JPH01163235A - Polyethylene resin composition - Google Patents
Polyethylene resin compositionInfo
- Publication number
- JPH01163235A JPH01163235A JP62321082A JP32108287A JPH01163235A JP H01163235 A JPH01163235 A JP H01163235A JP 62321082 A JP62321082 A JP 62321082A JP 32108287 A JP32108287 A JP 32108287A JP H01163235 A JPH01163235 A JP H01163235A
- Authority
- JP
- Japan
- Prior art keywords
- density
- resin composition
- polyethylene resin
- lldpe
- composition
- 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
- 239000011342 resin composition Substances 0.000 title claims abstract description 16
- 229920013716 polyethylene resin Polymers 0.000 title claims description 16
- 229920000092 linear low density polyethylene Polymers 0.000 claims abstract description 20
- 239000004707 linear low-density polyethylene Substances 0.000 claims abstract description 20
- 229920001903 high density polyethylene Polymers 0.000 claims description 13
- 239000004700 high-density polyethylene Substances 0.000 claims description 13
- 238000001746 injection moulding Methods 0.000 claims description 3
- 239000000203 mixture Substances 0.000 abstract description 14
- 239000004698 Polyethylene Substances 0.000 abstract description 8
- 238000002347 injection Methods 0.000 abstract description 5
- 239000007924 injection Substances 0.000 abstract description 5
- VGGSQFUCUMXWEO-UHFFFAOYSA-N Ethene Chemical compound C=C VGGSQFUCUMXWEO-UHFFFAOYSA-N 0.000 description 12
- 238000002156 mixing Methods 0.000 description 12
- 239000008188 pellet Substances 0.000 description 10
- 239000011347 resin Substances 0.000 description 8
- 229920005989 resin Polymers 0.000 description 8
- 229920001684 low density polyethylene Polymers 0.000 description 7
- 239000004702 low-density polyethylene Substances 0.000 description 7
- 239000005977 Ethylene Substances 0.000 description 6
- VXNZUUAINFGPBY-UHFFFAOYSA-N 1-Butene Chemical compound CCC=C VXNZUUAINFGPBY-UHFFFAOYSA-N 0.000 description 5
- 238000000034 method Methods 0.000 description 5
- 238000003756 stirring Methods 0.000 description 5
- 230000000052 comparative effect Effects 0.000 description 4
- 239000003054 catalyst Substances 0.000 description 3
- 229920001577 copolymer Polymers 0.000 description 3
- 238000005259 measurement Methods 0.000 description 3
- 238000012360 testing method Methods 0.000 description 3
- 150000003623 transition metal compounds Chemical class 0.000 description 3
- 239000004711 α-olefin Substances 0.000 description 3
- 239000004322 Butylated hydroxytoluene Substances 0.000 description 2
- NLZUEZXRPGMBCV-UHFFFAOYSA-N Butylhydroxytoluene Chemical compound CC1=CC(C(C)(C)C)=C(O)C(C(C)(C)C)=C1 NLZUEZXRPGMBCV-UHFFFAOYSA-N 0.000 description 2
- TWRXJAOTZQYOKJ-UHFFFAOYSA-L Magnesium chloride Chemical compound [Mg+2].[Cl-].[Cl-] TWRXJAOTZQYOKJ-UHFFFAOYSA-L 0.000 description 2
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 description 2
- 229940095259 butylated hydroxytoluene Drugs 0.000 description 2
- 235000010354 butylated hydroxytoluene Nutrition 0.000 description 2
- DIOQZVSQGTUSAI-UHFFFAOYSA-N decane Chemical compound CCCCCCCCCC DIOQZVSQGTUSAI-UHFFFAOYSA-N 0.000 description 2
- 230000007423 decrease Effects 0.000 description 2
- 238000004898 kneading Methods 0.000 description 2
