JPS62506A - Hydrocarbon resin - Google Patents
Hydrocarbon resinInfo
- Publication number
- JPS62506A JPS62506A JP13914385A JP13914385A JPS62506A JP S62506 A JPS62506 A JP S62506A JP 13914385 A JP13914385 A JP 13914385A JP 13914385 A JP13914385 A JP 13914385A JP S62506 A JPS62506 A JP S62506A
- Authority
- JP
- Japan
- Prior art keywords
- vinyl
- substituted aromatic
- cyclopentadiene
- hydrocarbon
- hydrocarbon resin
- 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.)
- Granted
Links
Landscapes
- Addition Polymer Or Copolymer, Post-Treatments, Or Chemical Modifications (AREA)
Abstract
Description
【発明の詳細な説明】
[産業上の利用分野]
本発明は、炭化水素樹脂に関し、さらに詳しくは、熱可
塑性樹脂または天然もしくは合成ゴムとの相溶性に優れ
、とくに、感圧粘着剤やホットメルト型接着剤の粘着性
付与剤として有用な炭化水素樹脂に関する。Detailed Description of the Invention [Industrial Application Field] The present invention relates to hydrocarbon resins, and more specifically, they have excellent compatibility with thermoplastic resins or natural or synthetic rubbers, and are particularly suitable for use in pressure-sensitive adhesives and hot-pressure adhesives. This invention relates to hydrocarbon resins useful as tackifiers for melt-type adhesives.
[従来技術]
感圧粘着剤やホットメルト型接着剤などの接着剤は、熱
可塑性樹脂または天然もしくは合成ゴムを粘着主剤とし
、これに、粘着性付与剤および必要に応じて可塑剤や充
填剤等を配合してなるものが大部分を占めている。[Prior art] Adhesives such as pressure-sensitive adhesives and hot-melt adhesives have a thermoplastic resin or natural or synthetic rubber as the main adhesive, and a tackifier and, if necessary, a plasticizer or filler. Most of the products are made by blending the following.
この粘着性付与剤としては、従来、例えば、シクロペン
タジェンとスチレンなどのビニル置換芳香族炭化水素と
を共重合せしめて得られる共重合体を水素添加してなる
炭化水素樹脂が知られている。As this tackifier, a hydrocarbon resin is conventionally known, which is obtained by hydrogenating a copolymer obtained by copolymerizing cyclopentadiene and a vinyl-substituted aromatic hydrocarbon such as styrene. .
[発明が解決しようとする問題]
従来のかかる炭化水素樹脂としては、主として、 O〜
3の臭素価を有するものが汎用されている。このものは
、たしかに、接着剤の粘着力、粘着保持力および熱安定
性等の増大に寄与するが、しかし、主剤である熱可塑性
樹脂や天然もしくは合成ゴム、とくにゴムとの相溶性か
悪いという不都合がある。そのため、接着剤の調製にあ
たっては、まず、この炭化水素樹脂とゴム等の粘着主剤
とを、ペンタンやベンゼン等の溶媒に溶解せしめて混合
し、この混合液を被接着領域に塗布したのち乾燥する必
要があり、工程的にみても極めて煩雑であるという問題
があった。[Problem to be solved by the invention] Conventional hydrocarbon resins mainly include O~
Those having a bromine number of 3 are commonly used. This material certainly contributes to increasing the adhesive force, adhesive holding power, and thermal stability of adhesives, but it has poor compatibility with thermoplastic resins and natural or synthetic rubbers, especially rubbers, which are the main ingredients. There is an inconvenience. Therefore, when preparing an adhesive, first, this hydrocarbon resin and a main adhesive agent such as rubber are dissolved and mixed in a solvent such as pentane or benzene, and this mixture is applied to the area to be bonded and then dried. There was a problem in that it was necessary and extremely complicated from a process standpoint.
[問題を解決するための手段]
本発明は、従来のかかる問題を解消し、熱可塑性樹脂や
天然もしくは合成ゴムとの相溶性に優れており、接着剤
の粘着性付与剤として有用な炭化水素樹脂の提供を目的
とする。[Means for Solving the Problems] The present invention solves the conventional problems and provides hydrocarbons that have excellent compatibility with thermoplastic resins and natural or synthetic rubbers and are useful as tackifiers for adhesives. The purpose is to provide resin.
