US4461734A
Expired / Lapsed
US
⏱️ 0.0 years remaining
Process for plasticization and pumping of low bulk density plastics
Assignee: Union Carbide Corp
•
Filing: 1982-09-13
•
Granted: 1984-07-24
•
Expires: 2002-09-13
Abstract
Abstract Process for the plasticization and pumping of low bulk density synthetic thermoplastic materials through extrusion die means employing a mixer type extruder, the extrudate from said extruder is passed through a rotary melt pump and the molten material is discharged therefrom through a die member.
Inventors
- 👤 David N. Jones
- 👤 Urho S. Haapala
- 👤 Leonard S. Scarola
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-10-30 12:53
CPC Classifications
B; B29; B29C; B29C48/00; B29C48/25; B29C48/36; B29C48/50; B29C48/505; B29C48/63; B29C48/365; B29C48/37; B29C48/375; B29C48/387; B29C48/53; B29C48/56; B29C48/03; B29C48/395; B29C48/40; B29C48/41; Y; Y02; Y02P; Y02P70/00; Y02P70/10; Y10; Y10S; Y10S264/00; Y10S264/911; Y10S264/92
Claims Analysis
Total Claims: 9
Claim 1
Independent Claim
134 words
A process for the plasticization and pumping of low bulk density thermoplastic materials through extrusion die means employing a rotary mixer type extruder, having feeding, transition and metering sections and a melt pump, said feeding section having relatively deeper screw root depth and/or greater screw pitch and/or greater screw length than normally employed, thereby increasing the volumetric throughput rate through the feed section to compensate for said lower bulk density of material being processed and provide a substantially material-filled metering section, wherein the extrudate from said extruder is subsequently passed through an upstream flow channel member to the inlet of a rotary melt pump, which serves to control the material thoughput rate of the process and the molten material is discharged therefrom, through a downstream flow channel member, to and through a die member.
Claim 2
Dependent Claim
134 words
A process for the plasticization and pumping of low bulk density thermoplastic materials through extrusion die means employing a rotary mixer type extruder, having feeding, transition and metering sections and a melt pump, said feeding section having relatively deeper screw root depth and/or greater screw pitch and/or greater screw length than normally employed, thereby increasing the volumetric throughput rate through the feed section to compensate for said lower bulk density of material being processed and provide a substantially material-filled metering section, wherein the extrudate from said extruder is subsequently passed through an upstream flow channel member to the inlet of a rotary melt pump, which serves to control the material thoughput rate of the process and the molten material is discharged therefrom, through a downstream flow channel member, to and through a die member.
Claim 3
Dependent Claim
58 words
The process in accordance with claim 1, wherein said material exiting said metering section is next passed through a mixing section having a plurality of flutes formed by alternate groove and land means arranged to extend substantially longitudinally in the surface thereof and capable of substantially complete melting and mixing of the material before discharge from the extruder.
Claim 4
Dependent Claim
146 words
A process for the plasticization and pumping of low bulk density thermoplastic materials through extrusion die means employing a rotary mixer type extruder having feeding, transition and metering sections and a melt pump, said feeding section having relatively deeper screw root depth and/or greater screw pitch and/or greater screw length than normally employed, thereby increasing the volumetric throughput rate through the feeding section to compensate for said lower bulk density of material being processed and provide a substantially material-filled metering section not alone capable of controlling the material throughput rate of the process, wherein the extrudate from said extruder is subsequently passed through an upstream flow channel member to the inlet of a rotary melt pump which serves to control the material thoughput rate of the process and the molten material is discharged therefrom, through a downstream flow channel member, to and through a die member.
Claim 5
Dependent Claim
146 words
A process for the plasticization and pumping of low bulk density thermoplastic materials through extrusion die means employing a rotary mixer type extruder having feeding, transition and metering sections and a melt pump, said feeding section having relatively deeper screw root depth and/or greater screw pitch and/or greater screw length than normally employed, thereby increasing the volumetric throughput rate through the feeding section to compensate for said lower bulk density of material being processed and provide a substantially material-filled metering section not alone capable of controlling the material throughput rate of the process, wherein the extrudate from said extruder is subsequently passed through an upstream flow channel member to the inlet of a rotary melt pump which serves to control the material thoughput rate of the process and the molten material is discharged therefrom, through a downstream flow channel member, to and through a die member.
Claim 6
Dependent Claim
58 words
The process in accordance with claim 3, wherein said material exiting said metering section is next passed through a mixing section having a plurality of flutes formed by alternate groove and land means arranged to extend substantially longitudinally in the surface thereof and capable of substantially complete melting and mixing of the material before discharge from the extruder.
Claim 7
Dependent Claim
160 words
A process for the plasticization and pumping of low bulk density synthetic thermoplastic materials through extrusion die means employing a rotary mixer type extruder having feeding, transition and metering section and a melt pump, said feeding section having at least one of: up to 40 percent deeper screw root depth, up to 40 percent greater screw pitch and up to 75 percent greater screw length than normally employed, thereby increasing the volumetric throughput rate through the feeding section to compensate for said lower bulk density of material being processed and provide a substantially material-filled metering section not alone capable of controlling the material throughput rate of the process; and wherein the extrudate from said extruder is subsequently passed though an upstream flow channel to the inlet of a rotary melt pump which serves to control the material thoughput rate of the process and the molten material is discharged therefrom, through a downstream flow channel, to and through a die member.
Claim 8
Dependent Claim
160 words
A process for the plasticization and pumping of low bulk density synthetic thermoplastic materials through extrusion die means employing a rotary mixer type extruder having feeding, transition and metering section and a melt pump, said feeding section having at least one of: up to 40 percent deeper screw root depth, up to 40 percent greater screw pitch and up to 75 percent greater screw length than normally employed, thereby increasing the volumetric throughput rate through the feeding section to compensate for said lower bulk density of material being processed and provide a substantially material-filled metering section not alone capable of controlling the material throughput rate of the process; and wherein the extrudate from said extruder is subsequently passed though an upstream flow channel to the inlet of a rotary melt pump which serves to control the material thoughput rate of the process and the molten material is discharged therefrom, through a downstream flow channel, to and through a die member.
Claim 9
Dependent Claim
58 words
The process in accordance with claim 5, wherein said material exiting said metering section is next passed through a mixing section having a plurality of flutes formed by alternate groove and land means arranged to extend substantially longitudinally in the surface thereof and capable of substantially complete melting and mixing of the material before discharge from the extruder.
References Cited (Backward Citations)
US2819493A
Cited
US3078513A
Cited
US3148231A
Cited
US3280425A
Cited
DE1435353A1
Cited
US3309736A
Cited
DE2051568A1
Cited
US3730492A
Cited
US4015828A
Cited
US4013745A
Cited
US4025056A
Cited
US3991153A
Cited
US4032391A
Cited
US4137023A
Cited
DE2703461A1
Cited
JPS5514253A
Cited
US4343755A
Cited
GB2076728A
Cited
US4321229A
Cited
US4350657A
Cited
USPTO Annuity & Maintenance Windows
| Annuity Stage | Window Opens | Payment Deadline | Surcharge Period Until | Estimated Fee | Status |
|---|---|---|---|---|---|
| 3.5 Years (Year 4) | 1987-07-24 | 1988-01-23 | 1988-07-24 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1991-07-24 | 1992-01-23 | 1992-07-24 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1995-07-24 | 1996-01-23 | 1996-07-24 | $7700.00 | Window Closed / Lapsed |