- 150000002681 magnesium compounds Chemical class 0.000 description 2
- 238000004519 manufacturing process Methods 0.000 description 2
- 150000002902 organometallic compounds Chemical class 0.000 description 2
- QQONPFPTGQHPMA-UHFFFAOYSA-N propylene Natural products CC=C QQONPFPTGQHPMA-UHFFFAOYSA-N 0.000 description 2
- 125000004805 propylene group Chemical group [H]C([H])([H])C([H])([*:1])C([H])([H])[*:2] 0.000 description 2
- 239000003381 stabilizer Substances 0.000 description 2
- -1 titanium chloride Chemical class 0.000 description 2
- LIKMAJRDDDTEIG-UHFFFAOYSA-N 1-hexene Chemical compound CCCCC=C LIKMAJRDDDTEIG-UHFFFAOYSA-N 0.000 description 1
- VBICKXHEKHSIBG-UHFFFAOYSA-N 1-monostearoylglycerol Chemical compound CCCCCCCCCCCCCCCCCC(=O)OCC(O)CO VBICKXHEKHSIBG-UHFFFAOYSA-N 0.000 description 1
- KWKAKUADMBZCLK-UHFFFAOYSA-N 1-octene Chemical compound CCCCCCC=C KWKAKUADMBZCLK-UHFFFAOYSA-N 0.000 description 1
- ADDIATRPAYCWOW-UHFFFAOYSA-N 2-butyl-6-(5-chlorobenzotriazol-2-yl)-4-methylphenol Chemical compound CCCCC1=CC(C)=CC(N2N=C3C=C(Cl)C=CC3=N2)=C1O ADDIATRPAYCWOW-UHFFFAOYSA-N 0.000 description 1
- CMAOLVNGLTWICC-UHFFFAOYSA-N 2-fluoro-5-methylbenzonitrile Chemical compound CC1=CC=C(F)C(C#N)=C1 CMAOLVNGLTWICC-UHFFFAOYSA-N 0.000 description 1
- WSSSPWUEQFSQQG-UHFFFAOYSA-N 4-methyl-1-pentene Chemical compound CC(C)CC=C WSSSPWUEQFSQQG-UHFFFAOYSA-N 0.000 description 1
- VYZAMTAEIAYCRO-UHFFFAOYSA-N Chromium Chemical compound [Cr] VYZAMTAEIAYCRO-UHFFFAOYSA-N 0.000 description 1
- FYYHWMGAXLPEAU-UHFFFAOYSA-N Magnesium Chemical compound [Mg] FYYHWMGAXLPEAU-UHFFFAOYSA-N 0.000 description 1
- RTAQQCXQSZGOHL-UHFFFAOYSA-N Titanium Chemical compound [Ti] RTAQQCXQSZGOHL-UHFFFAOYSA-N 0.000 description 1
- 239000006096 absorbing agent Substances 0.000 description 1
- 239000000654 additive Substances 0.000 description 1
- 150000001336 alkenes Chemical class 0.000 description 1
- 150000003973 alkyl amines Chemical class 0.000 description 1
- PNEYBMLMFCGWSK-UHFFFAOYSA-N aluminium oxide Inorganic materials [O-2].[O-2].[O-2].[Al+3].[Al+3] PNEYBMLMFCGWSK-UHFFFAOYSA-N 0.000 description 1
- 239000003963 antioxidant agent Substances 0.000 description 1
- 230000003078 antioxidant effect Effects 0.000 description 1
- 239000002216 antistatic agent Substances 0.000 description 1
- IAQRGUVFOMOMEM-UHFFFAOYSA-N butene Natural products CC=CC IAQRGUVFOMOMEM-UHFFFAOYSA-N 0.000 description 1
- CJZGTCYPCWQAJB-UHFFFAOYSA-L calcium stearate Chemical compound [Ca+2].CCCCCCCCCCCCCCCCCC([O-])=O.CCCCCCCCCCCCCCCCCC([O-])=O CJZGTCYPCWQAJB-UHFFFAOYSA-L 0.000 description 1
- 239000008116 calcium stearate Substances 0.000 description 1
- 235000013539 calcium stearate Nutrition 0.000 description 1
- 239000006229 carbon black Substances 0.000 description 1
- 229910052804 chromium Inorganic materials 0.000 description 1
- 239000011651 chromium Substances 0.000 description 1
- 150000001875 compounds Chemical class 0.000 description 1
- JGHYBJVUQGTEEB-UHFFFAOYSA-M dimethylalumanylium;chloride Chemical compound C[Al](C)Cl JGHYBJVUQGTEEB-UHFFFAOYSA-M 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000011156 evaluation Methods 0.000 description 1
- 238000001125 extrusion Methods 0.000 description 1
- 229920001519 homopolymer Polymers 0.000 description 1
