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US3883631A Expired / Lapsed US ⏱️ 0.0 years remaining

Method and means for making high molecular weight polyethylene sheets

Assignee: Impact Plastics Inc
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Filing: 1969-08-21
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Granted: 1975-05-13
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Expires: 1989-08-21
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Abstract

Abstract This information relates to the extrusion of high molecular weight polyethylene having a molecular weight in excess of 1,000,000 and to a method and means for altering the crosssectional dimensions of the extruded sheet.

Inventors

  • 👤 Coyt E Murray

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-10-26 01:47
CPC Classifications
B; B29; B29C; B29C48/00; B29C48/25; B29C48/88; B29C48/90; B29C48/908; B29C48/022; B29C48/03; B29C48/07; B29C48/08; B29C48/78; B29C48/793; B29C48/80; B29C48/83; B29C48/832; B29C48/834; B29C48/875; B29C48/91; B29K; B29K2023/00

Claims Analysis

Total Claims: 20
Claim 1
Independent Claim 184 words
A METHOD OF TRANSFORMING HIGH MOLECULAR WEIGHT POLYETHYLENE HAVING A MOLECULAR WEIGHT OF AT LEAST 1,000.000 FROM GRANULAR RESIN TO A SOLID STATE WHICH COMPRISE: A. HEATING THE RESIN ABOVE ITS CRYSTALLINE MELTING POINT B. MOVIING THE HEATED RESIN IN ONE DIRECTION THROUGH AN EXTRUDER OF GIVEN CROSS-SECTIONAL INTERNAL DIMENSION WHILE CONFINING THE RESIN AGAINST RADIAL MOVEMENT AND WHILE COOLING THE RESIN TO AN AMORPHOUS STATE WITHIN THE EXTRUDER, C. MOVING THE AMORPHOUS RESIN IN SAID ONE DIRECTION BEYOND THE EXTRUDER AND ACROSS AN AIR SPACE AND INTO A FINISHING DIE SPACE SUFFICIENTLY CLOSE TO THE EXTRUDER TO ENGAGE THE RESIN IN ITS AMORPHOUS CONDITION AND SPACED BEYOND THE EXTRUDER A DISTANCE SUFFICIENT TO PERMIT FORMATION OF A RESERVOIR OF RESIN IN THE AIR SPACE BETWEEN THE EXTRUDER AND THE FINISHING DIE, D. APPLYING INWARD PRESSURE ON THE AMORPHOUS RESIN AT THE FINISHING DIE SUFFICIENT TO EXERT A BACK PRESSURE ON THE AMORPHOUS RESIN IN THE OPPOSITE DIRECTION TO SAID ONE DIRECTION AND CREATE A RESERVIOR IN THE SPACE BETWEEN THE FINISHING DIE AND THE EXTRUDER OF GREATER CROSS-SECTIONAL DIMENSION THAN SAID GIVEN DIMENSION.
Claim 2
Independent Claim 184 words
A METHOD OF TRANSFORMING HIGH MOLECULAR WEIGHT POLYETHYLENE HAVING A MOLECULAR WEIGHT OF AT LEAST 1,000.000 FROM GRANULAR RESIN TO A SOLID STATE WHICH COMPRISE: A. HEATING THE RESIN ABOVE ITS CRYSTALLINE MELTING POINT B. MOVIING THE HEATED RESIN IN ONE DIRECTION THROUGH AN EXTRUDER OF GIVEN CROSS-SECTIONAL INTERNAL DIMENSION WHILE CONFINING THE RESIN AGAINST RADIAL MOVEMENT AND WHILE COOLING THE RESIN TO AN AMORPHOUS STATE WITHIN THE EXTRUDER, C. MOVING THE AMORPHOUS RESIN IN SAID ONE DIRECTION BEYOND THE EXTRUDER AND ACROSS AN AIR SPACE AND INTO A FINISHING DIE SPACE SUFFICIENTLY CLOSE TO THE EXTRUDER TO ENGAGE THE RESIN IN ITS AMORPHOUS CONDITION AND SPACED BEYOND THE EXTRUDER A DISTANCE SUFFICIENT TO PERMIT FORMATION OF A RESERVOIR OF RESIN IN THE AIR SPACE BETWEEN THE EXTRUDER AND THE FINISHING DIE, D. APPLYING INWARD PRESSURE ON THE AMORPHOUS RESIN AT THE FINISHING DIE SUFFICIENT TO EXERT A BACK PRESSURE ON THE AMORPHOUS RESIN IN THE OPPOSITE DIRECTION TO SAID ONE DIRECTION AND CREATE A RESERVIOR IN THE SPACE BETWEEN THE FINISHING DIE AND THE EXTRUDER OF GREATER CROSS-SECTIONAL DIMENSION THAN SAID GIVEN DIMENSION.
Claim 3
Dependent Claim 33 words
A method of processing high molecular weight polyethylene according to claim 1 which includes the step of relieving the inward pressure at the finishing die while moving the resin in said one direction.
Claim 4
Dependent Claim 233 words
