Apparatus for employing a high percentage of reground thermoplastic scrap resin in an extruder

Claim 2

A thermoplastic resin extruder apparatus which permits the use of high amounts of fluffy scrap resin to be employed without resin starvation of the extruder die, which apparatus comprises: a. a thermoplastic resin extruder which comprises i. an extruder barrel, ii. an extruder die at one end of the extruder for the extrusion of a resin product, iii. a lead screw in the barrel for movement of thermoplastic resin material through the barrel to the extruder die, iv. a first feed inlet in the barrel for the introduction of a fluffy low-density scrap resin into the barrel and compression of the fluffy resin in the barrel by the lead screw, v. a second feed inlet in the barrel for the introduction of a granular high-density resin into the barrel, the second feed inlet downstream of the first feed inlet by at least one lead screw length, and generally adjacent and close to the first feed inlet along the barrel, vi. the first feed inlet larger in inlet area than the second feed inlet, and vii. a heated extruder section downstream of the second feed inlet to heat the thermoplastic resin prior to the extrusion of the heated resin in the extruder die; b. a means upstream of said extruder barrel to grind a scrap thermoplastic resin onto a low-density fluffy scrap resin; c. a first feed hopper operable to contain the fluffy scrap resin and having an open throat area at the lower portion thereof communicating directly with the first feed inlet, the hopper free of any screw conveyor for the fluffy resin therein, whereby fluffy resin in the first feed hopper is introduced by gravity or low pressure into the first feed inlet and compressed in part by the lead screw prior to the second feed inlet; d. means operatively associated with said grinding means to convey the fluffy scrap resin from the grinding means to the first feed hopper; and e. an auxiliary feed hopper operable to contain a granular high-density thermoplastic resin, and having an open throat area which communicates with the second feed inlet, whereby, on occasional plugging of the first feed inlet by the fluffy resin, granular resin is fed by gravity from the auxiliary hopper to the barrel through the second feed inlet, preventing resin starvation of the extruder die.

Claim 3

The apparatus of claim 1 wherein the extruder die is a tubular-forming extruder die to form a tubular product for conversion into film.

Claim 4

The apparatus of claim 1 wherein the area of the first feed inlet and the throat area of the first feed hopper are from about two to six times the area of the second feed inlet.

Claim 5

The apparatus of claim 1 wherein the second feed inlet is positioned downstream from one to three screw lengths of the first feed inlet.

Claim 6

The apparatus of claim 1 wherein the means to convey the fluffy scrap resin comprises an air blower and conveyor tube, whereby fluffy resin from the grinding means is conveyed by air through the conveyor tube to the first feed hopper.

Claim 7

The apparatus of claim 1 wherein the means to grind the scrap resin comprises a film-grinding means, whereby salvageable resin film is ground into a low-density fluffy scrap resin.

Claim 8

The apparatus of claim 1 which includes a means operatively associated with said grinding means to admix high-density granular resin with the fluffy scrap resin from the grinding means prior to introduction of the admixture into the first feed hopper.

Claim 9

A thermoplastic resin extruder apparatus which permits the use of high amoints of fluffy scrap resin to be employed without resin starvation of the extruder die, which apparatus comprises: a. a thermoplastic resin extruder which comprises i. an extruder barrel, ii. an extruder die at one end of the extruder for the extrusion of a tubular resin product, iii. a lead screw in the barrel for movement of thermoplastic resin material through the barrel to the extruder die, iv. a first feed inlet in the barrel for the introduction of a fluffy low-density scrap resin into the barrel and compression of the fluffy resin in the barrel by the lead screw, v. a second feed inlet in the barrel for the introduction of a granular high-density resin into the barrel, the second feed inlet downstream of the first feed inlet by from about one to three lead screw lengths, vi. the first feed inlet about two to six times larger in inlet area then the second feed inlet, and vii. a heated extruder section downstream of the second feed inlet to heat the thermoplastic resin prior to the extrusion of the heated resin in the extruder die; b. a means up-stream of said extruder barrel to grind scrap thermoplastic resin film into a low-density fluffy scrap resin; c. a first cyclone-type feed hopper operable to contain the fluffy scrap resin and having an open throat area at the lower portion thereof communicating directly with the first feed inlet, the hopper free of any screw conveyor for the fluffy resin therein, whereby fluffy resin in the first feed hopper is introduced by gravity or low pressure into the first feed inlet and compressed in part by the lead screw prior to the second feed inlet; d. means operatively associated with said grinding means to convey the fluffy scrap resin by air from the grinding means to the first feed hopper which includes an air blower and conveyer tube; e. a means operatively associated with said grinding means to admix high-density granular resin with the fluffy scrap resin from the grinding means prior to introduction of the admixture into the first feed hopper; and f. an auxiliary cyclone-type feed hopper operable to contain a granular high-density thermoplastic resin, and having an open throat area which communicates with the second feed inlet, whereby, on occasional plugging of the first feed inlet by the fluffy resin, granular resin is fed by gravity from the auxiliary hopper to the barrel through the second feed inlet, preventing resin starvation of the extruder die.

Claim 10

A thermoplastic resin extruder apparatus which permits the use of high amoints of fluffy scrap resin to be employed without resin starvation of the extruder die, which apparatus comprises: a. a thermoplastic resin extruder which comprises i. an extruder barrel, ii. an extruder die at one end of the extruder for the extrusion of a tubular resin product, iii. a lead screw in the barrel for movement of thermoplastic resin material through the barrel to the extruder die, iv. a first feed inlet in the barrel for the introduction of a fluffy low-density scrap resin into the barrel and compression of the fluffy resin in the barrel by the lead screw, v. a second feed inlet in the barrel for the introduction of a granular high-density resin into the barrel, the second feed inlet downstream of the first feed inlet by from about one to three lead screw lengths, vi. the first feed inlet about two to six times larger in inlet area then the second feed inlet, and vii. a heated extruder section downstream of the second feed inlet to heat the thermoplastic resin prior to the extrusion of the heated resin in the extruder die; b. a means up-stream of said extruder barrel to grind scrap thermoplastic resin film into a low-density fluffy scrap resin; c. a first cyclone-type feed hopper operable to contain the fluffy scrap resin and having an open throat area at the lower portion thereof communicating directly with the first feed inlet, the hopper free of any screw conveyor for the fluffy resin therein, whereby fluffy resin in the first feed hopper is introduced by gravity or low pressure into the first feed inlet and compressed in part by the lead screw prior to the second feed inlet; d. means operatively associated with said grinding means to convey the fluffy scrap resin by air from the grinding means to the first feed hopper which includes an air blower and conveyer tube; e. a means operatively associated with said grinding means to admix high-density granular resin with the fluffy scrap resin from the grinding means prior to introduction of the admixture into the first feed hopper; and f. an auxiliary cyclone-type feed hopper operable to contain a granular high-density thermoplastic resin, and having an open throat area which communicates with the second feed inlet, whereby, on occasional plugging of the first feed inlet by the fluffy resin, granular resin is fed by gravity from the auxiliary hopper to the barrel through the second feed inlet, preventing resin starvation of the extruder die.