JPS6053510A - Polypropylene resin for drawing - Google Patents

Polypropylene resin for drawing

Info

Publication number
JPS6053510A
JPS6053510A JP58158989A JP15898983A JPS6053510A JP S6053510 A JPS6053510 A JP S6053510A JP 58158989 A JP58158989 A JP 58158989A JP 15898983 A JP15898983 A JP 15898983A JP S6053510 A JPS6053510 A JP S6053510A
Authority
JP
Japan
Prior art keywords
molecular weight
polypropylene
polypropylene resin
low
measured
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
JP58158989A
Other languages
Japanese (ja)
Other versions
JPH0549689B2 (en
Inventor
Tadashi Asanuma
正 浅沼
Shinryu Uchikawa
進隆 内川
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 Toatsu Chemicals Inc
Original Assignee
Mitsui Toatsu Chemicals Inc
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 Toatsu Chemicals Inc filed Critical Mitsui Toatsu Chemicals Inc
Priority to JP58158989A priority Critical patent/JPS6053510A/en
Publication of JPS6053510A publication Critical patent/JPS6053510A/en
Publication of JPH0549689B2 publication Critical patent/JPH0549689B2/ja
Granted legal-status Critical Current

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Landscapes

  • Addition Polymer Or Copolymer, Post-Treatments, Or Chemical Modifications (AREA)
  • Shaping By String And By Release Of Stress In Plastics And The Like (AREA)

Abstract

PURPOSE:Polypropylene resin for drawing, consisting of polypropylene having specific properties, having improved processability, capable of giving molded articles having good physical properties, and useful for films and tapes such as film grade, flat yarn grade, etc. CONSTITUTION:Polypropylene resin, obtained by polymerizing propylene in the presence of (A) titanium tetrachloride catalyst supported on magnesium chloride, and having >=8MW/MN on the high-molecular weight side and <=10MW/MN on the low-molecular weight side, obtained by measuring the molecular weight by gel permeation chromatography, and approximating the molecular weight from the molecular weight distribution curve, prepared by plotting the amount eluted versus the molecular weight expressed in natural logarithm with the peak position as a center, and dividing the curve into the high-molecular weight, low- molecular weight and medium-molecular weight regions using the Gaussian distribution and >=0.95 isotactic pentad measured by <13>C NMR. EFFECT:Even low-molecular weight polypropylene can be drawn.

Description

【発明の詳細な説明】 本発明は加工性に優れ、しかも延伸して得られた成形物
の物性が良好な、ポリプロピレン樹脂に関する。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a polypropylene resin which is excellent in processability and has good physical properties in molded products obtained by stretching.

ポリプロピレンは剛性が良好であり、特に延伸したもの
は引張り強度に優れたものであることから、フィルム及
びテープなどの用途に多く用いられている。しかしなが
ら強度、特に引張り強度の良好なものを得るために通常
比較的メルトフローインデックスの小さいポリプロピレ
ンが選択されるため、その成形時に於いて、比較的大き
いエネルギーを必要としており、省エネルギーの点から
も、物性が良好でしかも加工性に優れたプロピレン樹脂
が望まれる。
Polypropylene has good rigidity, and especially when stretched, it has excellent tensile strength, so it is widely used in applications such as films and tapes. However, in order to obtain good strength, especially tensile strength, polypropylene with a relatively low melt flow index is usually selected, and therefore a relatively large amount of energy is required during the molding process. A propylene resin with good physical properties and excellent processability is desired.

本発明は、種々の検討を行った結果、特定の性質を有す
るポリプロピレンが加工性が良好でしかも延伸された成
形物の物性も良好であることを見い出し本発明を完成し
た。
As a result of various studies, the present invention was completed after discovering that polypropylene having specific properties has good processability and also has good physical properties of stretched molded products.

