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US4245062A Expired / Lapsed US ⏱️ 0.0 years remaining

Process for producing propylene-ethylene copolymers

Assignee: JNC Corp
•
Filing: 1979-09-11
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Granted: 1981-01-13
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Expires: 1999-09-11
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Abstract

Abstract A process for producing a modified polypropylene by copolymerizing propylene with ethylene in the presence of a Ziegler-Natta catalyst is provided. This process consists of the following three steps: a first step of carrying out polymerization so as to give a propylene polymer corresponding to 75-90% by weight based on a final modified polypropylene and having an ethylene content of 2% by weight or lower, a second step of preparing an ethylene-propylene random copolymer (A) having an intrinsic viscosity of 12 dl/g or higher and an ethylene content of 50-95% by weight; and a third step of preparing an ethylene-propylene random copolymer (B) having an intrinsic viscosity of 9.5 dl/g or lower and an ethylene content of 40-90% by weight, the proportion of said (A) in the total amount of said (A) and (B) being adjusted to 4-30% by weight. In this process, it is possible to prepare said (B) in the second step and then prepare said (A) in the third step. The resulting copolymer product has improved low-temperature impact strength, high brittle temperature and melt flow characteristics along with stiffness and luster of polypropylene.

Inventors

  • 👤 Takeshi Suzuki
  • 👤 Hiromasa Chiba
  • 👤 Ryohichi Yasunaga
  • 👤 Hironaka Sekine

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-10-30 04:19
CPC Classifications
C; C08; C08F; C08F297/00; C08F297/06; C08F297/08; C08F297/083; C08F297/086

Claims Analysis

Total Claims: 6
Claim 1
Independent Claim 224 words
In a process for producing a modified polypropylene having an ethylene content of 5 to 20% by weight, by copolymerizing propylene with ethylene in the presence of a stereospecific catalyst comprising an organoaluminum compound component and a transition metal halide component, the improvement of the process which comprises a first step of carrying out polymerization so as to give a propylene polymer corresponding to 75 to 90% by weight based on the weight of a final modified polypropylene and having an ethylene content of 2% by weight or less; a second step of preparing an ethylene-propylene random copolymer (A) having an intrinsic viscosity of 12 dl/g or higher as measured in tetralin at 135° C. and an ethylene content of 50 to 95% by weight; and a third step of preparing an ethylene-propylene random copolymer (B) having an intrinsic viscosity of 9.5 dl/g or lower as measured in tetralin at 135° C. which is different from that of said ethylene-propylene random copolymer (A) and an ethylene content of 40 to 90% by weight, the proportion of said ethylene-propylene random copolymer (A) in the total amount of said ethylenepropylene random copolymers (A) and (B) being adjusted to 4 to 30% by weight and the first step being carried out always at first but the order of the second step and the third step being interexchangeable.
Claim 2
Dependent Claim 224 words
In a process for producing a modified polypropylene having an ethylene content of 5 to 20% by weight, by copolymerizing propylene with ethylene in the presence of a stereospecific catalyst comprising an organoaluminum compound component and a transition metal halide component, the improvement of the process which comprises a first step of carrying out polymerization so as to give a propylene polymer corresponding to 75 to 90% by weight based on the weight of a final modified polypropylene and having an ethylene content of 2% by weight or less; a second step of preparing an ethylene-propylene random copolymer (A) having an intrinsic viscosity of 12 dl/g or higher as measured in tetralin at 135° C. and an ethylene content of 50 to 95% by weight; and a third step of preparing an ethylene-propylene random copolymer (B) having an intrinsic viscosity of 9.5 dl/g or lower as measured in tetralin at 135° C. which is different from that of said ethylene-propylene random copolymer (A) and an ethylene content of 40 to 90% by weight, the proportion of said ethylene-propylene random copolymer (A) in the total amount of said ethylenepropylene random copolymers (A) and (B) being adjusted to 4 to 30% by weight and the first step being carried out always at first but the order of the second step and the third step being interexchangeable.
Claim 3
Dependent Claim 28 words
The improvement according to claim 1 wherein said ethylene-propylene random copolymer (B) has an intrinsic viscosity of 9.0 dl/g or lower as measured in tetralin at 135° C.
Claim 4
Dependent Claim 22 words
The improvement according to claim 1 wherein said ethylene-propylene random copolymer (A) has an ethylene content of 70 to 90% by weight.
Claim 5
Dependent Claim 19 words
The improvement according to claim 1 said ethylene-propylene random copolymer (B) has an ethylene content of 50-85% by weight.
Claim 6
Dependent Claim 22 words
The improvement according to claim 1 wherein said finally obtained modified polypropylene has an ethylene content of 8 to 15% by weight.

References Cited (Backward Citations)

US3480696A Cited
US3670053A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1984-01-13 1984-07-14 1985-01-13 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1988-01-13 1988-07-14 1989-01-13 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1992-01-13 1992-07-14 1993-01-13 $7700.00 Window Closed / Lapsed

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