JPH0436305A - Impact-resistant styrenic resin - Google Patents
Impact-resistant styrenic resinInfo
- Publication number
- JPH0436305A JPH0436305A JP14010390A JP14010390A JPH0436305A JP H0436305 A JPH0436305 A JP H0436305A JP 14010390 A JP14010390 A JP 14010390A JP 14010390 A JP14010390 A JP 14010390A JP H0436305 A JPH0436305 A JP H0436305A
- Authority
- JP
- Japan
- Prior art keywords
- resin
- impact
- rubber
- content
- styrenic
- 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
- 229920001890 Novodur Polymers 0.000 title claims abstract description 26
- 229920001971 elastomer Polymers 0.000 claims abstract description 31
- 239000005060 rubber Substances 0.000 claims abstract description 31
- 239000002245 particle Substances 0.000 claims abstract description 27
- 229920005989 resin Polymers 0.000 claims abstract description 24
- 239000011347 resin Substances 0.000 claims abstract description 24
- 230000008961 swelling Effects 0.000 claims abstract description 12
- 229920000642 polymer Polymers 0.000 claims description 16
- 229920002857 polybutadiene Polymers 0.000 claims description 15
- YXFVVABEGXRONW-UHFFFAOYSA-N Toluene Chemical compound CC1=CC=CC=C1 YXFVVABEGXRONW-UHFFFAOYSA-N 0.000 claims description 12
- 239000005062 Polybutadiene Substances 0.000 claims description 9
- 239000004609 Impact Modifier Substances 0.000 abstract 1
- PPBRXRYQALVLMV-UHFFFAOYSA-N Styrene Chemical compound C=CC1=CC=CC=C1 PPBRXRYQALVLMV-UHFFFAOYSA-N 0.000 description 19
- 238000000034 method Methods 0.000 description 16
- 230000000704 physical effect Effects 0.000 description 16
- 238000006116 polymerization reaction Methods 0.000 description 11
- 239000000243 solution Substances 0.000 description 9
- 230000000052 comparative effect Effects 0.000 description 7
- 238000003756 stirring Methods 0.000 description 6
- 239000013013 elastic material Substances 0.000 description 5
- 239000007788 liquid Substances 0.000 description 4
- 239000000178 monomer Substances 0.000 description 4
- 239000000047 product Substances 0.000 description 4
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 3
- 238000005259 measurement Methods 0.000 description 3
- 239000003505 polymerization initiator Substances 0.000 description 3
- MYRTYDVEIRVNKP-UHFFFAOYSA-N 1,2-Divinylbenzene Chemical compound C=CC1=CC=CC=C1C=C MYRTYDVEIRVNKP-UHFFFAOYSA-N 0.000 description 2
- 239000005063 High cis polybutadiene Substances 0.000 description 2
- 229920001577 copolymer Polymers 0.000 description 2
- 230000007423 decrease Effects 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 238000004519 manufacturing process Methods 0.000 description 2
- 239000000203 mixture Substances 0.000 description 2
- 238000000465 moulding Methods 0.000 description 2
- 239000004014 plasticizer Substances 0.000 description 2
- 230000000379 polymerizing effect Effects 0.000 description 2
- 238000010926 purge Methods 0.000 description 2
- GJBRNHKUVLOCEB-UHFFFAOYSA-N tert-butyl benzenecarboperoxoate Chemical compound CC(C)(C)OOC(=O)C1=CC=CC=C1 GJBRNHKUVLOCEB-UHFFFAOYSA-N 0.000 description 2
- FRQQKWGDKVGLFI-UHFFFAOYSA-N 2-methylundecane-2-thiol Chemical compound CCCCCCCCCC(C)(C)S FRQQKWGDKVGLFI-UHFFFAOYSA-N 0.000 description 1
- NLHHRLWOUZZQLW-UHFFFAOYSA-N Acrylonitrile Chemical compound C=CC#N NLHHRLWOUZZQLW-UHFFFAOYSA-N 0.000 description 1
- 239000004610 Internal Lubricant Substances 0.000 description 1
- 239000005064 Low cis polybutadiene Substances 0.000 description 1
- VVQNEPGJFQJSBK-UHFFFAOYSA-N Methyl methacrylate Chemical compound COC(=O)C(C)=C VVQNEPGJFQJSBK-UHFFFAOYSA-N 0.000 description 1
- 239000004793 Polystyrene Substances 0.000 description 1
- 235000021355 Stearic acid Nutrition 0.000 description 1
- 238000002835 absorbance Methods 0.000 description 1
- 239000000654 additive Substances 0.000 description 1
- 239000003963 antioxidant agent Substances 0.000 description 1