- 239000000314 lubricant Substances 0.000 description 1
- 229910052749 magnesium Inorganic materials 0.000 description 1
- 239000011777 magnesium Substances 0.000 description 1
- 229910001629 magnesium chloride Inorganic materials 0.000 description 1
- 238000000691 measurement method Methods 0.000 description 1
- 238000002844 melting Methods 0.000 description 1
- 230000008018 melting Effects 0.000 description 1
- 239000000178 monomer Substances 0.000 description 1
- JRZJOMJEPLMPRA-UHFFFAOYSA-N olefin Natural products CCCCCCCC=C JRZJOMJEPLMPRA-UHFFFAOYSA-N 0.000 description 1
- 238000005453 pelletization Methods 0.000 description 1
- 239000000049 pigment Substances 0.000 description 1
- 229920000573 polyethylene Polymers 0.000 description 1
- 238000011160 research Methods 0.000 description 1
- 229940116351 sebacate Drugs 0.000 description 1
- CXMXRPHRNRROMY-UHFFFAOYSA-L sebacate(2-) Chemical compound [O-]C(=O)CCCCCCCCC([O-])=O CXMXRPHRNRROMY-UHFFFAOYSA-L 0.000 description 1
- 239000000377 silicon dioxide Substances 0.000 description 1
- 239000011949 solid catalyst Substances 0.000 description 1
- 238000009864 tensile test Methods 0.000 description 1
- 229910052719 titanium Inorganic materials 0.000 description 1
- 239000010936 titanium Substances 0.000 description 1
- 150000003609 titanium compounds Chemical class 0.000 description 1
- XJDNKRIXUMDJCW-UHFFFAOYSA-J titanium tetrachloride Chemical compound Cl[Ti](Cl)(Cl)Cl XJDNKRIXUMDJCW-UHFFFAOYSA-J 0.000 description 1
- VOITXYVAKOUIBA-UHFFFAOYSA-N triethylaluminium Chemical compound CC[Al](CC)CC VOITXYVAKOUIBA-UHFFFAOYSA-N 0.000 description 1
- MCULRUJILOGHCJ-UHFFFAOYSA-N triisobutylaluminium Chemical compound CC(C)C[Al](CC(C)C)CC(C)C MCULRUJILOGHCJ-UHFFFAOYSA-N 0.000 description 1
- CNWZYDSEVLFSMS-UHFFFAOYSA-N tripropylalumane Chemical compound CCC[Al](CCC)CCC CNWZYDSEVLFSMS-UHFFFAOYSA-N 0.000 description 1
- GPPXJZIENCGNKB-UHFFFAOYSA-N vanadium Chemical compound [V]#[V] GPPXJZIENCGNKB-UHFFFAOYSA-N 0.000 description 1
- 229910052720 vanadium Inorganic materials 0.000 description 1
Landscapes
- Compositions Of Macromolecular Compounds (AREA)
Abstract
Description
【発明の詳細な説明】
(産業上の利用分野)
本発明は、引裂性を改良したポリエチレン樹脂組成物に
関する。特に大型の薄肉射出成形品の製造に適するポリ
エチレン樹脂組成物に関する。DETAILED DESCRIPTION OF THE INVENTION (Field of Industrial Application) The present invention relates to a polyethylene resin composition with improved tearability. In particular, the present invention relates to a polyethylene resin composition suitable for manufacturing large, thin-walled injection molded products.
(従来の技術)
従来、大型の薄肉射出成形品を得るためのポリエチレン
樹脂としては、
■ 高密度ポリエチレン樹脂(以下、HDPEという。(Prior Art) Conventionally, the polyethylene resins used to obtain large, thin-walled injection molded products include: (1) High-density polyethylene resin (hereinafter referred to as HDPE).
)Kメルトインデックス(以下、MIという。)の大き
い低密度ポリエチレン(以下、LDPEという。)を添
加したポリエチレン樹脂組成物。) A polyethylene resin composition to which low-density polyethylene (hereinafter referred to as LDPE) with a large K melt index (hereinafter referred to as MI) is added.
■ MIの大きいLDPE樹脂。■ LDPE resin with large MI.
■ MIの大きい直鎖状低密度ポリエチレン樹脂(以下
、LLDPEという。)。■Linear low-density polyethylene resin with large MI (hereinafter referred to as LLDPE).
などが知られている。etc. are known.
