷却固化させる。しかるのち、この収束体
を例えばダイヤモンドカッターにより所定の長さに切断
し、その後、溶剤により洗浄してガラス管収束剤を溶解
・除去せしめ、所望の長さのガラス管を、得る。
That is, first, the glass tube sizing agent is melted in a container. The melting temperature needs to be higher than the softening point of the glass tube sizing agent, and is usually 130 to 180°C. Next, a bundle of a plurality of glass tubes is immersed in the melt of the glass tube sizing agent for, for example, 1 to 30 minutes, and after the glass tubes are pulled up, the sizing agent is cooled and solidified. Thereafter, this convergent body is cut into a predetermined length using, for example, a diamond cutter, and then washed with a solvent to dissolve and remove the glass tube convergence agent, thereby obtaining a glass tube of a desired length.

このとき使用する溶剤としては、前述のガラス管収束剤
を溶解せしめるものであればよく、例えば、トルエン、
パークロロエチレン、キシレン、トリクロロエチレン、
クロロホルム、ジクロロエタン、ジクロロエタン、もし
くは、これらの混合溶液が好ましい。
The solvent used at this time may be any solvent that can dissolve the glass tube sizing agent described above, such as toluene,
perchlorethylene, xylene, trichlorethylene,
Chloroform, dichloroethane, dichloroethane, or a mixed solution thereof is preferred.

[実施例] 実施例1 (1)ガラス管収束剤の調製 シクロペンタジェン300gおよびキジ9フ300内容
積l!;Lのオートクレーブ中に仕込み、280℃にお
いて 1.5時間重合反応を行なわせ、重合体272g
を得た。このものの軟化点は72℃、臭素価は85であ
った.ついで、この重合体200gをシクロヘキサン2
00gに溶解させ、触媒として0.5重量%のPdを含
有する Pd−シリカ・アルミナ触媒10gを使用し、
水素圧50kg/cm 、  210’Oにおいて2時
間水素添加を行なった6その結果、水素添加重合体、す
なわち、ガラス管収束剤199gを得た。このものの軟
化点は98℃、臭素化は0.5であった。
[Example] Example 1 (1) Preparation of glass tube sizing agent 300 g of cyclopentadiene and 300 liters of pheasant 9 fu! ; Pour into L autoclave and carry out polymerization reaction at 280°C for 1.5 hours to obtain 272 g of polymer.
I got it. This material had a softening point of 72°C and a bromine number of 85. Next, 200 g of this polymer was mixed with cyclohexane 2
Using 10 g of Pd-silica alumina catalyst containing 0.5% by weight of Pd as a catalyst,
Hydrogenation was carried out for 2 hours at a hydrogen pressure of 50 kg/cm 2 and 210'O. As a result, 199 g of a hydrogenated polymer, ie, a glass tube sizing agent, was obtained. This material had a softening point of 98°C and a bromination level of 0.5.

(2)ガラス管の製造 上記により得られたガラス管収束剤を 150℃におい
て溶融させ、この融液中に外径lam 、長さ300m
層のガラス管42木を束にして、該ガラス管の長手方向
が液面と直交するようにして10分間浸漬し、引き上げ
たのち空気中で冷却固化せしめた。
(2) Production of glass tubes The glass tube sizing agent obtained above was melted at 150°C, and the outside diameter lam and length 300 m were added to the melt.
The glass tubes 42 of each layer were bundled and immersed for 10 minutes so that the longitudinal direction of the glass tubes was perpendicular to the liquid level. After being pulled out, the tubes were cooled and solidified in air.

この結果、上記ガラス管を収束してなる 8II11×
7+w+a X 30hmのガラス管収束体を得た.つ
いで、切削油として出光興産■製AL−38を使用し、
ダイヤモンドカッターによりこの収束体をガラス管の長
手方向と直交する面で21幅に切断した。
As a result, the above glass tubes are converged to form 8II11×
A glass tube converging body of 7+w+a x 30hm was obtained. Next, Idemitsu Kosan AL-38 was used as cutting oil.
This converging body was cut into 21 widths using a diamond cutter on a plane perpendicular to the longitudinal direction of the glass tube.

しかるのち、得られた収束体片を、まず、トルエン20
0−とパークロルエチレン200−とからなる混合溶媒
で予備洗浄してガラス管収束剤を溶解・除去し、ついで
中性洗剤により本洗浄を行なって収束剤を完全に除去せ
しめ、長さ2層mのガラス短管を得た。
After that, the obtained convergence body piece was first diluted with 20% of toluene.
The glass tube sizing agent was preliminarily washed with a mixed solvent consisting of 0- and perchlorethylene 200- to dissolve and remove it, and then the main cleaning was performed with a neutral detergent to completely remove the sizing agent. A glass short tube of m was obtained.