- 239000002216 antistatic agent Substances 0.000 description 1
- 238000005452 bending Methods 0.000 description 1
- 238000012662 bulk polymerization Methods 0.000 description 1
- 239000012986 chain transfer agent Substances 0.000 description 1
- 238000006243 chemical reaction Methods 0.000 description 1
- 239000003795 chemical substances by application Substances 0.000 description 1
- 238000007796 conventional method Methods 0.000 description 1
- 230000018044 dehydration Effects 0.000 description 1
- 238000006297 dehydration reaction Methods 0.000 description 1
- 229910001873 dinitrogen Inorganic materials 0.000 description 1
- GVGUFUZHNYFZLC-UHFFFAOYSA-N dodecyl benzenesulfonate;sodium Chemical compound [Na].CCCCCCCCCCCCOS(=O)(=O)C1=CC=CC=C1 GVGUFUZHNYFZLC-UHFFFAOYSA-N 0.000 description 1
- 238000001035 drying Methods 0.000 description 1
- 238000010528 free radical solution polymerization reaction Methods 0.000 description 1
- 239000012760 heat stabilizer Substances 0.000 description 1
- 238000009776 industrial production Methods 0.000 description 1
- 238000002347 injection Methods 0.000 description 1
- 239000007924 injection Substances 0.000 description 1
- 238000001746 injection moulding Methods 0.000 description 1
- 239000000314 lubricant Substances 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 238000000691 measurement method Methods 0.000 description 1
- 239000000155 melt Substances 0.000 description 1
- 239000002480 mineral oil Substances 0.000 description 1
- 235000010446 mineral oil Nutrition 0.000 description 1
- 238000002156 mixing Methods 0.000 description 1
- 239000006082 mold release agent Substances 0.000 description 1
- 238000006386 neutralization reaction Methods 0.000 description 1
- 229910052757 nitrogen Inorganic materials 0.000 description 1
- QIQXTHQIDYTFRH-UHFFFAOYSA-N octadecanoic acid Chemical compound CCCCCCCCCCCCCCCCCC(O)=O QIQXTHQIDYTFRH-UHFFFAOYSA-N 0.000 description 1
- OQCDKBAXFALNLD-UHFFFAOYSA-N octadecanoic acid Natural products CCCCCCCC(C)CCCCCCCCC(O)=O OQCDKBAXFALNLD-UHFFFAOYSA-N 0.000 description 1
- 150000001451 organic peroxides Chemical class 0.000 description 1
- 239000008188 pellet Substances 0.000 description 1
- 229920002223 polystyrene Polymers 0.000 description 1
- 229920002102 polyvinyl toluene Polymers 0.000 description 1
- -1 polyα-methylstyrene Polymers 0.000 description 1
- 239000002994 raw material Substances 0.000 description 1
- 229940080264 sodium dodecylbenzenesulfonate Drugs 0.000 description 1
- 239000008117 stearic acid Substances 0.000 description 1
- 229920003048 styrene butadiene rubber Polymers 0.000 description 1
- 239000006228 supernatant Substances 0.000 description 1
- 238000010558 suspension polymerization method Methods 0.000 description 1
- 238000012360 testing method Methods 0.000 description 1
- 125000000391 vinyl group Chemical group [H]C([*])=C([H])[H] 0.000 description 1
- 229920002554 vinyl polymer Polymers 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 1
Landscapes
- Compositions Of Macromolecular Compounds (AREA)
- Graft Or Block Polymers (AREA)
Abstract
Description
【発明の詳細な説明】
[産業上の利用分野]
本発明は、強度、流動性、光沢に優れた耐衝撃性スチレ
ン系樹脂に関し、さらに詳しくは、連続するスチレン系
重合体の分子量、強靭化剤として使用するゴムの種類と
含有量、樹脂中に分散しているグラフトされたゴム粒子
の粒子径、樹脂の膨潤度・ゲル含有量が特定の範囲内に
ある、実用的な耐衝撃強度、成形加工性1表面光沢に優
れた耐衝撃性スチレン系樹脂に関する。[Detailed Description of the Invention] [Industrial Application Field] The present invention relates to impact-resistant styrenic resins with excellent strength, fluidity, and gloss, and more particularly, to the molecular weight and toughening of continuous styrenic polymers. The type and content of the rubber used as the agent, the particle size of the grafted rubber particles dispersed in the resin, the degree of swelling and gel content of the resin are within specific ranges, and the practical impact resistance is achieved. Molding processability 1: Concerning impact-resistant styrenic resin with excellent surface gloss.
