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JPS58108240A - Resin composiion and its preparation - Google Patents

Resin composiion and its preparation

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Publication number
JPS58108240A
JPS58108240A JP20660081A JP20660081A JPS58108240A JP S58108240 A JPS58108240 A JP S58108240A JP 20660081 A JP20660081 A JP 20660081A JP 20660081 A JP20660081 A JP 20660081A JP S58108240 A JPS58108240 A JP S58108240A
Authority
JP
Japan
Prior art keywords
density polyethylene
polar
pigment
polyolefin
parts
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
Application number
JP20660081A
Other languages
Japanese (ja)
Other versions
JPH037497B2 (en
Inventor
Seiji Kawano
川野 清治
Masaru Nakayama
勝 中山
Mitsuo Katsumata
勝又 三男
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.)
Mitsui Petrochemical Industries Ltd
Original Assignee
Mitsui Petrochemical Industries 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 Mitsui Petrochemical Industries Ltd filed Critical Mitsui Petrochemical Industries Ltd
Priority to JP20660081A priority Critical patent/JPS58108240A/en
Publication of JPS58108240A publication Critical patent/JPS58108240A/en
Publication of JPH037497B2 publication Critical patent/JPH037497B2/ja
Granted legal-status Critical Current

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  • Processes Of Treating Macromolecular Substances (AREA)
  • Compositions Of Macromolecular Compounds (AREA)

Abstract

PURPOSE:To prepare a composition giving a colored shipping container free from die weldline, by compounding a high-density polyethylene with a pigment and a polar-group-containing polyolefin. CONSTITUTION:A high-density polyethylene is compounded with a pigment and a polyolefin having polar group. The amount of the polar group in the polyolefin is selected to be >=4.5X10<-7>g per 100g of the composition. The compounding is preferably carried out by mixing the above three components with each other to make a master batch having high pigment concentration, and adding the master batch to the residual high-density polyethylene. The polyolefin having polr group is a copolymer of a polar group-containing vinyl monomer and an olefin, preferably ethylene. The polar goup is preferably carboxyl group.

Description

【発明の詳細な説明】 本発明は、高密度ポリエチレンを主素材として、中空成
形法により、着色業務用容器を製造する際に生ずるダイ
ウェルドラインを実質的に解消した容器成形用樹脂組成
物およびその製造方法に関する。
DETAILED DESCRIPTION OF THE INVENTION The present invention provides a container-molding resin composition that substantially eliminates die-weld lines that occur when producing colored commercial containers using high-density polyethylene as a main material and a blow-molding method. It relates to its manufacturing method.

高密度ポリエチレンは、無味、無毒、無臭、耐薬品性、
成形性にすぐれる等の憂<の長所を有することから、薬
品、化粧品、食品用途などの家庭用小型、業務用大型容
器(びん)の成形に多量に用いられてきた。しかるに、
最近業務用液体洗剤用の内容積2〜1(l程度の中型び
んの需要が高まシ、該中型びんを中空成形することが試
みられた◎すなわち、押出機において可塑化溶融された
高密度ポリエチレンはマンドレルおよびコアに沿って押
出されパリソンを形成し、そのパリソンを金型に挾んで
空気を吹込み成形する。このパリソン形成過程において
、押出機から押出された溶融樹脂が分流し、再びパリソ
ン形成のため合流する際、合流線、通常ダイウェルドラ
インといわれる筋が屡々、1ないし数本中空びんの縦方
向に発生し、美麗感を損ねることが認められた。
High-density polyethylene is tasteless, non-toxic, odorless, chemical resistant,
Because it has certain advantages such as excellent moldability, it has been used in large quantities to mold small household containers (bottles) for use in pharmaceuticals, cosmetics, and food products, as well as large containers (bottles) for commercial use. However,
Recently, demand for medium-sized bottles with an internal volume of 2 to 1 (liter) for commercial liquid detergents has increased, and attempts have been made to blow-mold these medium-sized bottles. Polyethylene is extruded along a mandrel and a core to form a parison, and the parison is sandwiched between molds and air is blown into the mold. During this parison formation process, the molten resin extruded from the extruder is separated and recirculated into the parison. When merging for forming, one or more lines of merging, commonly called die weld lines, often appear in the vertical direction of the hollow bottle, detracting from its aesthetic appearance.