このようなガラス管収束剤を使用したガラス短管の製造
工程において、以下に述べる各評価試験を行なって、該
ガラス管収束剤が要求される特性を満足するものである
か否かを評価した。
In the manufacturing process of short glass tubes using such a glass tube sizing agent, the following evaluation tests were conducted to evaluate whether the glass tube sizing agent satisfies the required characteristics. .

(A)熱安定性 ガラス管収束剤を空気中、 150°Cで溶融させた状
態で20時間保持した後の粘度を測定し、初期値に対す
る粘度上昇率(%)を測定した。
(A) The viscosity of the heat-stable glass tube sizing agent was measured after being melted at 150°C in air for 20 hours, and the viscosity increase rate (%) with respect to the initial value was measured.

(B)無臭性 ガラス管収束剤を 150°Cで溶融させたときの臭気
の有無を調べた。
(B) The presence or absence of odor was investigated when the odorless glass tube sizing agent was melted at 150°C.

臭気なし・・・・・・・・・O1臭気あり・・・・・・
・・・×(C)非引火性(引火点) JIS K 22fi5に準拠してガラス管収束剤の引
火点(”O)を測定した。
No odor...O1 odor...
...×(C) Non-flammability (flash point) The flash point ("O) of the glass tube sizing agent was measured in accordance with JIS K 22fi5.

(D)収束性(固着能) ガラス管収束剤によりガラス管を収束した後、該収束体
をダイヤモンドカッターで切断した際のガラス管の固定
性を評価した。
(D) Convergence (Fixing ability) After converging the glass tubes with a glass tube convergence agent, the fixity of the glass tubes was evaluated when the convergence body was cut with a diamond cutter.

ガラス管の離脱なし   ・・・・・・・・・Oガラス
管の離脱が一部あり・・・・・・・・・×(E)非収縮
性 150°Cで溶融したガラス管収束剤を 150mmX
30amX 2mmの金型に流し込み室温まで冷却した
ときの亀裂の有無を目視により調べた。
No separation of glass tubes ・・・・・・O Some separation of glass tubes ・×(E) Non-shrinkage Glass tube sizing agent melted at 150°C 150mmX
The sample was poured into a 30 am x 2 mm mold and cooled to room temperature, and was visually inspected for cracks.

亀裂なし・・・・・・・・・0 亀裂あり・・・・・・・・・× (F)切削油に対する安定性 ガラス管収束剤と切削油(出光興産■AL−38)とを
重量比l:1で混合し、 1分間振とうしてから24時
間経過後の溶融性を調べた。
No cracks・・・・・・・・・0 Cracks・・・・・・・・・× (F) Stability against cutting oil The weight of the glass tube sizing agent and cutting oil They were mixed at a ratio of 1:1 and shaken for 1 minute, and their meltability was examined 24 hours later.

不溶  ・・・・・・・・・〇 一部不溶・・・・・・・・・Δ 溶解  ・・・・・・・・・× (G)溶剤に対する溶解性 ガラスw収束剤とトルエン/パークロルエチレン混合溶
媒(重量比に1)とを混合し、 1分間振とうしてから
24時間経過後の溶解性を調べた。
Insoluble ・・・・・・・・・〇Partially insoluble・・・・・・・・・Δ Dissolved ・・・・・・・・・× (G) Solubility of glass in solvent w Convergence agent and toluene/park It was mixed with a mixed solvent of rollethylene (weight ratio: 1), shaken for 1 minute, and examined for solubility 24 hours later.

溶解     ・・・・・・・・・O 不溶ないし難溶・・・・・・・・・× 以上の結果を一括して表に示した。Dissolution ・・・・・・・・・O Insoluble or poorly soluble...× The above results are summarized in the table.

実施例2 シクロペンタジェン200g、  スチレン200gお
よびキシレン200gを内容積 1愛のオートクレーブ
中に仕込み、260℃において 1.5時間重合反応を
行なわせ、重合体353gを得た。このものの軟化点は
72°C1臭素価は58、スチレン骨格含有率50重量
%であった。ついで、この重合体200gをシクロヘキ
サン200gに溶解させ、触媒として0.5重量%のP
dを含有する Pd−シリカ・アルミナ触媒10gを使
用し、水素圧30kg/cm、200℃において5時間
水素添加を行なった。その結果、水素添加重合体、すな
わち、ガラス管収束剤199gを得た。このものの軟化
点は102℃、臭素化は4.5、スチレン骨格含有率は
33重量%であった。
Example 2 200 g of cyclopentadiene, 200 g of styrene, and 200 g of xylene were charged into an autoclave having an internal volume of 1 cm, and a polymerization reaction was carried out at 260° C. for 1.5 hours to obtain 353 g of a polymer. The softening point of this product was 72°C, the bromine number was 58, and the styrene skeleton content was 50% by weight. Next, 200 g of this polymer was dissolved in 200 g of cyclohexane, and 0.5% by weight of P was added as a catalyst.
Using 10 g of Pd-silica/alumina catalyst containing d, hydrogenation was carried out at a hydrogen pressure of 30 kg/cm and at 200° C. for 5 hours. As a result, 199 g of a hydrogenated polymer, ie, a glass tube sizing agent, was obtained. The softening point of this product was 102°C, the bromination was 4.5, and the styrene skeleton content was 33% by weight.

