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US4350657A Expired / Lapsed US ⏱️ 0.0 years remaining

Low-energy extruder-pump system

Assignee: Union Carbide Corp
•
Filing: 1980-11-04
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Granted: 1982-09-21
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Expires: 2000-11-04
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Abstract

Abstract Method and apparatus are disclosed for the low energy melting, extrusion and pumping of material comprising feeding, metering, melting and mixing of such materials in an extruder having a melter screw and subsequently passing the resultant extrudate, through breaker plate and adapter means, to and through a rotary gear pump and, in turn, to a die member.

Inventors

  • 👤 David N. Jones
  • 👤 Archibald L Burnett
  • 👤 John C. Miller

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-10-24 05:32
CPC Classifications
B; B29; B29C; B29C48/00; B29C48/25; B29C48/36; B29C48/50; B29C48/505; B29C48/64; B29C48/645; B29C48/365; B29C48/37; B29C48/375; B29C48/387; B29C48/395; B29C48/397; B29C48/56; B29C48/03

Claims Analysis

Total Claims: 12
Claim 1
Independent Claim 149 words
A double-flighted melter screw for use in an extruder in combination with a gear pump to form a melting and pumping system, said melter screw successively having an inlet feeding section, a transition section, a metering section and a mixing section at the downstream end of said screw, each of said feeding, transition and metering sections having a substantially equal outer diameter, thread width and lead, high thread pitch in the feeding, transition and metering sections, decreasing root depth of the threads of said transition section between relatively deep root depth in said feeding section to relatively shallow root depth in said metering section; said 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 effecting substantially complete, final melting and mixing and complete homogenization of the material before discharge from the extruder.
Claim 2
Dependent Claim 149 words
A double-flighted melter screw for use in an extruder in combination with a gear pump to form a melting and pumping system, said melter screw successively having an inlet feeding section, a transition section, a metering section and a mixing section at the downstream end of said screw, each of said feeding, transition and metering sections having a substantially equal outer diameter, thread width and lead, high thread pitch in the feeding, transition and metering sections, decreasing root depth of the threads of said transition section between relatively deep root depth in said feeding section to relatively shallow root depth in said metering section; said 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 effecting substantially complete, final melting and mixing and complete homogenization of the material before discharge from the extruder.
Claim 3
Dependent Claim 55 words
A melting and pumping system comprising a melting extruder having an outer housing member enclosing a melter screw in accordance with claim 1, and discharging, through a breaker plate and an upstream adapter member, to the inlet of a rotary gear pump which, in turn, discharges, through a downstream adapter member, to a die member.
Claim 4
Dependent Claim 58 words
A melting and pumping system comprising a melting extruder in accordance with claim 2, and discharging, through a breaker plate and an upstream adapter member having a decreasing diameter in the downstream direction, to the inlet of a rotary gear pump which, in turn, discharges, through a downstream adapter member of substantially constant diameter, to a die member.
Claim 5
Independent Claim 179 words
A method for the extrusion of synthetic thermoplastic materials comprising passing such materials continuously to and through a rotary extruder having a successive feeding, transition, metering and mixing section; the extruder screw forming the feeding, transition and metering sections, in cooperation with the cylindrical interior of the outer extruder housing, having equal outer diameter, thread width and lead, high thread pitch in the feeding, transition and metering sections, decreasing root depth of the threads of said transition section between relatively deep root depth in said feeding section to relatively shallow root depth in said metering section, said 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, final melting and mixing and complete homogenization of the material before discharge from the extruder; and wherein the extrudate from said extruder is successively passed through a breaker plate and an upstream adapter member, to the inlet of a rotary gear pump which, in turn, discharges, through a downstream adapter member, to a die.
Claim 6
Independent Claim 179 words
A method for the extrusion of synthetic thermoplastic materials comprising passing such materials continuously to and through a rotary extruder having a successive feeding, transition, metering and mixing section; the extruder screw forming the feeding, transition and metering sections, in cooperation with the cylindrical interior of the outer extruder housing, having equal outer diameter, thread width and lead, high thread pitch in the feeding, transition and metering sections, decreasing root depth of the threads of said transition section between relatively deep root depth in said feeding section to relatively shallow root depth in said metering section, said 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, final melting and mixing and complete homogenization of the material before discharge from the extruder; and wherein the extrudate from said extruder is successively passed through a breaker plate and an upstream adapter member, to the inlet of a rotary gear pump which, in turn, discharges, through a downstream adapter member, to a die.
Claim 7
Dependent Claim 190 words