(発明が解決しようとする問題点)
上記■の組成物は、該組成物を用いて成形したときの該
成形品が引裂性に劣るという欠点を有し、■の樹脂では
、該樹脂を用いて得られる成形品の剛性が小さく、引裂
性に劣るという欠点を有していり。また、上記■の樹脂
では、該樹脂を用いて得られる成形品の剛性が小さいと
いう欠点を有している。(Problems to be Solved by the Invention) The composition (2) above has the disadvantage that the molded product when molded using the composition has poor tearability. The disadvantage is that the resulting molded product has low rigidity and poor tearability. Furthermore, the above-mentioned resin (3) has the disadvantage that the rigidity of molded products obtained using the resin is low.
本発明者等は、LDPE樹脂やLLDPEよシ剛性が高
く、かつ引裂性に優れた成形品が得られるポリエチレン
樹脂組成物を得るために、鋭意研究した。その結果、特
定のMIおよび密度を有するLLDPEに特定のMIお
よび密度を有するHDPEを添加してなるポリエチレン
樹脂組成物が、該組成物を用いて成形品としたときの該
成形品の剛性および引裂性を改善できることを見い出し
、本発明を完成した。The present inventors have conducted extensive research in order to obtain a polyethylene resin composition that has higher rigidity than LDPE resin or LLDPE and can yield molded articles with excellent tearability. As a result, a polyethylene resin composition formed by adding HDPE having a specific MI and density to LLDPE having a specific MI and density has a high rigidity and tear resistance when the molded product is made from the composition. The present invention was completed based on the discovery that the properties can be improved.
以上の記述から明らかなように、本発明の目的は、剛性
および引裂性が改善された大型の薄肉射出成形品が得ら
れるポリエチレン樹脂組成物を提供することである。As is clear from the above description, an object of the present invention is to provide a polyethylene resin composition from which large, thin-walled injection molded articles with improved rigidity and tearability can be obtained.
(問題点を解決するための手段) 本発明は以下の構成を有する。(Means for solving problems) The present invention has the following configuration.
(1) メルトインデックス(以下、MIという。)
が5〜50y/10分で、かつ密度が0.915〜0.
93511crdの直鎖状低密度ポリエチレン(以下、
LLDPEという。)に、MIが5〜30g/10分で
、かつ密度が0.945〜0.968.F/dの高密度
ポリエチレン(以下、HDPEという。)をポリエチレ
ン樹脂組成物に対して、10〜50重量係添加してなる
引裂性を改良した射出成形用ポリエチレン樹脂組成物。(1) Melt index (hereinafter referred to as MI)
is 5 to 50y/10 minutes, and the density is 0.915 to 0.
93511crd linear low density polyethylene (hereinafter referred to as
It is called LLDPE. ), MI is 5 to 30 g/10 min, and density is 0.945 to 0.968. A polyethylene resin composition for injection molding with improved tearability, which is obtained by adding F/d high-density polyethylene (hereinafter referred to as HDPE) in an amount of 10 to 50% by weight to a polyethylene resin composition.
本発明において使用されるLLDPEは、エチレンと他
のα−オレフィンとの共重合体であシ、従来の高圧法に
よシ製造されたLDPEとは異なる。The LLDPE used in the present invention is a copolymer of ethylene and other α-olefins and is different from LDPE produced by conventional high pressure methods.
該LLDPEは、エチレンと他のα−オレフィンである
ブテン、ヘキセン、オクテン、デカン、4−メチルペン
テン−1の4〜g/重量係、好ましくは5〜15重量係
とを共重合させたものであり、従来よシ中低圧法HDP
E製造に用いられるチーグラー型触媒またはフィリップ
ス型触媒を用いて製造されたものである。従来のHDP
Eよシ短い枝分かれ構造を有し、密度もこの短鎖枝分か
れを利用して適当に低下させ、0.910〜0.950
p/crA程度としたものであって、従来のLDPE
よシ直鎖性があシ、また、HDPHよシ枝分かれが多い
構造をもつポリエチレン樹脂である。The LLDPE is a copolymer of ethylene and other α-olefins such as butene, hexene, octene, decane, and 4-methylpentene-1 in an amount of 4 to 15 g/wt, preferably 5 to 15 g/wt. Yes, conventional medium and low pressure HDP
It is produced using a Ziegler type catalyst or a Phillips type catalyst used in E production. Conventional HDP
It has a short branched structure like E, and the density can be appropriately lowered using this short chain branching to 0.910 to 0.950.
p/crA level, compared to conventional LDPE.
It is a polyethylene resin with a more linear structure and a more branched structure than HDPH.