[従来の技術]
従来、スチレン系樹脂は硬質で脆い性質であるため、ゴ
ム状弾性体とスチレン系樹脂をブレンドしたり、ゴム状
弾性体の存在下にスチレン系単量体を重合して耐衝撃性
スチレン系樹脂とする方法等により改良されている。[Prior Art] Conventionally, since styrene resin is hard and brittle, it has been difficult to improve the resistance by blending a rubbery elastic material with a styrene resin or by polymerizing a styrene monomer in the presence of a rubbery elastic material. It has been improved by making it into an impact-resistant styrene resin.
通常、耐衝撃性スチレン系樹脂を射出成形法により成形
した成形品は、弱電機器、事務用機器。Molded products made from impact-resistant styrene resin using injection molding are usually used for light electrical equipment and office equipment.
雑貨等の産業分野、具体的にはテレビ、ラジオ。Industrial fields such as miscellaneous goods, specifically television and radio.
クリーナー、エアコン等のハウジング類に利用されてい
る。最近、射出成形品の利用分野、特に大型成形品の分
野では、耐衝撃性スチレン系樹脂に対し、高い耐衝撃性
とともに成形加工性、さらには耐熱性、高光沢等の高度
の品質バランスが要求されている。Used in housings for cleaners, air conditioners, etc. Recently, in the field of application of injection molded products, especially in the field of large molded products, a high quality balance such as high impact resistance, moldability, heat resistance, and high gloss is required for impact-resistant styrene resins. has been done.
従来より、スチレン系樹脂の個々の性質の改善について
は種々の提案がなされているが、これらの提案はいずれ
も品質間のバランスのよい耐衝撃性スチレン系樹脂を得
る方法としては、必ずしも満足できるものではなかった
。Various proposals have been made to improve the individual properties of styrenic resins, but none of these proposals is necessarily satisfactory as a method for obtaining impact-resistant styrenic resins with a good balance between qualities. It wasn't something.
スチレン系樹脂の耐衝撃性の向上には、周知のように、
スチレン系樹脂に含有されるゴム状弾性体の含有量を増
大することが有効であるされているが、ゴム状弾性体の
含有量が増大すると、次第にそのスチレン系単量体溶液
の粘度が上昇し、工業的製造における重合液の撹拌ある
いは輸送の面で好ましくない欠点があった。また、物性
面からも、ゴム状弾性体の含有量の高い耐衝撃性スチレ
ン系樹脂は、剛性、すなわち引張強度や曲げ強度が著し
く低下し、軟弱な樹脂となるので、物性のバランス上好
ましくない。As is well known, to improve the impact resistance of styrene resin,
It is effective to increase the content of rubbery elastic material contained in styrenic resin, but as the content of rubbery elastic material increases, the viscosity of the styrenic monomer solution gradually increases. However, it has disadvantages in terms of stirring or transportation of the polymerization solution in industrial production. In addition, from the viewpoint of physical properties, impact-resistant styrene resins with a high content of rubber-like elastic material are unfavorable in terms of the balance of physical properties, as the rigidity, that is, the tensile strength and bending strength, decreases significantly and the resin becomes weak. .
また、成形性を向上させるためには、白色鉱油等の可塑
剤や、ステアリン酸等の内部潤滑剤を添加する方法が一
般に知られているが、これらを多く添加すると耐熱性の
低下が避けられない欠点があった。Additionally, in order to improve moldability, it is generally known to add a plasticizer such as white mineral oil or an internal lubricant such as stearic acid, but adding a large amount of these may prevent a decrease in heat resistance. There were no drawbacks.
[発明が解決しようとする課題]
そこで、本発明者等は、これらの欠点を解決すべく鋭意
検討を重ねた結果、スチレン系重合体中に、グラフトさ
れたゴム粒子を分散してなる耐衝撃性スチレン系樹脂に
おいて、特定の連続するスチレン系重合体の分子量、特
定のゴムの種類と含有量、特定のグラフトされたゴム粒
子の粒子径、特定の樹脂の膨潤度・ゲル含有量に調整す
ることにより、実用的な耐衝撃強度、成形加工性、さら
に表面光沢に優れた耐衝撃性スチレン系樹脂を完成する
に至った。[Problems to be Solved by the Invention] Therefore, as a result of intensive studies to solve these drawbacks, the present inventors have developed an impact-resistant material made by dispersing grafted rubber particles in a styrene polymer. In styrenic resins, adjustments are made to the molecular weight of a specific continuous styrenic polymer, the type and content of a specific rubber, the particle size of a specific grafted rubber particle, and the degree of swelling and gel content of a specific resin. As a result, we have completed an impact-resistant styrenic resin that has excellent impact resistance, moldability, and surface gloss for practical use.