このダイウェルドライ/発生は、顔料中にチタ/ホワイ
トを含有するものに起り易いことが観察された。
It has been observed that this diewell drying/occurrence is more likely to occur in pigments containing tita/white.

本発明者は、このダイウェルドライン解消のため主素材
である高密度ポリエチレンに極性基含有のポリオレフィ
ンを少量存在せしめた結果、著しい改良効果のあること
を見出し、本発明を完成したものである。
The present inventors have discovered that, in order to eliminate this die weld line, adding a small amount of a polar group-containing polyolefin to the main material, high-density polyethylene, has a significant improvement effect, and has completed the present invention.

以下、本発明につき詳細に説明する。主素材である高密
度ポリエチレン(a)は、密度的0.93〜0.97F
/cm3.190℃におけるメルトフローレートが約0
.01〜IJ’/10分のもので、共重合成分として、
少量のプロピレン、l−ブテン、1−ペンテン、1−ヘ
キセン、4−メチル−1−ペンテンナトのα−オレフィ
ンが共重合しているものも含まれる。
Hereinafter, the present invention will be explained in detail. The main material, high-density polyethylene (a), has a density of 0.93 to 0.97F.
/cm3. Melt flow rate at 190℃ is approximately 0
.. 01 to IJ'/10 minutes, as a copolymer component,
It also includes those in which small amounts of α-olefins such as propylene, 1-butene, 1-pentene, 1-hexene, and 4-methyl-1-pentenato are copolymerized.

顔料(b)は、ポリオレフィンの着色に使用されている
ものであれば特に制限はない。たとえば、酸化チタン、
亜鉛華、リトポン、鉛白、クロムイエロー、チタンイエ
ロー、シンククロメート、ヘンジンイエロー、クロムパ
ーミリオン、アンバー、赤色酸化鉄、アリザリンレーキ
、リノールレッド、紺青、フタロシアニンブルー、群青
、酸化クロムグリーン、ミネラルバイオレット、カーボ
ンブランク、鉄黒、アニリンプラック、フタロシアニン
グリーン、コバルトブルーなどがある。
The pigment (b) is not particularly limited as long as it is used for coloring polyolefins. For example, titanium oxide,
Zinc white, lithopone, lead white, chrome yellow, titanium yellow, synchromate, Henjin yellow, chrome permillion, amber, red iron oxide, alizarin lake, linole red, navy blue, phthalocyanine blue, ultramarine blue, chromium oxide green, mineral violet, Available colors include carbon blank, iron black, aniline black, phthalocyanine green, and cobalt blue.

配合量は顔料の種類によって、又意図する着色度合によ
って適宜変化する。
The blending amount varies depending on the type of pigment and the intended degree of coloring.

極性基含有ポリオレフィン(C)としては、まずオレフ
ィン、好ましくはエチレンと極性基を含有するビニルモ
ノマーとの共重合体が挙げら九る。極性基含有ビニルモ
ノマーとしては、たとえばS酢酸ビニル、アクリル酸、
メタクリル酸、アクリル酸メチル、アクリル酸エチル、
メタクリル酸メチル、メタクリル酸エチル、マレイン酸
、マレイン酸無水物、フマール酸、イタコン酸、イタコ
ン酸無水物、ハイミック酸、無水ノ・イミノク酸、塩化
ビニル、アクリルアミドなどがある。
Examples of the polar group-containing polyolefin (C) include copolymers of olefins, preferably ethylene, and vinyl monomers containing polar groups. Examples of the polar group-containing vinyl monomer include S vinyl acetate, acrylic acid,
Methacrylic acid, methyl acrylate, ethyl acrylate,
Examples include methyl methacrylate, ethyl methacrylate, maleic acid, maleic anhydride, fumaric acid, itaconic acid, itaconic anhydride, himic acid, ino-iminocic anhydride, vinyl chloride, and acrylamide.

