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US4066718A Expired / Lapsed US ⏱️ 0.0 years remaining

Process for the production of ethylene-propylene block copolymers

Assignee: Sumitomo Chemical Co Ltd
•
Filing: 1976-10-08
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Granted: 1978-01-03
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Expires: 1996-10-08
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Abstract

Abstract A method for the continuous production of crystalline ethylene-propylene block copolymers containing propylene as the major component and having excellent physical properties as that by a batch process in a slurry-phase by homopolymerizing propylene and then copolymerizing ethylene and propylene in the presence of an inert hydrocarbon solvent and a stereoregular polymerization catalyst in polymerization vessels connected in series, which is characterized by homopolymerizing propylene in three polymerization vessels, wherein the inner pressure of the vessels is decreased in order so as to make the inner-pressure difference between each consecutive two vessels from 1 to 3 kg/cm 2 , and then copolymerizing ethylene and propylene in at least two polymerization vessels, the resulting slurry being transferred from one vessel to the next vessel by the inner-pressure difference between the vessels without using a transferring pump in the homopolymerization step and being pressure-transferred to at least one vessel by using a transferring pump for raising the pressure in the copolymerization step.

Inventors

  • 👤 Shinichi Saito
  • 👤 Asaya Okaue
  • 👤 Kazuo Baba
  • 👤 Shigeo Tanaka

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-10-29 01:34
CPC Classifications
C; C08; C08F; C08F297/00; C08F297/06; C08F297/08; C08F297/083; Y; Y02; Y02E; Y02E30/00; Y02E30/10

Claims Analysis

Total Claims: 6
Claim 1
Independent Claim 137 words
A method for the continuous production of crystalline ethylene-propylene block copolymers containing propylene as the major component in a slurry-phase by homopolymerizing propylene and then copolymerizing ethylene and propylene in the presence of an inert hydrocarbon solvent and a stereoregular polymerization catalyst in polymerization vessels connected in series, which comprises hompolymerizing propylene in three polymerization vessels, wherein the inner pressure of the vessels is decreased in order to make the inner-pressure difference between each consecutive two vessels from 1 to 3 kg/cm 2 , and then copolymerizing ethylene and propylene in at least two polymerization vessels, the resulting slurry being transferred from one vessel to the next vessel by the inner-pressure difference between the vessels in the homopolymerization step and being pressure-transferred by means of a slurry pump to at least one vessel in the copolymerization step.
Claim 2
Independent Claim 137 words
A method for the continuous production of crystalline ethylene-propylene block copolymers containing propylene as the major component in a slurry-phase by homopolymerizing propylene and then copolymerizing ethylene and propylene in the presence of an inert hydrocarbon solvent and a stereoregular polymerization catalyst in polymerization vessels connected in series, which comprises hompolymerizing propylene in three polymerization vessels, wherein the inner pressure of the vessels is decreased in order to make the inner-pressure difference between each consecutive two vessels from 1 to 3 kg/cm 2 , and then copolymerizing ethylene and propylene in at least two polymerization vessels, the resulting slurry being transferred from one vessel to the next vessel by the inner-pressure difference between the vessels in the homopolymerization step and being pressure-transferred by means of a slurry pump to at least one vessel in the copolymerization step.
Claim 3
Dependent Claim 21 words
The method according to claim 1, wherein said inner-pressure difference between the homopolymerization vessels is 1.5 to 2.5 kg/cm 2 .
Claim 4
Dependent Claim 20 words
The method according to claim 1, wherein the pressure in the first vessel is 11.5 to 5.5 kg/cm 2 (gauge).
Claim 5
Dependent Claim 26 words
The method according to claim 1, wherein the resulting slurry in the fourth vessel is pressure-transferred by means of a slurry pump to the fifth vessel.
Claim 6
Dependent Claim 47 words
The method according to claim 1, wherein the pressure in one vessel, to which the slurry is pressure-transferred by means of a slurry pump from the other vessel, is kept under a pressure of -0.5 to 5 kg/cm 2 higher than the pressure in the other vessel.

References Cited (Backward Citations)

US3378607A Cited
US3629368A Cited
US3401212A Cited
US3525781A Cited
US3514501A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1981-01-02 1981-07-04 1982-01-03 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1985-01-02 1985-07-04 1986-01-03 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1989-01-02 1989-07-04 1990-01-03 $7700.00 Window Closed / Lapsed

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