[課題を解決するための手段]
すなわち、本発明は、連続するスチレン系重合体中に、
グラフトされたゴム粒子を分散して含有し、かつゴムが
シス1,4結合が90モル%以上のポリブタジェンでそ
の含有量が5〜15重量%である耐衝撃性スチレン系樹
脂において、
(A)連続するスチレン系重合体の重量平均分子量が1
5〜25万
(B)グラフトされたゴム粒子の体積平均粒径が1.3
〜2.3μm
(C)樹脂のトルエン中の膨潤度が9以上(D)樹脂の
ゲル含有量(GEL)とゴム含有量(PBD)の比(G
EL/PBD)が2〜3
の範囲にあることを特徴とする耐衝撃性スチレン系樹脂
である。[Means for Solving the Problems] That is, the present invention provides a continuous styrenic polymer containing:
In an impact-resistant styrenic resin containing dispersed grafted rubber particles, and the rubber is polybutadiene with cis-1,4 bonds of 90 mol% or more and the content thereof is 5 to 15% by weight, (A) The weight average molecular weight of the continuous styrenic polymer is 1
50,000 to 250,000 (B) The volume average particle size of the grafted rubber particles is 1.3
~2.3 μm (C) The degree of swelling of the resin in toluene is 9 or more (D) The ratio of gel content (GEL) to rubber content (PBD) of the resin (G
It is an impact-resistant styrenic resin characterized by having an EL/PBD) of 2 to 3.
以下、本発明の詳細な説明する。The present invention will be explained in detail below.
本発明において、連続するスチレン系重合体は、ポリス
チレン、ポリα−メチルスチレン、ポリビニルトルエン
、ポリt−ブチルスチレン等の単独または共重合体であ
り、またアクリロニトリル、メタクリル酸メチル等との
共重合体であってもよい。In the present invention, the continuous styrenic polymer is a single or copolymer of polystyrene, polyα-methylstyrene, polyvinyltoluene, polyt-butylstyrene, etc., or a copolymer with acrylonitrile, methyl methacrylate, etc. It may be.
本発明において、連続するスチレン系重合体中に分散し
て含有するグラフトされたゴム粒子のゴムには、シス1
,4結合が90モル%以上のポリブタジェンが用いられ
る。一般に、ポリブタジェンは、スチレン系樹脂の耐衝
撃性の改善等の目的で同様に用いられるスチレン−ブタ
ジェン共重合体ゴムに比べて、低温耐衝撃性に優れた耐
衝撃性スチレン系樹脂が得られることから好ましいもの
である。しかし、シス1,4結合が低(90モル%未満
のポリブタジェンを使用すると、成形性が同程度の場合
は耐衝撃性が劣り、耐衝撃性が同程度の場合には成形性
が劣る等物性のバランスが悪(なる。In the present invention, the rubber of the grafted rubber particles dispersed and contained in the continuous styrenic polymer contains cis 1
, 4 bonds of 90 mol% or more is used. In general, polybutadiene can produce impact-resistant styrenic resins with superior low-temperature impact resistance compared to styrene-butadiene copolymer rubber, which is also used to improve the impact resistance of styrenic resins. It is preferable because However, if polybutadiene with low cis-1,4 bonds (less than 90 mol%) is used, the impact resistance will be inferior if the moldability is the same, and the moldability will be inferior if the impact resistance is the same. The balance is bad.
本発明の耐衝撃性スチレン系樹脂中のゴム含有量は通常
5〜15重量%、好ましくは7〜lO重量%が望ましい
。ゴム含有量が5重量%未満では実用的に満足できる程
の耐衝撃性は得られず、また15重量%を越えると製造
の際にゴムを溶解したスチレン系単量体溶液の粘度が上
昇して製造上に問題を生ずる。The rubber content in the impact-resistant styrenic resin of the present invention is usually 5 to 15% by weight, preferably 7 to 10% by weight. If the rubber content is less than 5% by weight, practically satisfactory impact resistance cannot be obtained, and if it exceeds 15% by weight, the viscosity of the styrenic monomer solution in which the rubber is dissolved increases during production. This causes manufacturing problems.
本発明の耐衝撃性スチレン系樹脂を製造するには、ポリ
ブタジェンの含有量が5〜15重量%となる様に、ポリ
ブタジェンをスチレン系単量体に溶解して得られたポリ
ブタジェン・スチレン系単量体溶液を原料として、公知
の重合方法、例えば塊状重合法、塊状−懸濁重合法ある
いは溶液重合法等により行なうことができる。In order to produce the impact-resistant styrenic resin of the present invention, polybutadiene/styrenic monomers obtained by dissolving polybutadiene in a styrenic monomer so that the polybutadiene content is 5 to 15% by weight. The polymerization can be carried out using a body solution as a raw material by a known polymerization method, such as a bulk polymerization method, a bulk-suspension polymerization method, or a solution polymerization method.