このような共重合体は通常のラジカル共重合、ポリオレ
フィンへのグラフト共重合等の手法で得られるし、又市
販されているものもある。つぎにポリオレフィン、好ま
しくはポリエチレンを酸化して、カルボン酸や水酸基を
該オレフィンに導入したものが挙げられる。この(C)
成分は、190℃でのメルトフローレートが約0.lJ
’/10分、粘度平均分子量約21万程度の高分子量の
ものから、粘度・F均分子量約800程度のワックス状
低分子量のものまで使用することができる。前記例示の
極性基含有ポリオレフィンの中で、特にカルボキシル基
含有ポリオレフィンが好ましい。
Such copolymers can be obtained by conventional methods such as radical copolymerization and graft copolymerization to polyolefin, and some are commercially available. Next, polyolefins, preferably polyethylene, may be oxidized to introduce carboxylic acid or hydroxyl groups into the olefin. This (C)
The components have a melt flow rate of approximately 0.0 at 190°C. lJ
' / 10 minutes, viscosity average molecular weight of about 210,000 high molecular weight ones to waxy low molecular weight ones of viscosity/F average molecular weight of about 800 can be used. Among the above-mentioned polar group-containing polyolefins, carboxyl group-containing polyolefins are particularly preferred.

(c)成分の使用量は、樹脂組成物の総量1001に対
して、極性基、たとえばカルボキシル基(C!0OH)
が4.5X10時i以上、好ましくは4.5 X 10
−6 J’以上存在するよう(c)を配合する。しかし
、高密度ポリエチレン本来の性質を損わないこと、又経
済性の観点から、多くても(c)成分として10部以内
である。
The amount of component (c) to be used is based on the total amount of the resin composition (1001).
is 4.5 x 10 or more, preferably 4.5 x 10
-6 J' or more of (c) is blended. However, from the viewpoint of not impairing the original properties of high-density polyethylene and from the viewpoint of economic efficiency, the amount of component (c) should be within 10 parts at most.

本発明組成物の調製方法はいわゆるマスターバッチ方式
が好ましい。すなわち、(1)多量の顔料と高密度ポリ
エチレンとを必要であれば通常用いられる分散剤と共に
混合し、高濃度顔料のペレット(マスターバッチ)をつ
くる。つぎに、(2)顔料濃度が所望のものとなるよう
このマスターバッチを高密度ポリエチレンと混合する。
The method for preparing the composition of the present invention is preferably a so-called masterbatch method. That is, (1) a large amount of pigment and high-density polyethylene are mixed together with a commonly used dispersant, if necessary, to produce pellets (masterbatch) of high-concentration pigment. Next, (2) this masterbatch is mixed with high density polyethylene to achieve the desired pigment concentration.

(C)成分は、(1)、(2)のいずれの段階で混合し
てもよいが、(1)の段階で混合し、マスターバッチ中
に混在せしめた方がダイウェルドラインの解消には効果
的である。この場合、(C)成分として低分子量のもの
を用いれば分散剤の役割を果し、高分子量のものを用い
れば、高密度ポリエチレンに代用することもできる。
Component (C) may be mixed at either step (1) or (2), but it is better to mix it at step (1) and mix it in the masterbatch to eliminate die weld lines. Effective. In this case, if a component (C) with a low molecular weight is used, it will play the role of a dispersant, and if a component with a high molecular weight is used, it can be substituted for high-density polyethylene.

以下実施例をもって説明する。実施例中の部は重量部を
、%は重量%を示す。
This will be explained below using examples. In the examples, parts indicate parts by weight, and percentages indicate weight %.