本発明で使用されるLLDPEは、MI (JIS K
6760に準拠して測定した値)が5〜s o y71
゜分で、かつ密度が0.915〜0.935g/d、好
ましくは0.920〜0.930F/iのものである。The LLDPE used in the present invention is MI (JIS K
6760) is 5 to s o y71
°min and a density of 0.915 to 0.935 g/d, preferably 0.920 to 0.930 F/i.
該LLDPEのMIが5.9/10分よシ少さいと、溶
融樹脂の流動性が悪化し、該LLDPEのMIが50
F/10分を超えると得られた成形品の引裂性が低下す
るので好ましくない。If the MI of the LLDPE is as low as 5.9/10 minutes, the fluidity of the molten resin will deteriorate, and the MI of the LLDPE will be 50/10.
If it exceeds F/10 minutes, the tearability of the obtained molded article will decrease, which is not preferable.
また、該LLDPEの密度が0.915.P/dよシ小
さいと得られた成形品の剛性を低下させ、該LLDPE
の密度が0.93597cdを超えると引裂性を低下さ
せるので好ましくない。Further, the density of the LLDPE is 0.915. If P/d is smaller, the rigidity of the obtained molded product will be reduced, and the LLDPE
If the density exceeds 0.93597 cd, it is not preferable because it reduces tearability.
本発明で使用されるHDPEは、エチレンの単独重合体
またはエチレンとプロピレン、ブテン−1といったオレ
フィン単量体との共重合体である。The HDPE used in the present invention is a homopolymer of ethylene or a copolymer of ethylene and an olefin monomer such as propylene or butene-1.
該HDPEは、遷移金属化合物と有機金属化合物とから
なる触媒を用いて、エチレンの単独重合またはエチレン
とα−オレフィン、たとえばプロピレン、ブテン−1な
どを共重合させて得られるものである。遷移金属化合物
としては、チタン、バナジウム、クロムなどの遷移金属
化合物を1穏または2種以上、または、これらをシリカ
、アルミナ、マグネシウム化合物などに担持ま九は反応
させたものが挙げられる。特にチタンの塩化物、ハロア
ルコラード、アルコラードなどのチタン化合物をマグネ
シウムアルコラード、塩化マグネシウムなどのマグネシ
ウム化合物に担持または反応させた固体触媒成分が好適
に用いられる。The HDPE is obtained by homopolymerizing ethylene or copolymerizing ethylene with an α-olefin such as propylene, butene-1, etc. using a catalyst comprising a transition metal compound and an organometallic compound. Examples of the transition metal compound include one or more transition metal compounds such as titanium, vanadium, and chromium, or those supported on silica, alumina, magnesium compounds, etc., or reacted with them. In particular, a solid catalyst component in which a titanium compound such as titanium chloride, haloalcolade, or alcolade is supported on or reacted with a magnesium compound such as magnesium alcolade or magnesium chloride is preferably used.
有機金属化合物としては、一般式AlRnX3−n(式
中、Alはアルミニウム原子、Rは炭素数1〜14の炭
化水素基、Xはハロゲン原子、nは1〜3の数字を表わ
す。)で表わされる有機アルミニウム化合物が挙げられ
る。具体的には、トリエチルアルミニウム、トリn−プ
ロピルアルミニウム、トリイソブチルアルミニウム、ジ
メチルアルミニウムモノクロライド、エチルアルミニウ
ムセスキクロライドなどが挙げられる。The organometallic compound is represented by the general formula AlRn Examples include organoaluminum compounds. Specifically, triethylaluminum, tri-n-propylaluminum, triisobutylaluminum, dimethylaluminum monochloride, ethylaluminum sesquichloride and the like can be mentioned.
本発明で使用されるHDPEの配合割合は、全組成物に
対して10〜50重量係、好ましくは15〜30重量係
である。該配合割合が10重重量上シ少ないと、得られ
た組成物を用いて成形品としたときの該成形品の剛性が
小さく、また該配合割合が50重量係を超えると得られ
た組成物を用いて成形品とした該成形品の引裂性が低下
するので好ましくない。また、該HDPEのMI(JI
SK 6760に準拠して測定した値)は5〜3(1/
10分、好ましくは10〜259710分である。該H
DPEのMIが5II/10分未満では、溶融時の樹脂
の流動性が悪化し、また、30.9/10分を超えると
得られた組成物を用いて成形したときの該成形品の引裂
性が低下するので好ましくない。The blending ratio of HDPE used in the present invention is 10 to 50 weight percent, preferably 15 to 30 weight percent, based on the total composition. If the blending ratio is less than 10% by weight, the rigidity of the molded product will be low when the resulting composition is made into a molded product, and if the blending ratio exceeds 50% by weight, the resulting composition will have a low rigidity. This is not preferable because the tearability of the molded product obtained by using the method decreases. In addition, MI (JI) of the HDPE
Value measured according to SK 6760) is 5 to 3 (1/
10 minutes, preferably 10-259710 minutes. The H
If the MI of the DPE is less than 5II/10 minutes, the fluidity of the resin during melting will deteriorate, and if it exceeds 30.9/10 minutes, the molded product will tear when molded using the resulting composition. This is not preferable because it reduces performance.
