US3956438A
Expired / Lapsed
US
⏱️ 0.0 years remaining
Process for extruding a partially foamed thermoplastic product
Assignee: Oerlikon Barmag AG
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Filing: 1973-10-09
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Granted: 1976-05-11
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Expires: 1993-10-09
Abstract
Abstract Process for producing a partially foamed thermoplastic polymer product in a single screw extruder by dividing an initial melt stream of the polymer into separate partial melt streams conveyed individually by the extruder to a shaping or forming die, uniformly mixing a foaming agent with at least one but not all of the separate and individually conveyed partial melt streams, and then rejoining all of said melt streams in the die in abutting core and shell layers with foaming of at least one but not all of said layers.
Inventors
- 👤 Heinz Schippers
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-10-22 23:33
CPC Classifications
B; B29; B29C; B29C44/00; B29C44/20; B29C44/22; B29C44/02; B29C44/04; B29C44/0461; B29C44/34; B29C44/36; B29C44/46; B29C44/50; B29C44/507; B29C48/00; B29C48/25; B29C48/285; B29C48/29; B29C48/36; B29C48/50; B29C48/74; B29C48/745; B29C45/00; B29C48/022; B29C48/03; B29C48/09; B29K; B29K2105/00; B29K2105/0005; B29K2105/04; B29K2105/043; Y; Y10; Y10S; Y10S264/00; Y10S264/05
Claims Analysis
Total Claims: 4
Claim 1
Independent Claim
178 words
In a process for the production of a partially foamed thermoplastic polymer product having a core and shell layered structure by means of the addition of a foaming agent during continuous extrusion of the polymer with a screw extruder, the improvement which comprises: first melting said thermoplastic polymer free of foaming agent and conveying the resulting melt under compression through a first screw zone of the extruder; dividing said melt free of foaming agent into at least two separate partial melt streams for individual conveyance from said first extrusion zone into a die shaping zone of the extruder; introducing and uniformly mixing the foaming agent into at least one of said separate partial melt streams in a second screw zone of the same extruder while maintaining at least one other of said separate partial melt streams free of said foaming agent during conveyance to said die shaping zone; and recombining the individual melt streams in said die shaping zone while expanding said foaming agent to form abutting foamed and non-foamed extruded layers of the core and shell structure.
Claim 2
Dependent Claim
178 words
In a process for the production of a partially foamed thermoplastic polymer product having a core and shell layered structure by means of the addition of a foaming agent during continuous extrusion of the polymer with a screw extruder, the improvement which comprises: first melting said thermoplastic polymer free of foaming agent and conveying the resulting melt under compression through a first screw zone of the extruder; dividing said melt free of foaming agent into at least two separate partial melt streams for individual conveyance from said first extrusion zone into a die shaping zone of the extruder; introducing and uniformly mixing the foaming agent into at least one of said separate partial melt streams in a second screw zone of the same extruder while maintaining at least one other of said separate partial melt streams free of said foaming agent during conveyance to said die shaping zone; and recombining the individual melt streams in said die shaping zone while expanding said foaming agent to form abutting foamed and non-foamed extruded layers of the core and shell structure.
Claim 3
Dependent Claim
56 words
A process as claimed in claim 1 wherein one of two separate melt streams is branched to flow into a cylinder core and an outer shell layer of the die shaping zone and the other melt stream is directed into an intermediate shell layer of the die shaping zone between said core and outer shell layer.
Claim 4
Dependent Claim
62 words
A process as claimed in claim 2 wherein said core and outer shell layer are maintained substantially free of foaming agent while the intermediate layer is formed by the polymer in admixture with said foaming agent, thereby yielding a solid non-foamed core cylinder surrounded first by an intermediate annular foamed layer which in turn is surrounded by an outer solid non-foamed shell.
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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) | 1979-05-11 | 1979-11-10 | 1980-05-11 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1983-05-11 | 1983-11-10 | 1984-05-11 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1987-05-11 | 1987-11-10 | 1988-05-11 | $7700.00 | Window Closed / Lapsed |