本発明の目的は、加i性に嘲れしかも延伸して得られた
成形物の物性の良好なポリプロピノう樹ラフイーで測定
し、縦軸を溶出量、横軸を分子量の自然対数で表わした
分子量分布曲線のピーク位置を中心として高分子量域、
低分子量域、中間量域にわけそれぞれについてガウス分
布で近似した時のMw/MNが高分子量側で8以上、低
分子量側で10以下 口)I″CNMRで測定したアイ
ソタクチックペンタッド分率が0.95 以上であるこ
とを特徴とする加工性の巨好な延伸用ポリプロピレン樹
脂に関する。
The object of the present invention is to measure polypropyl resin roughy, which has good physical properties of molded products obtained by stretching and is characterized by its additive properties, and the vertical axis represents the elution amount, and the horizontal axis represents the natural logarithm of the molecular weight. High molecular weight region centered around the peak position of the molecular weight distribution curve,
Mw/MN is 8 or more on the high molecular weight side and 10 or less on the low molecular weight side when approximated by Gaussian distribution for each of the low molecular weight range and intermediate weight range. The present invention relates to a polypropylene resin for stretching that has excellent processability and is characterized by having a polypropylene resin of 0.95 or more.

本発明のポリプロピレン樹脂は高立体規則性のものであ
り、6ONMR(400MH2)で測定したアイソタク
テイクベンタノド分率はA Zambc l l iら
によって帰属されMacromolecules 86
87(1975)に記載された方法に従いN M i(
、で測定され、メチル炭素の各ピークの面積比によって
定められた値である。
The polypropylene resin of the present invention has high stereoregularity, and the isotactic bentanod fraction measured by 6ONMR (400MH2) was assigned by A Zambcil et al.
87 (1975), N M i (
, and is a value determined by the area ratio of each peak of methyl carbon.

ペンタッド分率が0.95 以下ではポリプロピレン樹
脂として剛性及び引張強度が不足し好ましくない。好ま
しい範囲は0.95〜0.99程度である。
If the pentad fraction is less than 0.95, the polypropylene resin will lack rigidity and tensile strength, which is not preferable. The preferred range is about 0.95 to 0.99.

本発明のポリプロピレンの分子量分布は次のようにして
測定された値である。ゲルパーミェーションクロマトグ
ラフによって測定された(例えば1358Cで1.2.
4〜トリクロロベンゼンを移動層としてカラムとして5
hodeX A−80’M 2本を用いて測定される。
The molecular weight distribution of the polypropylene of the present invention is a value measured as follows. measured by gel permeation chromatography (e.g. 1.2 at 1358C).
4 to 5 as a column with trichlorobenzene as a mobile phase
Measured using two hodeX A-80'M.

)クロマドグ27を用いて図に示すように横軸を分子量
の自然対数で表わし、縦軸を溶出量で表わした分子量分
布曲線を3分割し高分子量側ピーク付近及び低分子量側
についてそれぞれガウス分布に近似してめる。
) Using Chromadog 27, as shown in the figure, the molecular weight distribution curve, in which the horizontal axis is represented by the natural logarithm of the molecular weight and the vertical axis is represented by the elution amount, is divided into three parts, and a Gaussian distribution is created around the peak on the high molecular weight side and on the low molecular weight side, respectively. Approximate it.

分子量分布をガウス分布で近似する方法は、例えばJo
urnal of Chromatographic 
5ciencevol 20 June 198225
2に詳細に説明しである。
For example, the method of approximating the molecular weight distribution with a Gaussian distribution is as follows:
urnal of chromatographic
5ciencevol 20 June 198225
2 is explained in detail.

即ち分子量分布曲線を下式で近似する。That is, the molecular weight distribution curve is approximated by the following formula.

Y = Ym、exp (−(X−XnJ/2FfEY
;分子量の自然対数(In(分子量))Xの時のの高さ 茄;ピーク分子量の自然対数(1n(ピーク分子量)X
mの時の高さ又は3分割した時の境界点に一致するよう
に算出したピーク高さ。)S−1l](重量子均分−7
−17数〒可券子量)ことによって重量平均分子量/数
乎均分子量 即ちMw/MHが算出される。こうしてめ
た上記比率のうち加工性に大きな影響を与えるのは特に
高分子量側での値であり8以上である必要がある。
Y = Ym, exp (-(X-XnJ/2FfEY
;Natural logarithm of molecular weight (In (molecular weight))
The peak height calculated to match the height at m or the boundary point when divided into three. )S-1l] (Weight molecular weight -7
-17 number (noteable molecular weight), weight average molecular weight/number average molecular weight, ie, Mw/MH is calculated. Of the above ratios thus determined, it is the value on the high molecular weight side that has a large effect on processability, and must be 8 or more.