本発明のポリエチレン樹脂組成物は、前記したLLDP
EとHDPEの所定量を撹拌装置たとえばヘンセルミキ
サー(商品名)、リボンブレンダー、スーパーミキサー
などで撹拌混合したあと、通常の溶融混線法、たとえば
バンバリーミキサ−、コンテニュアスミキサー、ミキシ
ングロール、押出機によって、溶融混線温度130〜2
50℃で溶融混練し、ペレット化することによって得ら
れる。The polyethylene resin composition of the present invention has the above-mentioned LLDP.
After stirring and mixing a predetermined amount of E and HDPE using a stirring device such as a Hensel mixer (trade name), a ribbon blender, or a super mixer, the mixture is mixed using a conventional melt mixing method such as a Banbury mixer, continuous mixer, mixing roll, or extrusion. Depending on the machine, melt crosstalk temperature 130~2
It is obtained by melt-kneading at 50°C and pelletizing.
また、本発明のポリエチレン樹脂組成物には、必要に応
じて酸化防止剤たとえばブチル化ヒドロキシトルエン(
BHT)、シミリスチル−3,3′−チオジプロピオン
酸エステルなど、滑剤たとえばカルシウムステアレート
、紫外線吸収剤たとえば2− (2’−ヒドロキシ−3
′−1−ブチル−5′−メチルフェニル)−5−クロロ
ベンゾトリアゾール、ビス(2,2’ 6,6’−テト
ラメチル−4−ピペリジンセバケート)など、帯電防止
剤たとえばグリセリンモノステアレー)、N、N−ビス
(2−ヒドロキシエチル)アルキルアミン)など、顔料
たとえばカーボンブラックなど通常ポリエチレンに使用
される公知の各種添加剤を加えることができる。In addition, the polyethylene resin composition of the present invention may optionally contain an antioxidant such as butylated hydroxytoluene (
lubricants such as calcium stearate, UV absorbers such as 2-(2'-hydroxy-3
'-1-butyl-5'-methylphenyl)-5-chlorobenzotriazole, bis(2,2'6,6'-tetramethyl-4-piperidine sebacate), antistatic agents such as glycerin monostearate) , N,N-bis(2-hydroxyethyl)alkylamine), pigments such as carbon black, and various known additives commonly used in polyethylene can be added.
(実施例)
以下、実施例によって本発明をさらに詳細に説明するが
、本発明はその要旨を超えない限り実施例に限定される
ものではない。(Examples) Hereinafter, the present invention will be explained in more detail with reference to Examples, but the present invention is not limited to the Examples unless the gist thereof is exceeded.
なお、実施例中、剛性の評価法としての曲げ弾性率の測
定、アイゾツト衝撃強度の測定、引裂性および引裂強度
の測定は次の方法によシ行った。In the Examples, measurements of flexural modulus, Izot impact strength, tearability, and tear strength as methods for evaluating rigidity were carried out by the following methods.
(1)曲げ弾性率 ・・・ JIS K 6760に準
する。(1) Flexural modulus: Conforms to JIS K 6760.
(li)アイゾツト衝撃強度 ・・・ JIS K 6
760に準する。(li) Izot impact strength... JIS K 6
760.
(fil)引裂性および引裂強度 ・・・ 縦400f
l、横80*xs厚さ2u
の平板を射出成形機で成形し、試験片とした。試験は、
試験片の短片の中央から、長辺に平行に内部へ100B
切込みを入れ、該切込み部分のそれぞれを引張試験機の
上下チャックに取υ付け、引張最大荷重を測定し引裂強
度とした。引裂性の評価として、直線状に引裂かれるも
のを○、ノコギリ状に引裂かれるものを×とした。測定
条件は次の通りである。(fil) Tearability and tear strength... Vertical 400f
A flat plate with a width of 80*xs and a thickness of 2u was molded using an injection molding machine and used as a test piece. The exam is
100B from the center of the short piece of the test piece to the inside parallel to the long side
A cut was made, each of the cut portions was attached to the upper and lower chucks of a tensile testing machine, and the maximum tensile load was measured to determine the tear strength. As for evaluation of tearability, those that were torn in a straight line were rated as ○, and those that were torn in a sawtooth pattern were rated as x. The measurement conditions are as follows.
