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US4499247A Expired / Lapsed US ⏱️ 0.0 years remaining

High-rigidity, high-melt-viscoelasticity polypropylene and process for producing the same

Assignee: JNC Corp
•
Filing: 1983-06-07
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Granted: 1985-02-12
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Expires: 2003-06-07
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Abstract

Abstract A superior high-rigidity and high-melt-viscoelasticity polypropylene for sheets to be post-processed and for blow molding is provided which polypropylene is produced by subjecting propylene to a multi-stage polymerization into polymer portions of two sections in the presence of a specified Ziegler Natta catalyst, the relationship between the intrinsic viscosities of the polymer portions of the respective sections being regulated within a specified range and also the amount ratio of the polymer portions of the respective sections being regulated.

Inventors

  • 👤 Hiromasa Chiba
  • 👤 Kenjiro Obama
  • 👤 Shunji Kawazoe
  • 👤 Takahiro Oka
  • 👤 Akihiro Satoh

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-10-31 03:46
CPC Classifications
C; C08; C08F; C08F10/00; C08F10/04; C08F10/06; Y; Y10; Y10S; Y10S526/00; Y10S526/905

Claims Analysis

Total Claims: 7
Claim 1
Independent Claim 230 words
A process for producing a high-rigidity and high-melt-viscoelasticity polypropylene for sheets to be post-processed and for blow molding, obtained by subjecting propylene to a multi-stage polymerization in the presence of a catalyst prepared by reacting an organoaluminum compound (I) or a reaction product of an organoaluminum compound (I) with an electron donor (A), with TiCl 4 (C); reacting the resulting solid product (II) with an electron donor (A) and an electron acceptor (B); and combining the resulting solid product (III) with an organoaluminum compound (IV) and an aromatic carboxylic acid ester (V), so as to give a molar ratio (V/VIII) of the aromatic carboxylic acid ester to the solid product (III) of 0.1 to 10.0; in this polymerization, adjusting the amount of propylene polymerized at the first stage so as to constitute 35 to 65% by weight based on the total amount polymerized and that at the second stage et seq so as to constitute 65 to 35% by weight based thereon; and when the intrinsic viscosity of the polymer portion having a higher molecular weight is named [η] H and that having a lower molecular weight is named [η] L , between the polymer portion formed at the first stage and that formed at the second stage et seq, adjusting the intrinsic viscosity values of the respective polymer portions so as to satisfy a relationship 3.0≦[η].sub.H -[η].sub.L ≦6.5 (1).
Claim 2
Dependent Claim 230 words
A process for producing a high-rigidity and high-melt-viscoelasticity polypropylene for sheets to be post-processed and for blow molding, obtained by subjecting propylene to a multi-stage polymerization in the presence of a catalyst prepared by reacting an organoaluminum compound (I) or a reaction product of an organoaluminum compound (I) with an electron donor (A), with TiCl 4 (C); reacting the resulting solid product (II) with an electron donor (A) and an electron acceptor (B); and combining the resulting solid product (III) with an organoaluminum compound (IV) and an aromatic carboxylic acid ester (V), so as to give a molar ratio (V/VIII) of the aromatic carboxylic acid ester to the solid product (III) of 0.1 to 10.0; in this polymerization, adjusting the amount of propylene polymerized at the first stage so as to constitute 35 to 65% by weight based on the total amount polymerized and that at the second stage et seq so as to constitute 65 to 35% by weight based thereon; and when the intrinsic viscosity of the polymer portion having a higher molecular weight is named [η] H and that having a lower molecular weight is named [η] L , between the polymer portion formed at the first stage and that formed at the second stage et seq, adjusting the intrinsic viscosity values of the respective polymer portions so as to satisfy a relationship 3.0≦[η].sub.H -[η].sub.L ≦6.5 (1).
Claim 3
Dependent Claim 25 words
A process for producing a polypropylene according to claim 1, having a melt flow index (MI) in the range of 0.03 to 2.0 g/10 min.
Claim 4
Dependent Claim 19 words
A process for producing a polypropylene according to claim 1 wherein said organoaluminum compound (IV) is a dialkylaluminum monohalide.
Claim 5
Dependent Claim 41 words
A process for producing a polypropylene according to claim 1 wherein an α-olefin is reacted with the combination of said solid product (III) with said organoaluminum compound (IV) and said aromatic carboxylic acid ester, and the resulting preactivated catalyst is used.
Claim 6
Dependent Claim 32 words
A process for producing a polypropylene according to claim 1 wherein the relationship between its isotactic pentad ratio (P) and MFR is adjusted to be in the range of 1.0a≧P≧0.015 log MFR+0.955.
Claim 7
Dependent Claim 45 words
A process for producing a polypropylene according to claim 1 wherein the relationship between its melt flow index (HMI) (10.8 Kg/10 min., 230° C.) and melt flow index (MI) (2.16 Kg/10 min., 230° C.) is adjusted to satisfy an equation log HMI-0.922 log MI≧1.44 (2).

References Cited (Backward Citations)

JPS5438389A Cited
JPS5670014A Cited
US4309521A Cited
US4420593A Cited
GB2094319A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1988-02-12 1988-08-13 1989-02-12 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1992-02-12 1992-08-13 1993-02-12 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1996-02-12 1996-08-13 1997-02-12 $7700.00 Window Closed / Lapsed

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