好ましくは、8〜25であり、8以下では加工性の改良
が不充分であり、25以上では物性の低下が見られる。
Preferably, it is 8 to 25; if it is less than 8, the improvement in processability is insufficient, and if it is more than 25, a decrease in physical properties is observed.

低分子量側の比率は成形品の外観に大きな影響を与え1
0以トでは表面の状態が不良で好ましくない。好ましい
範囲は4〜10である。
The ratio of low molecular weight side has a great influence on the appearance of the molded product.
If it is 0 or less, the surface condition is poor and undesirable. The preferred range is 4-10.

本発明の樹脂は延伸用として好ましく用いられフィルム
グレード、フラットヤーングレードとして好適に用いら
れる。
The resin of the present invention is preferably used for stretching, and is suitably used as film grade and flat yarn grade.

本発明のポリプロピレン樹脂は種々の方法で製造可能で
あるが一例を挙げれば公知の1″」[々の塩化マグネシ
ウムに担持した四塩化チタン触媒と、有機アルミニウム
化合物からなる触媒系の中でも高立体規則性のポリプロ
ピレンを与えるもの、場合によってはエステル系の化合
物を加えてさらに高立体規則性のポリプロピレンを与え
る触媒系としたものを用いることが好ましい。
The polypropylene resin of the present invention can be produced by various methods, but to give an example, the polypropylene resin with high stereoregularity is used among the catalyst systems consisting of a titanium tetrachloride catalyst supported on magnesium chloride and an organoaluminum compound. It is preferable to use a catalyst system that provides polypropylene with high stereoregularity, and in some cases, an ester compound is added to form a catalyst system that provides polypropylene with high stereoregularity.

上記触媒系を用いてプロピレン自身を液状媒体とする塊
状重合法でそれも比較的高温即ち65℃〜80℃の温度
でプロピレンを重合し、次いでプロピレンなどの低沸点
炭化水素でプロピレン可溶の低立体規則性のポリプロピ
レンを除去することによって得られる。
This is a bulk polymerization method using propylene itself as a liquid medium using the above catalyst system, in which propylene is polymerized at a relatively high temperature, that is, 65°C to 80°C, and then a low boiling point hydrocarbon such as propylene is used to polymerize propylene. Obtained by removing stereoregular polypropylene.

本発明のポリプロピレン樹脂は延伸フィルム用或はフラ
ットヤーン等の延伸用樹脂として、得られた成形物が剛
性及び引張強度が大きくしかも成形時のエネルギーが少
なくてすみまた驚くべきことに比較的低分子量のポリプ
ロピレン(メルトフローインデックスが大きいもの)で
も延伸が可能であるという工業的意義の極めて高いもの
である。
The polypropylene resin of the present invention can be used as a resin for stretching films or flat yarns, etc., so that the resulting molded products have high rigidity and tensile strength, require less energy during molding, and surprisingly have a relatively low molecular weight. This is of extremely high industrial significance as it is possible to stretch even polypropylene (with a high melt flow index).

以下に実施例を挙げ本発明をさらに具体的に説明する。EXAMPLES The present invention will be explained in more detail with reference to Examples below.

実施例1.2及び比較例1.2 禦胎示したポリプロピレン樹脂を用いて2軸延伸フイル
ムを製膜し物性を測定した。
Example 1.2 and Comparative Example 1.2 Biaxially stretched films were formed using the polypropylene resins shown above, and their physical properties were measured.