このガラス管収束剤を使用して、上記実施例1と同様に
ガラス短管を製造し、かつ、同様の評価試験を行なって
結果を表に示した。
Using this glass tube sizing agent, short glass tubes were manufactured in the same manner as in Example 1 above, and the same evaluation tests were conducted, and the results are shown in the table.

比較例1 ガラス管収束剤として、松ヤニとパラフィンワックスと
を重量比で97:3となるように混合したものを使用し
た点を除いては上記実施例1と同様にしてガラス短管を
製造し、かつ、同様の評7価試験を行なって結果を表に
示した。
Comparative Example 1 A short glass tube was produced in the same manner as in Example 1, except that a mixture of pine resin and paraffin wax at a weight ratio of 97:3 was used as the glass tube sizing agent. In addition, a similar evaluation test was conducted and the results are shown in the table.

比較例2 ガラス管収束剤として、上記実施例1で得られた水素添
加前の重合体を使用した点を除いては上記実施例1と同
様にしてガラス短管を製造し、かつ、同様の評価試験を
行なって結果を表に示した。
Comparative Example 2 A short glass tube was produced in the same manner as in Example 1 above, except that the polymer before hydrogenation obtained in Example 1 above was used as a glass tube sizing agent, and the same method was used. An evaluation test was conducted and the results are shown in the table.

比較例3 ガラス管収束剤として、上記実施例2で得られた水素添
加前の重合体を使用した点を除いては上記実施例1と同
様にしてガラス短管を製造し、かつ、同様の評価試験を
行なって結果を表に示した。
Comparative Example 3 A short glass tube was produced in the same manner as in Example 1 above, except that the polymer before hydrogenation obtained in Example 2 above was used as a glass tube sizing agent, and the same method was used. An evaluation test was conducted and the results are shown in the table.

[発明の効果] 以上の説明から明らかなように、本発明のガラス管収束
剤はガラス管の収束・固着性に優れていることは言うま
でもなく、とくに、溶融時の熱安定性、無臭性、非引火
性ならびに溶剤に対する溶解性の点で、従来のガラス管
収束剤に比べてはるかに優れたものであるため、なかで
も電子・電気回路素子等の製造分野においてその工業的
価値は極めて大である。
[Effects of the Invention] As is clear from the above explanation, it goes without saying that the glass tube binding agent of the present invention is excellent in binding and fixing properties of glass tubes, and particularly has excellent thermal stability during melting, odorlessness, It is far superior to conventional glass tube sizing agents in terms of non-flammability and solubility in solvents, so its industrial value is extremely high, especially in the field of manufacturing electronic and electrical circuit elements. be.

Claims (1)

【特許請求の範囲】[Claims] シクロペンタジエン系重合体および/またはシクロペン
タジエン系化合物−ビニル置換芳香族炭化水素共重合体
の水素添加物よりなることを特徴とするガラス管収束剤
A glass tube binding agent comprising a hydrogenated product of a cyclopentadiene polymer and/or a cyclopentadiene compound-vinyl-substituted aromatic hydrocarbon copolymer.
JP15230885A 1985-07-12 1985-07-12 Glass tube collecting agent Pending JPS6217051A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP15230885A JPS6217051A (en) 1985-07-12 1985-07-12 Glass tube collecting agent

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP15230885A JPS6217051A (en) 1985-07-12 1985-07-12 Glass tube collecting agent

Publications (1)

Publication Number Publication Date
JPS6217051A true JPS6217051A (en) 1987-01-26

Family

ID=15537685

Family Applications (1)

Application Number Title Priority Date Filing Date
JP15230885A Pending JPS6217051A (en) 1985-07-12 1985-07-12 Glass tube collecting agent

Country Status (1)

Country Link
JP (1) JPS6217051A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5171793A (en) * 1990-02-22 1992-12-15 Exxon Chemical Patents Inc. Hydrogenated resins, adhesive formulations and process for production of resins

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5171793A (en) * 1990-02-22 1992-12-15 Exxon Chemical Patents Inc. Hydrogenated resins, adhesive formulations and process for production of resins

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