本発明において、重合温度は、80〜170℃の範囲が
好ましく、80℃未満では目的とする物性バランスの優
れた耐衝撃性スチレン系樹脂を得るのに長時間を要し、
170℃を越えると反応速度が過大となり円滑な重合
制御が困難となる。In the present invention, the polymerization temperature is preferably in the range of 80 to 170°C, and if it is less than 80°C, it will take a long time to obtain the desired impact-resistant styrenic resin with an excellent balance of physical properties.
If the temperature exceeds 170°C, the reaction rate becomes excessive and smooth polymerization control becomes difficult.
また、本発明においては、有機過酸化物等の重合開始剤
を用いることもできる。Further, in the present invention, a polymerization initiator such as an organic peroxide can also be used.
本発明の耐衝撃性スチレン系樹脂中の連続するスチレン
系重合体の重量平均分子量は、通常15〜25万、好ま
しくは17〜22万の範囲が望ましい。重量平均分子量
が15万未満であると耐衝撃性が劣り、25万を越える
と流動性が劣り、物性のバランスが悪くなる。なお、連
続するスチレン系重合体の分子量は、連鎖移動剤、重合
開始剤、重合温度等により調整することが出来る。The weight average molecular weight of the continuous styrenic polymer in the impact-resistant styrenic resin of the present invention is usually in the range of 150,000 to 250,000, preferably in the range of 170,000 to 220,000. If the weight average molecular weight is less than 150,000, the impact resistance will be poor, and if it exceeds 250,000, the fluidity will be poor and the balance of physical properties will be poor. The molecular weight of the continuous styrenic polymer can be adjusted by adjusting the chain transfer agent, polymerization initiator, polymerization temperature, etc.
本発明において、連続するスチレン系重合体中に分散し
て含有するグラフトされたゴム粒子の粒径は、体積平均
粒径で通常1.3〜2.3pm、好ましくは1.4〜2
.0pmの範囲が望ましい。平均体積粒径が1.3pm
未満であると耐衝撃性が劣り、2.31を越えると光沢
に劣り物性バランスが悪くなる。In the present invention, the particle size of the grafted rubber particles dispersed and contained in the continuous styrenic polymer is usually 1.3 to 2.3 pm, preferably 1.4 to 2 pm in terms of volume average particle size.
.. A range of 0 pm is desirable. Average volume particle size is 1.3pm
If it is less than 2.31, the impact resistance will be poor, and if it exceeds 2.31, the gloss will be poor and the balance of physical properties will be poor.
グラフトされたゴム粒子の粒径は重合時に使用するゴム
の分子量、重合中の撹拌速度等により調整することがで
きる。The particle size of the grafted rubber particles can be adjusted by adjusting the molecular weight of the rubber used during polymerization, the stirring speed during polymerization, etc.
本発明において、樹脂のトルエン中の膨張度は通常9以
上、好ましくはlO〜12の範囲が望ましい。膨潤度が
9未満であると耐衝撃性が劣るために好ましくない。な
お、膨潤度が12を越える場合には改良効果が少な(な
る。In the present invention, the expansion degree of the resin in toluene is usually 9 or more, preferably in the range of 10 to 12. If the degree of swelling is less than 9, the impact resistance will be poor, which is not preferable. Note that if the degree of swelling exceeds 12, the improvement effect will be small.
また、本発明は、樹脂のゲル含有量(GEL)とゴム含
有量(PBD)の比(GEL/PBD)が2〜3である
ことを特徴とする。GEL/PBDが2未満であると耐
衝撃性が劣り、3を越えると流動性が低下する。膨潤度
及びゲル含有量は、重合開始剤の種類・添加量、重合温
度等により調整することができる。Further, the present invention is characterized in that the ratio (GEL/PBD) of gel content (GEL) to rubber content (PBD) of the resin is 2 to 3. If GEL/PBD is less than 2, impact resistance will be poor, and if it exceeds 3, fluidity will be reduced. The degree of swelling and gel content can be adjusted by adjusting the type and amount of polymerization initiator, polymerization temperature, etc.
さらに、本発明の耐衝撃性スチレン系樹脂には、必要に
応じて、可塑剤、滑剤、離型剤、熱安定剤、酸化防止剤
、帯電防止剤等の公知の添加剤を添加することもできる
。Furthermore, known additives such as plasticizers, lubricants, mold release agents, heat stabilizers, antioxidants, and antistatic agents may be added to the impact-resistant styrenic resin of the present invention, if necessary. can.