実施例1 メルトフローレート0.35り710m1n、密度0.
(1581部cm3の高密度ポリエチレン60部、チタ
ンホワイト23部、加工顔料(チタンホワイト50’6
、ワックス40 ’% %チタンイエローlo%を含有
)7部、粘度平均分子量2700 、密度0.93F/
(7)3、酸価30■・KOH/iのマレイン化ポリエ
チレンワックス10部を混合して着色用マスターバッチ
を調製した。ついで、メルト7o−レート0.351 
/ 10m1n (1りO′C: ) 、密度0.95
87’/cm3の高密度ポリエチレン100部に上記マ
スターバッチ5部を混合して、L/D = 20.90
問φの押出機を備えた中空成形機を用いて、樹脂温[1
4+5 ’Cで、パリソンを押出し、22の中空びんを
成形した。
Example 1 Melt flow rate 0.35 710 m1n, density 0.
(1581 parts cm3 high-density polyethylene 60 parts, titanium white 23 parts, processed pigment (titanium white 50'6
, containing 40'% wax (lo% titanium yellow) 7 parts, viscosity average molecular weight 2700, density 0.93F/
(7) A masterbatch for coloring was prepared by mixing 10 parts of maleated polyethylene wax with an acid value of 30 .KOH/i. Then, Melt 7o-rate 0.351
/ 10m1n (1O'C: ), density 0.95
Mix 5 parts of the above masterbatch with 100 parts of high-density polyethylene of 87'/cm3 to obtain L/D = 20.90.
Using a blow molding machine equipped with an extruder of about φ, the resin temperature [1
At 4+5'C, the parison was extruded to form 22 hollow bottles.

なお、全組成物100Fあたり、マレイン化ポリエチレ
ンワックス中のカルボキシル基は、約1.17XIO”
4P存在した。
In addition, the carboxyl group in the maleated polyethylene wax is approximately 1.17XIO" per 100F of the total composition.
There were 4P.

実施例2 実施例1で用いたマレイン化ポリエチレンワックス10
部の代わりに、マレイン化ポリエチレンワックス1部と
粘度平均分子量4000のポリエチレンワックス9部を
用いた以外は、実施例1と同様に実施し、中空びんを成
形した。カルボキシル基含量は全組成物1001中約1
.1’7 X 10−5 P存在した。
Example 2 Maleated polyethylene wax 10 used in Example 1
A hollow bottle was molded in the same manner as in Example 1, except that 1 part of maleated polyethylene wax and 9 parts of polyethylene wax having a viscosity average molecular weight of 4000 were used instead of 1 part of maleated polyethylene wax. Carboxyl group content is approximately 1 in 1001 of the total composition
.. 1'7 x 10-5 P were present.

実施例3 実施例2で用いたマレイン化ポリエチレンワックス1部
の代わりに、密度0.g71/1wi’、酸価20■・
KOH/P 、粘度平均分子量2400の酸化ポリエチ
レンワックスを用いた以外は、実施例2と同様に実施し
、中空びんを成形した。極性基含量はカルボキシル基換
算で全組成物100 J’中約’7.65 X 10−
6 、/存在した。
Example 3 In place of 1 part of the maleated polyethylene wax used in Example 2, a density of 0. g71/1wi', acid value 20■・
A hollow bottle was molded in the same manner as in Example 2, except that KOH/P and oxidized polyethylene wax having a viscosity average molecular weight of 2,400 were used. The polar group content is approximately 7.65 x 10- in 100 J' of the total composition in terms of carboxyl groups.
6,/existed.

実施例4 実施例1で用いたマスターバッチにおいて、マレイン化
ポリエチレンワックスの代わりに粘度・ト均分子量24
00のポリエチレンワックスを用い、且つ該マスターパ
ッチにメルトフローレート1op/10m1n、密度0
.93 J’ 7cm3の無水マレイン酸クラフトポリ
エチレン5部を追加した以外は、実施例1と同様に実施
し、中空びんを成形した。カルボキシル基含有量は、全
組成物100p中、約1.04 X 10−4り存在し
た。
Example 4 In the masterbatch used in Example 1, a viscosity/average molecular weight of 24 was used instead of maleated polyethylene wax.
00 polyethylene wax was used, and the master patch had a melt flow rate of 1 op/10 m1n and a density of 0.
.. A hollow bottle was molded in the same manner as in Example 1, except that 5 parts of maleic anhydride kraft polyethylene of 7 cm3 of 93 J' were added. The carboxyl group content was approximately 1.04 x 10-4 in 100 p of the total composition.

