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US4489195A Expired / Lapsed US ⏱️ 0.0 years remaining

Process for producing thermoplastic olefinic elastomer

Assignee: Resonac Holdings Corp
•
Filing: 1983-01-31
•
Granted: 1984-12-18
•
Expires: 2003-01-31
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Abstract

Abstract A process for producing a thermoplastic elastomer in the presence of a Ziegler catalyst which comprises a first step of forming polypropylene and then a second step of forming an ethylene/propylene random copolymer, characterized in that (a) the catalyst is used such that the total amount of the polymer formed is at least 50 kg per gram of titanium metal in the catalyst, (b) a hydrocarbon having 3 or 4 carbon atoms is used as a slurry polymerization solvent, (c) the solvent phase of the slurry is evaporated and separated without bringing the resulting polymer into contact with alcohols and/or hydrocarbons having at least 5 carbon atoms, (d) the polymerization temperature in the second step is adjusted to not more than 50° C., and (e) in the first step, polypropylene is formed in an amount of 5 to 50% by weight based on the total weight of the elastomer, and in the second step, the ethylene/propylene random copolymer having a propylene content of 5 to 60% based on the weight of the ethylene/propylene random copolymer and an intrinsic viscosity at 135° C. in decalin of 1.5 to 15 is formed in an amount of 50 to 95% by weight based on the total weight of the elastomer.

Inventors

  • 👤 Shigeru Saeda
  • 👤 Zenichiro Izumi

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-10-30 14:50
CPC Classifications
C; C08; C08F; C08F297/00; C08F297/06; C08F297/08; C08F297/083

Claims Analysis

Total Claims: 4
Claim 1
Independent Claim 237 words
A process for producing a thermoplastic elastomer by a slurry polymerization technique in the presence of a Ziegler catalyst, which comprises a first step of forming polypropylene and then a second step of forming an ethylene/propylene random copolymer, wherein (a) the catalyst is composed of (1) a solid component containing titanium, magnesium and chlorine and (2) an organoaluminum compound, with or without (3) a third component, and the catalyst is used such that the total amount of the elastomer formed is at least 50 kg per gram of the titanium metal in the catalyst, (b) propylene is used as a slurry polymerization solvent as well as a starting material, (c) the solvent phase of the slurry is evaporated and separated without bringing the resulting elastomer into contact with alcohols and/or hydrocarbons having at least 5 carbon atoms, (d) the polymerization temperature in the second step is adjusted to not more than 50° C., and (e) in the first step, polypropylene is formed in an amount of 5 to 38.3% by weight based on the total weight of the elastomer, and in the second step, the ethylene/propylene random copolymer having a propylene content of 5 to 60% based on the weight of the ethylene/propylene random copolymer and an intrinsic viscosity at 135° C. in decalin of 1.5 to 15 is formed in an amount of 61.7 to 95% by weight based on the total weight of the elastomer.
Claim 2
Dependent Claim 237 words
A process for producing a thermoplastic elastomer by a slurry polymerization technique in the presence of a Ziegler catalyst, which comprises a first step of forming polypropylene and then a second step of forming an ethylene/propylene random copolymer, wherein (a) the catalyst is composed of (1) a solid component containing titanium, magnesium and chlorine and (2) an organoaluminum compound, with or without (3) a third component, and the catalyst is used such that the total amount of the elastomer formed is at least 50 kg per gram of the titanium metal in the catalyst, (b) propylene is used as a slurry polymerization solvent as well as a starting material, (c) the solvent phase of the slurry is evaporated and separated without bringing the resulting elastomer into contact with alcohols and/or hydrocarbons having at least 5 carbon atoms, (d) the polymerization temperature in the second step is adjusted to not more than 50° C., and (e) in the first step, polypropylene is formed in an amount of 5 to 38.3% by weight based on the total weight of the elastomer, and in the second step, the ethylene/propylene random copolymer having a propylene content of 5 to 60% based on the weight of the ethylene/propylene random copolymer and an intrinsic viscosity at 135° C. in decalin of 1.5 to 15 is formed in an amount of 61.7 to 95% by weight based on the total weight of the elastomer.
Claim 3
Dependent Claim 47 words
A process according to claim 1, wherein the polypropylene formed in the first step rises to the surface of the ethylene/propylene random copolymer formed in the second step so as to maintain a microscopic dispersion of the polypropylene and random copolymer in each other during the polymerization.
Claim 4
Dependent Claim 30 words
A process for producing a thermoplastic elastomer which comprises crosslinking the polymerization product obtained by the process of claim 1 with a crosslinking agent composed mainly of an organic peroxide.

References Cited (Backward Citations)

US3358056A Cited
US4284739A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1987-12-18 1988-06-18 1988-12-18 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1991-12-18 1992-06-18 1992-12-18 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1995-12-18 1996-06-18 1996-12-18 $7700.00 Window Closed / Lapsed

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