Process for plasticization and pumping of low bulk density plastics

Claim 2

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

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

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

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

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

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 scre ' # 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

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 scre ' # 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

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.