測定温度 23重2°C温度 50±5係R,H引張速
度 500貫シー チャック間距離 100詣実施例
1〜5
LLDPE (安定剤、ブチル化ヒドロキシトルエン0
.1li%、シミリスチル−3,3′−チオジプロピオ
ン酸エステル0.05重−f1%、カルシウムステアレ
ート0.1重量%をそれぞれ含有)にHDPE(LLD
PEと同量、同様の安定剤を含有)を後述の第1表に記
載した配合割合でヘンセルミキサー(商品名)に入れ、
3分間撹拌混合したあと、該混合物をシリンダー温度1
90℃の単軸押出機で溶融混練して押出しペレットとし
た。得られたペレットを用いて所定の試験片を作製し、
上記の測定方法によシ曲げ弾性率、アイゾツト衝撃強度
、引裂強度、引裂性の測定および評価を行った。その結
果を第1表に示した。Measurement temperature: 23 times 2°C Temperature: 50 ± 5 R, H Tensile speed: 500 seams Distance between chucks: 100 times Examples 1 to 5 LLDPE (stabilizer, butylated hydroxytoluene 0
.. HDPE (LLD
The same amount of PE (containing the same stabilizer) was placed in a Hensel mixer (trade name) at the mixing ratio listed in Table 1 below.
After stirring and mixing for 3 minutes, the mixture was heated to a cylinder temperature of 1
The mixture was melt-kneaded using a single-screw extruder at 90°C to obtain extruded pellets. A predetermined test piece was prepared using the obtained pellet,
The flexural modulus, Izot impact strength, tear strength, and tearability were measured and evaluated using the above measurement methods. The results are shown in Table 1.
比較例1
実施例1〜5で用いたと同様のLLDPEをシリンダー
温度190℃の単軸押出機で溶融混練して押出し、ペレ
ットとした。得られたペレットを用いて、実施例1〜5
に準拠して曲げ弾性率、アイゾツト衝撃強度、引裂強度
、引裂性の測定お二び評価を行った。その結果を第1表
に示した。Comparative Example 1 LLDPE similar to that used in Examples 1 to 5 was melt-kneaded and extruded using a single-screw extruder with a cylinder temperature of 190°C to form pellets. Examples 1 to 5 using the obtained pellets
Flexural modulus, Izot impact strength, tear strength, and tearability were measured and evaluated in accordance with the following. The results are shown in Table 1.
比較例2
実施例1〜5で用いたと同様のLLDPEとHDPEを
後述の第1表に記載された配合割合で添加し、実施例1
〜5に準拠して撹拌混合、溶融混練、押出してペレット
とした。得られたペレットを用いて、実施例1〜5に準
拠して曲げ弾性率、アイゾツト衝撃強度、引裂強度、引
裂性の測定および評価を行った。その結果を第1表に示
した。Comparative Example 2 LLDPE and HDPE similar to those used in Examples 1 to 5 were added at the blending ratios listed in Table 1 below, and Example 1
- 5 to form pellets by stirring, mixing, melt-kneading, and extruding. Using the obtained pellets, the flexural modulus, Izot impact strength, tear strength, and tearability were measured and evaluated in accordance with Examples 1 to 5. The results are shown in Table 1.
比較例3
実施例1〜5で用いたと同様のLLDPEをシリンダー
温度190℃の単軸押出機で溶融混線、押出してペレッ
トとした。得られたペレットを用いて、実施例1〜5に
準拠して曲げ弾性率、アイゾツト衝撃強度、引裂強度、
引裂性の測定および評、価を行った。その結果を第1表
に示した。Comparative Example 3 LLDPE similar to that used in Examples 1 to 5 was melted and mixed and extruded into pellets using a single screw extruder with a cylinder temperature of 190°C. Using the obtained pellets, flexural modulus, Izot impact strength, tear strength,
Tearability was measured and evaluated. The results are shown in Table 1.