実施例5 実施例1で用いたベースレジンの高密度ポリエチレン1
00部の代わりに、同じ高密度ポリエチレン99.5部
と無水マレイン酸クラフトポリエチレン0.5部とを用
い、且つマスターパッチにおいて、マレイン化ポリエチ
レンワックスの代わりに粘度下−均分子量4000のポ
リエチレンワックスを用いる以外は、実施例1と同様に
実施し、中空びんを成形した。カルボキシル基含有量は
、全組成物100/111、約2.16 X 10−4
7’存在した。
Example 5 High-density polyethylene 1 of the base resin used in Example 1
00 parts, the same high-density polyethylene 99.5 parts and maleic anhydride kraft polyethylene 0.5 parts were used, and in the master patch, instead of maleated polyethylene wax, polyethylene wax with a viscosity average molecular weight of 4000 was used. A hollow bottle was molded in the same manner as in Example 1 except for using the following. Carboxyl group content is 100/111 for all compositions, approximately 2.16 x 10-4
7' existed.

比較例1 メルトフローレート0.35P/10分、密度−0,9
587’/crn”の高密度ポリエチレン60部、チタ
ンホワイト23部、実施例1と同じ加工顔料7部および
溶融粘度550CPSのポリエチレンワックス10部を
混合して着色用マスターバッチを調製した。ついで、メ
ルトフローレート0.351710分、密度0.958
J’/cm”の高密度ポリエチレン100部に上記マス
ターバッチ5部を混合して、L/D = 20の901
8φの押出機を備えた中空成形機にてパリソン(樹脂温
度195℃)を押出し、2Qの中空びんを成形した。
Comparative example 1 Melt flow rate 0.35P/10 minutes, density -0.9
A coloring masterbatch was prepared by mixing 60 parts of high-density polyethylene of 587'/crn'', 23 parts of titanium white, 7 parts of the same processed pigment as in Example 1, and 10 parts of polyethylene wax with a melt viscosity of 550 CPS. Flow rate 0.351710 minutes, density 0.958
5 parts of the above masterbatch were mixed with 100 parts of high-density polyethylene of J'/cm'' to obtain 901 with L/D = 20.
A parison (resin temperature: 195° C.) was extruded using a blow molding machine equipped with an 8φ extruder to mold a 2Q hollow bottle.

比較例2 比較例1で用いたマスターバッチ中の高密度ポリエチレ
ン60部の代わりに、高密度ポリエチレン、50部、メ
ルトフローレート1.3 //10m1n、密度0.9
20、F 7cm3の低密度ポリエチレン10部を用い
た以外は比較例1と同様に実施し、中空びんを成形した
Comparative Example 2 Instead of 60 parts of high-density polyethylene in the masterbatch used in Comparative Example 1, 50 parts of high-density polyethylene, melt flow rate 1.3 //10 m1n, density 0.9
A hollow bottle was molded in the same manner as in Comparative Example 1, except that 10 parts of low-density polyethylene of 20.F 7cm3 was used.

以上の実施例、比較例で得た中空びんの外観を目視観察
した結果を第1表に示した。
Table 1 shows the results of visual observation of the appearance of the hollow bottles obtained in the above Examples and Comparative Examples.

第  1  表 外観の評価はダイウェルドラインが表面に目視でくっき
り見える状態を1、全然見えない状態を5として全体を
5段階に分けて評価した。
Table 1: Appearance was evaluated in 5 grades, with 1 indicating that the die weld line was clearly visible on the surface and 5 indicating that it was not visible at all.

なお、実施例1〜5において、いずれも成形性は良好で
あり、又、得られたびんに洗剤を充填シフ。
In addition, in Examples 1 to 5, all had good moldability, and the resulting bottles were filled with detergent.

60℃で150時間放置し、耐ストレスクラツキング性
を試験したところいずれも良好であった。
When the stress cracking resistance was tested after being left at 60° C. for 150 hours, all results were good.