本発明者らは、得られる炭化水素樹脂の臭素価に着目し
て鋭意検討を重ねた結果、該臭素価が後述する範囲のと
きに上記目的を達成することを確認して本発明を完成す
るに到った。As a result of intensive studies focusing on the bromine number of the obtained hydrocarbon resin, the present inventors confirmed that the above object is achieved when the bromine number falls within the range described below, and completed the present invention. reached.
すなわち、本発明の炭化水素樹脂は、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
添加物であって、3を超え、かつ7以下の臭素価を有す
ることを特徴とする。That is, the hydrocarbon resin of the present invention is a hydrogenated product of a cyclopentadiene compound-vinyl-substituted aromatic hydrocarbon copolymer, and is characterized by having a bromine number of more than 3 and less than or equal to 7. .
[具体的説明]
本発明の炭化水素樹脂は、前述したように、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
合体の水素添加物であって、その臭素価は3を超え、か
つ7以下であることが必要とされる。この臭素価が3以
下である場合には、該炭化水素樹脂の熱可塑性樹脂また
は天然もしくは合成ゴムに対する相溶性が低下するので
好ましくない。一方、臭素価が7を超える場合には。[Specific Description] As mentioned above, the hydrocarbon resin of the present invention is a hydrogenated product of a copolymer of a cyclopentadiene compound and a vinyl-substituted aromatic hydrocarbon, and has a bromine number of more than 3. , and is required to be 7 or less. When the bromine number is 3 or less, the compatibility of the hydrocarbon resin with the thermoplastic resin or natural or synthetic rubber decreases, which is not preferable. On the other hand, when the bromine number exceeds 7.
上記した相溶性低下の問題はないが、該炭化水素樹脂自
体の熱安定性ならびに耐候性が劣化するという不都合が
生ずる。臭素価の好ましい値は3.5〜6.0である。Although there is no problem of decreased compatibility as described above, there is a disadvantage that the thermal stability and weather resistance of the hydrocarbon resin itself are deteriorated. The preferred value of the bromine number is 3.5 to 6.0.
本発明の炭化水素樹脂は次のようにして製造される。The hydrocarbon resin of the present invention is produced as follows.
すなわち、まず、上述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反応により両者
を共重合成分とする共重合体を製造する。That is, first, a copolymer containing the above-described cyclopentadiene compound and a vinyl-substituted aromatic hydrocarbon as copolymerization components is produced by a copolymerization reaction of the above-mentioned cyclopentadiene compound and a vinyl-substituted aromatic hydrocarbon.
このとき使用するシクロペンタジェン化合物としては、
とくに限定されるものではなく、例えば、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をあげることができ、なかでも
シクロペンタジェン、ジシクロペンタジェンは好ましい
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
ェンとしてもよい、また、使用するビニル置換芳香族炭
化水としては、とくに限定されるものではなく、例エバ
、スチレン、α−メチルスチレン、ビニルトルエン、イ
ソプロピルベンゼ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。The cyclopentadiene compound used at this time is
It is not particularly limited, and examples include cyclopentadiene, methylcyclopentadiene, ethylcyclopentadiene, dimers, trimers, or codimers thereof. Among them, cyclopentadiene and dicyclopentadiene 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. The vinyl-substituted aromatic hydrocarbon used is not particularly limited, and examples include EVA, styrene, and α-methyl. Examples include styrene, vinyltoluene, and isopropylbenzene. 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80〜30重量%、ビニル置換芳香族炭化水素が20
〜70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 80 to 30% by weight, and the vinyl-substituted aromatic hydrocarbon is 20% by weight.
It is preferable to set the usage amount of each component so that the total amount is 100% by weight at 70% by weight.
