US4788265A
Expired / Lapsed
US
⏱️ 0.0 years remaining
Preparation of copolmers of ethylene with acrylic acid esters in a tubular reactor at above 500 bar
Assignee: BASF SE
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Filing: 1987-04-22
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Granted: 1988-11-29
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Expires: 2007-04-22
Abstract
Abstract Copolymers of ethylene with acrylates or solutions of free acrylic acid in acrylates are prepared in a continuously operated tubular polymerization system at high pressures and temperatures by feeding a mixture of ethylene, acrylate, initiator and, if appropriate, regulant into the polymerization system in the form of a main stream at the inlet point thereof and at the same time through two or more secondary streams, secondary streams (I) being metered in at points where the reaction temperature has just exceeded a maximum temperature due to the heat of polymerization and secondary streams (II) at points which, relative to the direction of flow of the ethylene, are upstream of the feed points of secondary streams (I) and upstream of the respective maximum temperature.
Inventors
- 👤 Klaus Pfleger
- 👤 Klaus Boettcher
- 👤 Oskar Buechner
- 👤 Friedrich Kanne
- 👤 Siegfried Kursawe
- 👤 Wieland Zacher
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-11-04 10:24
CPC Classifications
C; C08; C08F; C08F210/00; C08F210/02
Claims Analysis
Total Claims: 6
Claim 1
Independent Claim
223 words
A process for preparing a copolymer of ethylene with an acrylic acid ester by copolymerizing 100 parts by weight of ethylene with from 0.1 to 25.0 parts by weight of an acrylic acid ester or of a solution of free acrylic acid in an acrylic acid ester in a continuously operated tubular polymerization reactor at pressures of from 500 to 5,000 bar and at temperatures of from 50° to 450° C. in the presence of a polymerization initiator which decomposes into free radicals which process further comprises: feeding a mixture of ethylene, comonomer and initiator into the tubular polymerization reactor in the form of a main stream at the inlet point of the reactor; passing said mixture along said reactor where the ethylene and comonomer polymerize to form a copolymer; feeding into the reactor an additional amount of said mixtures in one or more secondary streams(I) at a point or points where a maximum temperature is reached in the reactor due to the heat of polymerization, and feeding a further amount of said mixture into the reactor in one or more secondary streams(II) at a point or points which, relative to the direction of flow of the ehtylene, are positioned upstream of the feed points of secondary streams(I) and upstream of the points at which a maximum temperature is reached in the reactor.
Claim 2
Dependent Claim
223 words
A process for preparing a copolymer of ethylene with an acrylic acid ester by copolymerizing 100 parts by weight of ethylene with from 0.1 to 25.0 parts by weight of an acrylic acid ester or of a solution of free acrylic acid in an acrylic acid ester in a continuously operated tubular polymerization reactor at pressures of from 500 to 5,000 bar and at temperatures of from 50° to 450° C. in the presence of a polymerization initiator which decomposes into free radicals which process further comprises: feeding a mixture of ethylene, comonomer and initiator into the tubular polymerization reactor in the form of a main stream at the inlet point of the reactor; passing said mixture along said reactor where the ethylene and comonomer polymerize to form a copolymer; feeding into the reactor an additional amount of said mixtures in one or more secondary streams(I) at a point or points where a maximum temperature is reached in the reactor due to the heat of polymerization, and feeding a further amount of said mixture into the reactor in one or more secondary streams(II) at a point or points which, relative to the direction of flow of the ehtylene, are positioned upstream of the feed points of secondary streams(I) and upstream of the points at which a maximum temperature is reached in the reactor.
Claim 3
Dependent Claim
35 words
The process of claim 1, wherein a secondary stream (I) is fed in at a point where a maximum temperature is reached and a secondary stream (II) is fed in upstream of this maximum temperature.
Claim 4
Dependent Claim
52 words
The process of claim 1, wherein secondary stream (I) is fed in at a point where the reaction mixture has a temperature of from 290° to 310° C. and secondary stream (II) is fed in at a point upstream thereof where the reaction mixture is cooler by from 30° to 60° C.
Claim 5
Dependent Claim
23 words
The process of claim 1, wherein the amount of comonomer required for copolymerization is predominantly fed in through secondary streams (I) and (II).
Claim 6
Dependent Claim
13 words
The process of claim 1, wherein the mixture further contains a polymerization regulant.
References Cited (Backward Citations)
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US4042767A
Cited
US4076919A
Cited
US4135044A
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USPTO Annuity & Maintenance Windows
| Annuity Stage | Window Opens | Payment Deadline | Surcharge Period Until | Estimated Fee | Status |
|---|---|---|---|---|---|
| 3.5 Years (Year 4) | 1991-11-29 | 1992-05-30 | 1992-11-29 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1995-11-29 | 1996-05-30 | 1996-11-29 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1999-11-29 | 2000-05-30 | 2000-11-29 | $7700.00 | Window Closed / Lapsed |