本発明の耐衝撃性スチレン系樹脂は、ASTM D−2
56により測定されたアイゾツト衝撃強度が9.0kg
−cm/cm以上で、かつASTM D−1238によ
り測定されたメルトフローインデックスが1.8 g/
10分以上で、耐衝撃強度、成形加工性に優れ、また表
面光沢も良好である。The impact-resistant styrenic resin of the present invention is ASTM D-2
Izotsu impact strength measured by 56 is 9.0 kg
- cm/cm or more and the melt flow index measured by ASTM D-1238 is 1.8 g/cm.
If the molding time is 10 minutes or more, the impact strength and moldability are excellent, and the surface gloss is also good.
なお、本発明でいうポリブタジェンのミクロ構造、連続
するスチレン系重合体の分子量、連続するスチレン系重
合体中に分散して含有するグラフトされたゴム粒子の粒
径、樹脂の膨潤度・ゲル含有量、アイゾツト(Izod
)衝撃強度、メルトフローインデックス(MFI)は、
次の方法により測定される。In addition, the microstructure of the polybutadiene referred to in the present invention, the molecular weight of the continuous styrenic polymer, the particle size of the grafted rubber particles dispersed and contained in the continuous styrenic polymer, the swelling degree/gel content of the resin , Izod
) impact strength, melt flow index (MFI),
It is measured by the following method.
(1)ポリブタジェンのミクロ構造
日本分光IR−810を用いてモレロ法で測定を行い、
シス1,4結合、トランス1.4結合、ビニル1.2結
合の吸光度の比で示した。(1) Microstructure of polybutadiene Measured by Morello method using JASCO IR-810,
It is expressed as a ratio of absorbance of cis 1,4 bond, trans 1.4 bond, and vinyl 1.2 bond.
(2)連続するスチレン系重合体の分子量GPC(東ソ
ー側社製 HLC−802A)を用い、カラム(GMH
−612本直列にて測定を行い、重量平均分子量で示し
た。(2) Molecular weight of continuous styrenic polymer Column (GMH
- Measurement was carried out using 612 pieces in series, and the weight average molecular weight is shown.
(3)クラフトされたゴム粒子の粒径
コールタ−カウンター((m日科機社製TA−I[)を
用い、301のアパーチャーにて測定を行い、体積平均
粒径で示した。(3) Particle diameter of crafted rubber particles Measured using a Coulter counter (TA-I [manufactured by Nikkaki Co., Ltd.] with an aperture of 301, and expressed as a volume average particle diameter.
(4)膨潤度、ゲル含有量
樹脂約2gを精秤(W、とする)し、トルエン50mA
+に溶解する。不溶分を遠心分離機を用いて分離し、上
澄み液を捨て湿った状態で秤量(W2とする)する。そ
の後、真空乾燥機にて恒量となるまで乾燥し秤量(W3
とする)し、次式によって算出する。(4) Swelling degree, gel content Accurately weigh approximately 2 g of resin (referred to as W), and add 50 mA of toluene.
Dissolves in +. Insoluble matter is separated using a centrifuge, the supernatant liquid is discarded, and the sample is weighed in a wet state (referred to as W2). Then, dry it in a vacuum dryer until it reaches a constant weight and weigh it (W3
) and is calculated using the following formula.
膨潤度 = W z / W a
ゲル含有量(%) = (W、 /W、 ) X100
(5)アイゾツト(Izod)衝撃強度ASTM D−
256に基づいて測定を行った。Swelling degree = W z / W a Gel content (%) = (W, /W, ) X100
(5) Izod impact strength ASTM D-
Measurements were made based on 256.
(テストピース: 12.7X 6.4X64mm)
(6)メルトフローインデックス(MFI)ASTM
D−1238に基づいて測定を行った。(Test piece: 12.7X 6.4X64mm)
(6) Melt flow index (MFI) ASTM
Measurements were made based on D-1238.
(温度=200℃、荷重:5kg)
[実施例]
以下、実施例を示し本発明をさらに具体的に説明するが
、本発明はこれらの例によって制限されるものではない
。(Temperature = 200° C., Load: 5 kg) [Examples] The present invention will be described in more detail below with reference to Examples, but the present invention is not limited to these Examples.