なお、この共重合反応における反応条件は1反応源度が
220〜320℃、好ましくは、250〜300℃、反
応時間が1〜8時間、好ましくは 1.5〜5時間、圧
力がO〜30 kg/cnsG 、好ましくは5〜20
kg/cydGとなるように設定される。また、反応
に際しては必要に応じてキシレン、トルエンなどの溶媒
を使用してもよい。The reaction conditions for this copolymerization reaction are as follows: 1 reaction degree is 220 to 320°C, preferably 250 to 300°C, reaction time is 1 to 8 hours, preferably 1.5 to 5 hours, and pressure is 0 to 30°C. kg/cnsG, preferably 5-20
kg/cydG. Further, during the reaction, a solvent such as xylene or toluene may be used as necessary.
ついで、このようにして得られた共重合体に水素添加せ
しめることにより、水素添加共重合体、すなわち、目的
とする本発明の炭化水素樹脂を得る。この工程において
、使用する触媒としては、例えば、旧、 Pd、 Go
、 Pt、 Rh系の触媒をあげることができる。また
、反応に際して、シクロヘキサン、テトラヒドロフラン
などの溶媒を必要に応じて使用してもよい、なお、反応
条件は前述した臭素価を達成するように設定することが
好ましく、反応温度は130〜300℃、好ましくは、
150〜260℃、反応時間は1〜7時間、好ましくは
、2 ′〜5時間に設定する。なお、この工程におけ
る芳香環水素添加度は80%以下となる。そして、この
ようにして得られた炭化水素樹脂のガードナー色度は
1以下であり、かつその軟化点は50−185℃程度で
ある。Next, the thus obtained copolymer is hydrogenated to obtain a hydrogenated copolymer, that is, the desired hydrocarbon resin of the present invention. In this step, examples of catalysts used include old, Pd, and Go.
, Pt, and Rh-based catalysts. Further, during the reaction, a solvent such as cyclohexane or tetrahydrofuran may be used as necessary.The reaction conditions are preferably set to achieve the above-mentioned bromine number, and the reaction temperature is 130 to 300°C. Preferably,
The temperature is set at 150-260°C and the reaction time is set at 1-7 hours, preferably 2'-5 hours. Note that the degree of aromatic ring hydrogenation in this step is 80% or less. The Gardner chromaticity of the hydrocarbon resin obtained in this way is
1 or less, and its softening point is about 50-185°C.
[実施例]
実施例1〜3、比較例1〜3
内容積 1交のオートクレーブに、シクロペンタジェン
200g (仕込みはジシクロペンタジェン)スチレン
200gおよびキシレン2QOgを仕込み、温度260
°C1圧力12kg/cr+fGにおいて2時間共重合
反応を行なわせた。これにより、共重合体360gを得
た。このもの軟化点は 102℃、臭素価は57、色相
を表わすガードナー色度は5であった。[Example] Examples 1 to 3, Comparative Examples 1 to 3 Inner volume 200 g of cyclopentadiene (prepared with dicyclopentadiene) and 2 QOg of xylene were charged into a single-cross autoclave, and the temperature was 260 g.
The copolymerization reaction was carried out for 2 hours at °C1 pressure of 12 kg/cr+fG. As a result, 360 g of copolymer was obtained. This material had a softening point of 102°C, a bromine number of 57, and a Gardner chromaticity of 5.
このようにして得られた共重合体に対し表示した各条件
で水素添加を行ない目的とする炭化水素樹脂を得た。ま
た、水素添加触媒としては、 0.5重量%のPdを含
有する Pd−シリカ・アルミナ触媒を使用した。The copolymer thus obtained was subjected to hydrogenation under the conditions indicated to obtain the desired hydrocarbon resin. Further, as a hydrogenation catalyst, a Pd-silica alumina catalyst containing 0.5% by weight of Pd was used.
かかる炭化水素樹脂の軟化点、臭素価、色相(ガードナ
ー色度)、芳香環水素添加度を表中に示した。The softening point, bromine number, hue (Gardner chromaticity), and degree of aromatic ring hydrogenation of the hydrocarbon resin are shown in the table.
さらに、これらの炭化水素樹脂について、下記の各評価
試験を行なった。Furthermore, the following evaluation tests were conducted on these hydrocarbon resins.