2軸延伸フイルムは、TMロング社の2軸延伸機を用い
4. Q m/m 下向ダイで原反を製膜(押し出し温
度250℃で厚さ750μ) L 150℃で60秒加
熱し延伸倍率(MDxTD)=5 X7 延伸スピード
10 cm/ secで製膜し物性値は次の方法で測定
した。
4. The biaxially stretched film was produced using a biaxially stretched machine manufactured by TM Long Co., Ltd. Q m/m Form the original fabric into a film with a downward die (extrusion temperature 250°C, thickness 750μ) L Heating at 150°C for 60 seconds, stretching ratio (MDxTD) = 5 X7 Film forming at a drawing speed of 10 cm/sec Physical properties The value was measured by the following method.

メルトフローインデックス、9−/I Qtnin 2
30°C2,16kg荷重で測定 JISK7210 ヘ イ ズ 、ASTM D1003 %ヤング率 、
 ASTM I)882 kg/in♂引張強度 、 
AS’l”M I)638 k!//++ui’熱収縮
率 、ASTM 1)1206により120°CX15
m1nでそれぞれ測定し、結果は表1に示した。
Melt flow index, 9-/I Qtnin 2
Measured at 30°C2, 16kg load JISK7210 haze, ASTM D1003% Young's modulus,
ASTM I) 882 kg/in♂ tensile strength,
AS'l"M I) 638 k!//++ui' Heat shrinkage rate, 120°CX15 according to ASTM 1) 1206
The results are shown in Table 1.

実施例3.4及び比較例3〜5 そ劣り1h目牛表2に示したポリグロビイントr1脂を
用いてフラットヤーンを製膜し物性を測定した。
Example 3.4 and Comparative Examples 3 to 5 Poor 1-h cow A flat yarn was formed using the polyglobint r1 fat shown in Table 2, and its physical properties were measured.

フラットヤーンは日本製鋼社製の112朋φ(L/■)
−28)の押出機で1700龍の下向′1゛〜ダイで原
反を製膜(押し出し温度約250°Cで厚さ160μ)
しスリッターで6mm巾にした後、100°Cで所定の
延伸を行い100〜150°Cでアニール後巻きとって
約1100 デニル、巾2.4mmのヤーンを成形し、
物性を測定した。 ■の唄ツ虻1よ 強 度、JIS L−10739/d 伸 度、JIS L−1073% 初期抵抗、伸度5チにおける強度X2a り/dにより
それぞれめ押出機の樹脂温度及びメインモーターの電流
は同一成形速度となるように条件を定め、それぞれの値
は表2に示した。
The flat yarn is 112mmφ (L/■) manufactured by Nippon Steel Corporation.
-28) Extruder with a 1700 x 1700 x 100mm downward die to form a film (thickness: 160μ at extrusion temperature of about 250°C)
After cutting the yarn to a width of 6 mm using a slitter, it was stretched to a specified temperature at 100°C, annealed at 100 to 150°C, and then wound to form a yarn of approximately 1100 denier and a width of 2.4 mm.
Physical properties were measured. ■ No Uta Tsuji 1 strength, JIS L-10739/d elongation, JIS L-1073% initial resistance, strength at elongation 5 The conditions were set so that the molding speed was the same, and the respective values are shown in Table 2.

比較的低温で押出電力が少ない条件であるにもが又わら
ず実施例では物性の良好なものが得られることがわかる
It can be seen that although the conditions were relatively low temperature and low extrusion power, in the examples, products with good physical properties were obtained.

【図面の簡単な説明】[Brief explanation of drawings]