比較例4〜6
実施例1〜5で用いたと同様のLLDPEおよびHDP
Eを後述の第1表に記載された配合割合で添加し、実施
例1〜5に準拠して、撹拌混合、溶融混線、押出してペ
レットとした。得られたペレットを用いて実施例1〜5
に準拠して曲げ弾性率、アイゾツト衝撃強度、引裂強度
、引裂性の測定および評価を行った。その結果を第1表
に示した。Comparative Examples 4-6 LLDPE and HDP similar to those used in Examples 1-5
E was added in the proportions shown in Table 1 below, and pellets were prepared by stirring, mixing, melt mixing, and extruding according to Examples 1 to 5. Examples 1 to 5 using the obtained pellets
Flexural modulus, Izot impact strength, tear strength, and tearability were measured and evaluated in accordance with the following. The results are shown in Table 1.
(発明の効果)
本発明の組成物を用いることによりLDPEおよびLL
DPEをそれぞれ単独で用いて得られた成形品よシ剛性
が高く、引裂性が改良された成形品が得られる。従って
本発明のポリエチレン樹脂組成物は、大型の薄肉射出成
形品の用途に好適に用いることができる。(Effect of the invention) By using the composition of the invention, LDPE and LL
A molded article with higher rigidity and improved tearability can be obtained than a molded article obtained by using each DPE alone. Therefore, the polyethylene resin composition of the present invention can be suitably used for large-sized, thin-walled injection molded products.
Claims (1)
〜50g/10分で、かつ密度が0.915〜0.93
5g/cm^3の直鎖状低密度ポリエチレンに、MIが
5〜30g/10分で、かつ密度が0.945〜0.9
68g/cm^3の高密度ポリエチレンをポリエチレン
樹脂組成物に対して10〜50重量%添加してなる引裂
性を改良した射出成形用ポリエチレン樹脂組成物。(1) Melt index (hereinafter referred to as MI) is 5
~50g/10min and density 0.915~0.93
Linear low density polyethylene of 5 g/cm^3, MI of 5 to 30 g/10 min, and density of 0.945 to 0.9
A polyethylene resin composition for injection molding with improved tearability, which is obtained by adding 68 g/cm^3 high-density polyethylene in an amount of 10 to 50% by weight based on the polyethylene resin composition.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP62321082A JPH01163235A (en) | 1987-12-18 | 1987-12-18 | Polyethylene resin composition |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP62321082A JPH01163235A (en) | 1987-12-18 | 1987-12-18 | Polyethylene resin composition |
Publications (1)
Publication Number | Publication Date |
---|---|
JPH01163235A true JPH01163235A (en) | 1989-06-27 |
Family
ID=18128608
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP62321082A Pending JPH01163235A (en) | 1987-12-18 | 1987-12-18 | Polyethylene resin composition |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH01163235A (en) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US5262228A (en) * | 1990-06-12 | 1993-11-16 | Mitsui Petrochemical Industries, Ltd. | Ethylene/pentene-1 copolymer compositions and their use |
KR100269769B1 (en) * | 1997-09-05 | 2001-01-15 | 오재옥 | Method for manufacturing reinforced reservoir and drum of composite resin material |
Citations (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS54100445A (en) * | 1978-01-26 | 1979-08-08 | Showa Denko Kk | Polyethylene resin composition for injection molding |
JPS60233136A (en) * | 1984-05-04 | 1985-11-19 | Idemitsu Petrochem Co Ltd | Ethylenic polymer composition for storing hydrocarbon |
JPS6143640A (en) * | 1984-08-07 | 1986-03-03 | Karupu Kogyo Kk | Resin composition |
-
1987
- 1987-12-18 JP JP62321082A patent/JPH01163235A/en active Pending
Patent Citations (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS54100445A (en) * | 1978-01-26 | 1979-08-08 | Showa Denko Kk | Polyethylene resin composition for injection molding |
JPS60233136A (en) * | 1984-05-04 | 1985-11-19 | Idemitsu Petrochem Co Ltd | Ethylenic polymer composition for storing hydrocarbon |
JPS6143640A (en) * | 1984-08-07 | 1986-03-03 | Karupu Kogyo Kk | Resin composition |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US5262228A (en) * | 1990-06-12 | 1993-11-16 | Mitsui Petrochemical Industries, Ltd. | Ethylene/pentene-1 copolymer compositions and their use |
KR100269769B1 (en) * | 1997-09-05 | 2001-01-15 | 오재옥 | Method for manufacturing reinforced reservoir and drum of composite resin material |
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