(1)相溶性評価試験
天然ゴムおよび5BR(日本合成ゴム■製11507S
BR)に対する炭化水素樹脂の相溶性を調べた。すなわ
ち天然ゴム (又は5BR)とトルエンと炭化水素樹脂
とを重量比1:l+1で均一に混合してなる溶液をガラ
ス板りに塗布し、トルエンを除去した後の透明度を目視
観察により評価し、透明なものを0、不透明なものを×
1両者の中間をΔで示した。(1) Compatibility evaluation test Natural rubber and 5BR (11507S manufactured by Japan Synthetic Rubber)
The compatibility of hydrocarbon resin with BR) was investigated. That is, a solution made by uniformly mixing natural rubber (or 5BR), toluene, and hydrocarbon resin at a weight ratio of 1:1+1 is applied to a glass plate, and the transparency after removing toluene is evaluated by visual observation. 0 for transparent, × for opaque
1 The middle point between the two is indicated by Δ.
(2)熱安定性評価試験
炭化水素樹脂試料logを内容積20ccのSOS製開
放容器に採取し、この容器を 150℃の熱風乾燥機中
に20時間放置した後の粘度変化をB型粘度計により測
定し、初期粘度に対する粘度上昇率(%)を算出した。(2) Thermal stability evaluation test The hydrocarbon resin sample log was collected in an SOS open container with an internal volume of 20 cc, and the viscosity change after leaving the container in a hot air dryer at 150°C for 20 hours was measured using a B-type viscometer. The viscosity increase rate (%) with respect to the initial viscosity was calculated.
3)耐候性評価試験
炭化水素樹脂試料を +00m+sX 50mmX 5
m信のシート金型内で溶融させたのち冷却せしめること
により樹脂プレートを得た。この樹脂プレートに対し、
キセノンウェザ−テスター (東洋精機製作所部)を使
用して 100時間の耐候試験を実施したのちの着色の
変化を目視観察により評価し1着色の変化の少ないもの
を0、着色の著しいものをXで示した。3) Weather resistance evaluation test hydrocarbon resin sample +00m+sX 50mmX 5
A resin plate was obtained by melting the resin in a metal sheet mold and then cooling it. For this resin plate,
After conducting a 100-hour weather test using a xenon weather tester (Toyo Seiki Seisakusho Department), the changes in coloring were evaluated by visual observation. Indicated.
以上の評価試験(1)〜(3)の結果を一括して表中に
併記した。The results of the above evaluation tests (1) to (3) are listed together in the table.
[発明の効果]
以上の説明から明らかなように、本発明の炭化水素樹脂
は、熱可塑性樹脂および天然もしくは合成ゴム、とくに
ゴムとの相溶性に優れており、しかも、それ自身の熱安
定性および耐候性にも優れているため、感圧粘着剤やホ
ットメルト型接着剤の粘着性付与剤として極めて有用で
あり、その工業的価値は大である。[Effects of the Invention] As is clear from the above explanation, the hydrocarbon resin of the present invention has excellent compatibility with thermoplastic resins and natural or synthetic rubber, especially rubber, and has excellent thermal stability. Since it also has excellent weather resistance, it is extremely useful as a tackifier for pressure-sensitive adhesives and hot-melt adhesives, and has great industrial value.