実施例1
容量50I!のオートクレーブ中に、高シスポリブタジ
ェン(商品名:ウベボールBR15H,宇部興産社製、
シス1,4結合97.5%) 3.2kgを溶解した
スチレン溶液40kg及びターシャリ−ドデシルメルカ
プタン28gを加え、250rpmで撹拌した。オート
クレーブ内を窒素ガスで置換してから密閉し、昇温した
。110℃で5時間重合した後、冷却し、予備重合を終
えた。Example 1 Capacity 50I! In the autoclave, high-cis polybutadiene (product name: Ubeball BR15H, manufactured by Ube Industries, Ltd.,
40 kg of a styrene solution in which 3.2 kg of cis-1,4 bond (97.5%) was dissolved and 28 g of tertiary dodecyl mercaptan were added, and the mixture was stirred at 250 rpm. After purging the inside of the autoclave with nitrogen gas, the autoclave was sealed and the temperature was raised. After polymerizing at 110° C. for 5 hours, the mixture was cooled to complete the preliminary polymerization.
次いで、容量100I!のオートクレーブ中に、純水5
0kg、 ドデシルベンゼンスルホン酸ナトリウム0
.50g 、第3リン酸カルシウム500gを系内に加
え、180rpmに撹拌しながら、ターシャリ−ブチル
パーオキシベンゾエート32gを加えた前記の予備重合
液を入れ、窒素置換後、密閉、昇温し、 115℃で5
時間、135℃で3時間重合し、冷却した。Next, the capacity is 100I! During the autoclave, pure water
0kg, sodium dodecylbenzenesulfonate 0
.. 50 g of tertiary-butylperoxybenzoate were added to the system, and while stirring at 180 rpm, the prepolymerization solution containing 32 g of tertiary-butyl peroxybenzoate was added to the system. After purging with nitrogen, the system was sealed, heated, and heated to 115°C for 50 minutes.
Polymerization was carried out at 135° C. for 3 hours and then cooled.
常法に従い、中和、脱水、乾燥した後、重合物を押出機
により押出し通常のベレット形状として耐衝撃性スチレ
ン系樹脂を得た。第1表に物性を示す。After neutralization, dehydration, and drying according to conventional methods, the polymer was extruded using an extruder to obtain an impact-resistant styrenic resin in the form of a normal pellet. Table 1 shows the physical properties.
実施例2
予備重合液に4−メチル−2,4−ジフェニルペンテン
−1を60g加えた以外は実施例1と同様に行った。第
1表に物性を示す。Example 2 The same procedure as in Example 1 was carried out except that 60 g of 4-methyl-2,4-diphenylpentene-1 was added to the prepolymerization liquid. Table 1 shows the physical properties.
実施例3
予備重合の撹拌数を25Orpmから20Orpmに変
えた以外は実施例1と同様に行った。第1表に物性を示
す。Example 3 The same procedure as in Example 1 was carried out except that the stirring speed during prepolymerization was changed from 25 Orpm to 20 Orpm. Table 1 shows the physical properties.
実施例4
予備重合液に加えるターシャリ−ブチルパーオキシベン
ゾエートを32gから62gに変えた以外は実施例1と
同様に行った。第1表に物性を示す。Example 4 The same procedure as in Example 1 was carried out except that the amount of tert-butyl peroxybenzoate added to the prepolymerization solution was changed from 32 g to 62 g. Table 1 shows the physical properties.
比較例1
高シスポリブタジェンの代わりに低シスポリブタジェン
(商品名ニジエン55AS、無化成社製、シス1,4結
合35%)を用いた以外は実施例1と同様に行った。第
2表に物性を示す。Comparative Example 1 The same procedure as in Example 1 was carried out except that low cis polybutadiene (trade name Nidiene 55AS, manufactured by Mukasei Co., Ltd., 35% cis 1,4 bonds) was used instead of high cis polybutadiene. Table 2 shows the physical properties.
比較例2
予備重合液にジビニルベンゼンを4g加えた以外は実施
例1と同様に行った。第2表に物性を示す。Comparative Example 2 The same procedure as in Example 1 was carried out except that 4 g of divinylbenzene was added to the prepolymerization liquid. Table 2 shows the physical properties.
比較例3
予備重合液に4−メチル−2,4−ジフェニルペンテン
−1を120g加えた以外は実施例1と同様に行った。Comparative Example 3 The same procedure as in Example 1 was carried out except that 120 g of 4-methyl-2,4-diphenylpentene-1 was added to the prepolymerization liquid.
第2表に物性を示す。Table 2 shows the physical properties.
比較例4
予備重合の撹拌数を25Orpmから30Orpmに変
えた以外は実施例1と同様に行った。第2表に物性を示
す。Comparative Example 4 The same procedure as in Example 1 was carried out except that the stirring number during prepolymerization was changed from 25 Orpm to 30 Orpm. Table 2 shows the physical properties.
比較例5
予備重合の撹拌数を25Orpmから15Orpmに変
えた以外は実施例1と同様に行った。第2表に物性を示
す。Comparative Example 5 The same procedure as in Example 1 was carried out except that the stirring speed during prepolymerization was changed from 25 Orpm to 15 Orpm. Table 2 shows the physical properties.