A double-flighted melter screw for use in an extruder in combination with a gear pump to form a melting and pumping system, said melter screw successively having an inlet feeding section, a transition section, a metering section and a mixing section at the downstream end thereof, each of said feeding, transition and metering sections having an equal outer diameter, thread width and lead, high thread pitch in the feeding, transition and metering sections, decreasing root depth of the threads of said transition section between relatively deep root depth in said feeding section to relatively shallow root depth in said metering section; said mixing section having a plurality of groove means arranged to extend substantially longitudinally in the surface thereof, said groove means open at the upstream ends and closed at the downstream ends, hollow internal passage means positioned axially within said mixing section over a substantial portion of its terminal length, and a plurality of radial inlet conduits communicating between said internal passage means and the exterior of said mixing section, said inlet conduits being positioned between a pair of lands which are positioned, in turn, between said groove means.
Claim 8
Dependent Claim 190 words
A double-flighted melter screw for use in an extruder in combination with a gear pump to form a melting and pumping system, said melter screw successively having an inlet feeding section, a transition section, a metering section and a mixing section at the downstream end thereof, each of said feeding, transition and metering sections having an equal outer diameter, thread width and lead, high thread pitch in the feeding, transition and metering sections, decreasing root depth of the threads of said transition section between relatively deep root depth in said feeding section to relatively shallow root depth in said metering section; said mixing section having a plurality of groove means arranged to extend substantially longitudinally in the surface thereof, said groove means open at the upstream ends and closed at the downstream ends, hollow internal passage means positioned axially within said mixing section over a substantial portion of its terminal length, and a plurality of radial inlet conduits communicating between said internal passage means and the exterior of said mixing section, said inlet conduits being positioned between a pair of lands which are positioned, in turn, between said groove means.
Claim 9
Dependent Claim 55 words
A melting and pumping system comprising a melting extruder having an outer housing member enclosing a melter screw in accordance with claim 5, and discharging, through a breaker plate and an upstream adapter member, to the inlet of a rotary gear pump which, in turn, discharges, through a downstream adapter member, to a die member.
Claim 10
Dependent Claim 58 words
A melting and pumping system comprising a melting extruder in accordance with claim 6, and discharging, through a breaker plate and an upstream adapter member having a decreasing diameter in the downstream direction, to the inlet of a rotary gear pump which, in turn, discharges, through a downstream adapter member of substantially constant diameter, to a die member.
Claim 11
Independent Claim 214 words
A method for the extrusion of synthetic thermoplastic materials comprising passing such materials continuously to and through a rotary extruder having a successive feeding, transition, metering and mixing section; the extruder screw forming the feeding, transition and metering sections, in cooperation with the cylindrical interior of the outer extruder housing, having equal outer diameter, thread width and lead, decreasing root depth of the threads of said transition section between relatively deep root depth in said feeding section to relatively shallow root depths in said metering section, said mixing section having a plurality of groove means arranged to extend substantially longitudinally in the surface thereof, said groove means open at the upstream ends and closed at the downstream ends, hollow internal passage means positioned axially within said mixing section over a substantial portion of its terminal length, and a plurality of radial inlet conduits communicating between said internal passage means and the exterior of said mixing section, said inlet conduits being positioned between a pair of lands which are positioned, in turn, between said groove means; and wherein the extrudate from said extruder is successively passed through a breaker plate and an upstream adapter member, to the inlet of a rotary gear pump which, in turn, discharges, through a downstream adapter member, to a die.
Claim 12
Independent Claim 214 words
A method for the extrusion of synthetic thermoplastic materials comprising passing such materials continuously to and through a rotary extruder having a successive feeding, transition, metering and mixing section; the extruder screw forming the feeding, transition and metering sections, in cooperation with the cylindrical interior of the outer extruder housing, having equal outer diameter, thread width and lead, decreasing root depth of the threads of said transition section between relatively deep root depth in said feeding section to relatively shallow root depths in said metering section, said mixing section having a plurality of groove means arranged to extend substantially longitudinally in the surface thereof, said groove means open at the upstream ends and closed at the downstream ends, hollow internal passage means positioned axially within said mixing section over a substantial portion of its terminal length, and a plurality of radial inlet conduits communicating between said internal passage means and the exterior of said mixing section, said inlet conduits being positioned between a pair of lands which are positioned, in turn, between said groove means; and wherein the extrudate from said extruder is successively passed through a breaker plate and an upstream adapter member, to the inlet of a rotary gear pump which, in turn, discharges, through a downstream adapter member, to a die.

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1985-09-20 1986-03-22 1986-09-21 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1989-09-20 1990-03-22 1990-09-21 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1993-09-20 1994-03-22 1994-09-21 $7700.00 Window Closed / Lapsed

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