Claims (1)
素共重合体の水素添加物であって、3を超え、かつ7以
下の臭素価を有することを特徴とする炭化水素樹脂。A hydrocarbon resin, which is a hydrogenated product of a cyclopentadiene compound-vinyl-substituted aromatic hydrocarbon copolymer, and has a bromine number of more than 3 and less than or equal to 7.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP13914385A JPS62506A (en) | 1985-06-27 | 1985-06-27 | Hydrocarbon resin |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP13914385A JPS62506A (en) | 1985-06-27 | 1985-06-27 | Hydrocarbon resin |
Publications (2)
Publication Number | Publication Date |
---|---|
JPS62506A true JPS62506A (en) | 1987-01-06 |
JPH0566401B2 JPH0566401B2 (en) | 1993-09-21 |
Family
ID=15238559
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP13914385A Granted JPS62506A (en) | 1985-06-27 | 1985-06-27 | Hydrocarbon resin |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS62506A (en) |
Cited By (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH01165604A (en) * | 1987-12-21 | 1989-06-29 | Arakawa Chem Ind Co Ltd | Decoloration of petroleum resin through hydrogenation |
US5126868A (en) * | 1988-12-27 | 1992-06-30 | Casio Computer Co., Ltd. | Color compensated double layered liquid crystal display device |
US5171793A (en) * | 1990-02-22 | 1992-12-15 | Exxon Chemical Patents Inc. | Hydrogenated resins, adhesive formulations and process for production of resins |
WO1994002521A1 (en) * | 1992-07-28 | 1994-02-03 | Nippon Zeon Co., Ltd. | Hydrogenated resin |
WO2004003041A1 (en) * | 2002-06-26 | 2004-01-08 | Idemitsu Kosan Co., Ltd. | High-softening-point copolymer, process for producing the same, and product of hydrogenation thereof |
WO2007148530A1 (en) * | 2006-06-22 | 2007-12-27 | Kansai Paint Co., Ltd. | Powder coating material, process for producing the same, and method of forming coating film with use of powder coating material |
Families Citing this family (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN104945560B (en) * | 2015-06-29 | 2017-11-21 | 安徽同心化工有限公司 | A kind of phenylethene modified dicyclopentadiene petroleum resin of hydrogenation and preparation method thereof |
Citations (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS52140591A (en) * | 1976-05-20 | 1977-11-24 | Nippon Zeon Co Ltd | Novel hydrogenated hydrocarbon resisn |
JPS6128508A (en) * | 1984-07-18 | 1986-02-08 | Mitsui Petrochem Ind Ltd | Novel hydrocarbon resin and adhesive additive formed therefrom |
-
1985
- 1985-06-27 JP JP13914385A patent/JPS62506A/en active Granted
Patent Citations (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS52140591A (en) * | 1976-05-20 | 1977-11-24 | Nippon Zeon Co Ltd | Novel hydrogenated hydrocarbon resisn |
JPS6128508A (en) * | 1984-07-18 | 1986-02-08 | Mitsui Petrochem Ind Ltd | Novel hydrocarbon resin and adhesive additive formed therefrom |
Cited By (10)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH01165604A (en) * | 1987-12-21 | 1989-06-29 | Arakawa Chem Ind Co Ltd | Decoloration of petroleum resin through hydrogenation |
US5126868A (en) * | 1988-12-27 | 1992-06-30 | Casio Computer Co., Ltd. | Color compensated double layered liquid crystal display device |
US5171793A (en) * | 1990-02-22 | 1992-12-15 | Exxon Chemical Patents Inc. | Hydrogenated resins, adhesive formulations and process for production of resins |
EP0666273A2 (en) * | 1990-02-22 | 1995-08-09 | Exxon Chemical Patents Inc. | Hydrogenated resins, adhesive formulations and process for production of resins |
EP0666273A3 (en) * | 1990-02-22 | 1995-11-08 | Exxon Chemical Patents Inc | Hydrogenated resins, adhesive formulations and process for production of resins. |
WO1994002521A1 (en) * | 1992-07-28 | 1994-02-03 | Nippon Zeon Co., Ltd. | Hydrogenated resin |
WO2004003041A1 (en) * | 2002-06-26 | 2004-01-08 | Idemitsu Kosan Co., Ltd. | High-softening-point copolymer, process for producing the same, and product of hydrogenation thereof |
US7196143B2 (en) | 2002-06-26 | 2007-03-27 | Idemitsu Kosan Co., Ltd. | High-softening-point copolymer, process for producing the same, and product of hydrogenation thereof |
WO2007148530A1 (en) * | 2006-06-22 | 2007-12-27 | Kansai Paint Co., Ltd. | Powder coating material, process for producing the same, and method of forming coating film with use of powder coating material |
JPWO2007148530A1 (en) * | 2006-06-22 | 2009-11-19 | 関西ペイント株式会社 | Powder coating, powder coating manufacturing method, and coating film forming method using powder coating |
Also Published As
Publication number | Publication date |
---|---|
JPH0566401B2 (en) | 1993-09-21 |
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