US4499247A
Expired / Lapsed
US
⏱️ 0.0 years remaining
High-rigidity, high-melt-viscoelasticity polypropylene and process for producing the same
Assignee: JNC Corp
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Filing: 1983-06-07
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Granted: 1985-02-12
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Expires: 2003-06-07
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)
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 |