図面はゲルパーミェーションクロマトグラフィーで測定
した分子量分布曲線と、その3分割の状態を示す図であ
り、横軸は自然対数で表わした分子量を、縦軸は溶出量
を、それぞれ示す。横軸の左が高分子量布が低分子量で
ある。 aは高分子量域1/3 を、 bは中間量域 1/3 を、 Cは低分子量域1/3 を、 実線は実測分子量分布曲線を、 破線は近似分子量分布曲線のピークへの外挿を縦軸は溶
出量(高さ)をそれぞれ示し、横軸は左側が高分子量側
を右側が低分子量側をI n(分子量で目盛り、Oはピ
ーク及び境界点をそれぞれ示す。 図面
The figure shows a molecular weight distribution curve measured by gel permeation chromatography and its three-division state, where the horizontal axis shows the molecular weight expressed in natural logarithm, and the vertical axis shows the elution amount. On the left side of the horizontal axis, high molecular weight cloth has low molecular weight. a represents 1/3 of the high molecular weight region, b represents 1/3 of the intermediate weight region, C represents 1/3 of the low molecular weight region, the solid line is the measured molecular weight distribution curve, and the broken line is extrapolation to the peak of the approximate molecular weight distribution curve. The vertical axis shows the elution amount (height), and the horizontal axis shows the high molecular weight side on the left and the low molecular weight side on the right (scaled by molecular weight, O shows the peak and boundary point, respectively.

Claims (1)

【特許請求の範囲】[Claims] イ)ケルパーミェーションクロマトグラフィーで測定し
縦軸を溶出量、横軸を分子量の自然対数で表わした分子
量分布曲線のピーク位置を中心として高分子量域、低分
子量域、中間量域にわけそれぞれについてガウス分布で
近似した時のM w/M Nが高分子量側で8以上、低
分子量側で10以下口)’bNMRで測定したアイソタ
クチックペンタッド分率が0.95以上であることを特
徴とする加工性の良好な延伸用ポリプロピレン樹脂。
b) Divided into high molecular weight range, low molecular weight range, and intermediate weight range around the peak position of the molecular weight distribution curve measured by Köl permeation chromatography and showing the elution amount on the vertical axis and the natural logarithm of the molecular weight on the horizontal axis. The isotactic pentad fraction measured by NMR must be 0.95 or more. Polypropylene resin for stretching with good processability.
JP58158989A 1983-09-01 1983-09-01 Polypropylene resin for drawing Granted JPS6053510A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP58158989A JPS6053510A (en) 1983-09-01 1983-09-01 Polypropylene resin for drawing

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP58158989A JPS6053510A (en) 1983-09-01 1983-09-01 Polypropylene resin for drawing

Publications (2)

Publication Number Publication Date
JPS6053510A true JPS6053510A (en) 1985-03-27
JPH0549689B2 JPH0549689B2 (en) 1993-07-27

Family

ID=15683781

Family Applications (1)

Application Number Title Priority Date Filing Date
JP58158989A Granted JPS6053510A (en) 1983-09-01 1983-09-01 Polypropylene resin for drawing

Country Status (1)

Country Link
JP (1) JPS6053510A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2014145072A (en) * 2012-10-30 2014-08-14 China Petroleum & Chemical Corp Narrow molecular weight distribution polypropylene and its preparation method
WO2023079785A1 (en) * 2021-11-05 2023-05-11 住友化学株式会社 Propylene-based polymer composition, method for producing propylene-based polymer composition, and biaxially oriented film

Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS55102606A (en) * 1979-01-30 1980-08-06 Mitsui Toatsu Chem Inc Polymerization of alpha-olefin
JPS5894927A (en) * 1981-11-27 1983-06-06 Mitsubishi Electric Corp Method of wire-cutting electric discharge machining

Patent Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS55102606A (en) * 1979-01-30 1980-08-06 Mitsui Toatsu Chem Inc Polymerization of alpha-olefin
JPS5894927A (en) * 1981-11-27 1983-06-06 Mitsubishi Electric Corp Method of wire-cutting electric discharge machining

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2014145072A (en) * 2012-10-30 2014-08-14 China Petroleum & Chemical Corp Narrow molecular weight distribution polypropylene and its preparation method
US10301405B2 (en) 2012-10-30 2019-05-28 Beijing Research Institute Of Chemical Industry, China Petroleum & Chemical Corp Polypropylene with narrow molecular weight distribution range and processes for preparation thereof
WO2023079785A1 (en) * 2021-11-05 2023-05-11 住友化学株式会社 Propylene-based polymer composition, method for producing propylene-based polymer composition, and biaxially oriented film

Also Published As

Publication number Publication date
JPH0549689B2 (en) 1993-07-27

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