代理人 弁理士 井 上 雅 生Agent: Patent attorney Masao Inoue

Claims (1)

【特許請求の範囲】 1、  (a)高密度ポリエチレン、(b)顔料、およ
び(C)極性基含有ポリオレフィンからなり、(C)中
に含有する極性基の量が樹脂組成物1001当シ、少な
くとも4.5 X 10−’J’以上存在することを特
徴とする樹脂組成物。 2、 高密度ポリエチレンの一部に顔料および極性基含
有ポリオレフィンを予め混合し、高顔料濃度のマスター
バッチをつ<シ、該マスターパンチと残余の高密度ポリ
エチレンとを混合し、且つ極性基含有ポリオレフィン中
に含有する極性基の量が樹脂組成物100 J’当り、
少なくとも4.5 X 10−”1以上存在させること
を特徴とする樹脂組成物の製造方法。
[Claims] 1. Consisting of (a) high-density polyethylene, (b) pigment, and (C) polar group-containing polyolefin, the amount of polar groups contained in (C) is 1001, A resin composition characterized in that the resin composition contains at least 4.5 x 10-'J'. 2. Mix a pigment and a polar group-containing polyolefin in advance with a portion of high-density polyethylene, prepare a masterbatch with a high pigment concentration, mix the master punch with the remaining high-density polyethylene, and prepare a polar group-containing polyolefin. The amount of polar groups contained therein per 100 J' of the resin composition,
A method for producing a resin composition, characterized in that the resin composition is present at least 4.5 x 10-"1 or more.
JP20660081A 1981-12-21 1981-12-21 Resin composiion and its preparation Granted JPS58108240A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP20660081A JPS58108240A (en) 1981-12-21 1981-12-21 Resin composiion and its preparation

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP20660081A JPS58108240A (en) 1981-12-21 1981-12-21 Resin composiion and its preparation

Publications (2)

Publication Number Publication Date
JPS58108240A true JPS58108240A (en) 1983-06-28
JPH037497B2 JPH037497B2 (en) 1991-02-01

Family

ID=16526071

Family Applications (1)

Application Number Title Priority Date Filing Date
JP20660081A Granted JPS58108240A (en) 1981-12-21 1981-12-21 Resin composiion and its preparation

Country Status (1)

Country Link
JP (1) JPS58108240A (en)

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS58198534A (en) * 1982-04-24 1983-11-18 Toppan Printing Co Ltd Highly concentrated plastic colorant
JPS62235956A (en) * 1986-04-05 1987-10-16 Ricoh Co Ltd Coloring agent and utilization thereof
JPH0931206A (en) * 1995-07-14 1997-02-04 Toyo Ink Mfg Co Ltd Composition for coloration
KR970065596A (en) * 1996-03-20 1997-10-13 마르코위츠 스티븐 에이치 Masterbatch Blends for the Production of Polyolefin Products
JPH10279772A (en) * 1997-04-07 1998-10-20 Toyo Ink Mfg Co Ltd Colorant composition for paving material
JP2017014522A (en) * 2016-08-29 2017-01-19 東洋インキScホールディングス株式会社 Resin composition for color molding

Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS57174327A (en) * 1981-04-22 1982-10-27 Idemitsu Kosan Co Ltd Color-improved polyolefin composition

Patent Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS57174327A (en) * 1981-04-22 1982-10-27 Idemitsu Kosan Co Ltd Color-improved polyolefin composition

Cited By (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS58198534A (en) * 1982-04-24 1983-11-18 Toppan Printing Co Ltd Highly concentrated plastic colorant
JPS6339012B2 (en) * 1982-04-24 1988-08-03 Toppan Printing Co Ltd
JPS62235956A (en) * 1986-04-05 1987-10-16 Ricoh Co Ltd Coloring agent and utilization thereof
JPH0931206A (en) * 1995-07-14 1997-02-04 Toyo Ink Mfg Co Ltd Composition for coloration
KR970065596A (en) * 1996-03-20 1997-10-13 마르코위츠 스티븐 에이치 Masterbatch Blends for the Production of Polyolefin Products
JPH10279772A (en) * 1997-04-07 1998-10-20 Toyo Ink Mfg Co Ltd Colorant composition for paving material
JP2017014522A (en) * 2016-08-29 2017-01-19 東洋インキScホールディングス株式会社 Resin composition for color molding

Also Published As

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JPH037497B2 (en) 1991-02-01

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