比較例6
予備重合液に加えるターシャリ−ブチルパーオキシベン
ゾエートを32gから20gに変えた以外は実施例1と
同様に行った。第2表に物性を示す。Comparative Example 6 The same procedure as in Example 1 was carried out except that the amount of tert-butyl peroxybenzoate added to the prepolymerization solution was changed from 32 g to 20 g. Table 2 shows the physical properties.
比較例7
予備重合液に加えるターシャリ−ブチルパーオキシベン
ゾエートを32gから96gに変えた以外は実施例1と
同様に行った。第2表に物性を示す。Comparative Example 7 The same procedure as in Example 1 was carried out except that the amount of tertiary-butyl peroxybenzoate added to the prepolymerization solution was changed from 32 g to 96 g. Table 2 shows the physical properties.
第1表 (注)下記に測定方法を示す。Table 1 (Note) The measurement method is shown below.
■アイゾツト(Izod)衝撃強度
■メルトフローインデックス(MFI)■HDT (
荷重たわみ温度)
■光 沢
: ASTM D−256
: ASTM D−1238
: ASTM D−648
:JIS Z−8741
[発明の効果]
以上説明した様に、本発明の耐衝撃性スチレン系樹脂は
、実用的な耐衝撃強度、成形加工性、表面光沢の品質バ
ランスに優れており、弱電機器、事務用機器、雑貨等の
産業分野できわめて有用である。■Izod impact strength ■Melt flow index (MFI) ■HDT (
(deflection temperature under load) ■Gloss: ASTM D-256: ASTM D-1238: ASTM D-648: JIS Z-8741 [Effects of the Invention] As explained above, the impact-resistant styrenic resin of the present invention is suitable for practical use. It has an excellent quality balance of impact resistance, moldability, and surface gloss, making it extremely useful in industrial fields such as light electrical equipment, office equipment, and miscellaneous goods.
出願人 電気化学工業株式会社Applicant: Denki Kagaku Kogyo Co., Ltd.
Claims (1)
子を分散して含有し、かつゴムがシス1,4結合が90
モル%以上のポリブタジエンでその含有量が5〜15重
量%である耐衝撃性スチレン系樹脂において、 (A)連続するスチレン系重合体の重量平均分子量が1
5〜25万 (B)グラフトされたゴム粒子の体積平均粒径が1.3
〜2.3μm (C)樹脂のトルエン中の膨潤度が9以上 (D)樹脂のゲル含有量(GEL)とゴム含有量(PB
D)の比(GEL/PBD)が2〜3 の範囲にあることを特徴とする耐衝撃性スチレン系樹脂
。[Claims] Contains grafted rubber particles dispersed in a continuous styrenic polymer, and the rubber has 90 cis-1,4 bonds.
In impact-resistant styrenic resins whose content is 5 to 15% by weight of polybutadiene of mol% or more, (A) the weight average molecular weight of the continuous styrenic polymer is 1
50,000 to 250,000 (B) The volume average particle size of the grafted rubber particles is 1.3
~2.3 μm (C) Resin swelling degree in toluene is 9 or more (D) Resin gel content (GEL) and rubber content (PB
An impact-resistant styrenic resin characterized in that the ratio (GEL/PBD) of D) is in the range of 2 to 3.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP14010390A JPH0436305A (en) | 1990-05-31 | 1990-05-31 | Impact-resistant styrenic resin |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP14010390A JPH0436305A (en) | 1990-05-31 | 1990-05-31 | Impact-resistant styrenic resin |
Publications (1)
Publication Number | Publication Date |
---|---|
JPH0436305A true JPH0436305A (en) | 1992-02-06 |
Family
ID=15261014
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP14010390A Pending JPH0436305A (en) | 1990-05-31 | 1990-05-31 | Impact-resistant styrenic resin |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH0436305A (en) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2002080542A (en) * | 2000-09-06 | 2002-03-19 | Toyo Styrene Co Ltd | Rubber-modified styrenic resin composition |
JP2017002237A (en) * | 2015-06-12 | 2017-01-05 | 東洋スチレン株式会社 | Rubber modified styrene resin composition and molded body using the same |
-
1990
- 1990-05-31 JP JP14010390A patent/JPH0436305A/en active Pending
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2002080542A (en) * | 2000-09-06 | 2002-03-19 | Toyo Styrene Co Ltd | Rubber-modified styrenic resin composition |
JP2017002237A (en) * | 2015-06-12 | 2017-01-05 | 東洋スチレン株式会社 | Rubber modified styrene resin composition and molded body using the same |
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