Apparatus for extruding high molecular weight polyethylene having a molecular weight in excess of 1,000,000 comprising a major die having an inlet end and an outlet end, a ram reciprocably mounted for movement within the inlet end of the major die, means for introducing successive charges of granular resin into the inlet end of the major die in advance of the retracted ram, a plurality of thermal zones in said major die and spaced axially along its length, means for heating said thermal zones above the crystalline melting point of the resin, means for imparting intermittent inward movement to said ram to move the resin through said thermal zones and out from the outlet end of the major die, and a finishing die for inducing a back pressure of sufficient magnitude on the extruded resin after it leaves the major die to create a reservoir of extruded resin adjoining the outlet end of the major die and of greater cross-sectional dimension than the internal cross-sectional dimension of the major die, said finishing die being spaced beyond the outlet end of said major die a sufficient distance to provide clearance for said reservoir and spaced sufficiently close to the outlet end of said major die to be engageable with the extruded sheet while in its amorphous state, and said finishing die including a platen on opposite sides of the axis of the major die.
Claim 5
Dependent Claim 233 words
Apparatus for extruding high molecular weight polyethylene having a molecular weight in excess of 1,000,000 comprising a major die having an inlet end and an outlet end, a ram reciprocably mounted for movement within the inlet end of the major die, means for introducing successive charges of granular resin into the inlet end of the major die in advance of the retracted ram, a plurality of thermal zones in said major die and spaced axially along its length, means for heating said thermal zones above the crystalline melting point of the resin, means for imparting intermittent inward movement to said ram to move the resin through said thermal zones and out from the outlet end of the major die, and a finishing die for inducing a back pressure of sufficient magnitude on the extruded resin after it leaves the major die to create a reservoir of extruded resin adjoining the outlet end of the major die and of greater cross-sectional dimension than the internal cross-sectional dimension of the major die, said finishing die being spaced beyond the outlet end of said major die a sufficient distance to provide clearance for said reservoir and spaced sufficiently close to the outlet end of said major die to be engageable with the extruded sheet while in its amorphous state, and said finishing die including a platen on opposite sides of the axis of the major die.
Claim 6
Dependent Claim 45 words
An apparatus for processing high molecular weight polyethylene according to claim 3 wherein means are provided for imparting reciprocable movement to at least one platen of said finishing die transversely of the axis of the major die in synchronization with axial reciprocation of said ram.
Claim 7
Dependent Claim 30 words
Apparatus for processing high molecular weight polyethylene according to claim 3 wherein said finishing die includes means for limiting lateral movement of said extruded sheet under pressure of said platens.
Claim 8
Dependent Claim 29 words
Apparatus according to claim 3 wherein the platens of said finishing die are heated above room temperature but below the crystalline melting point of the high molecular weight polymer.
Claim 9
Dependent Claim 28 words
Apparatus according to claim 2 wherein second pressure means are positioned adjacent said finishing die, said additional pressure means exerting a constant predetermined pressure on the extruded sheet.
Claim 10
Dependent Claim 35 words
Apparatus according to claim 7 which includes sensing means adjacent said reservoir and responsive to an increased size of said reservoir beyond a predetermined point to relieve the pressure on said second pressure actuating means.
Claim 11
Independent Claim 135 words
A method of controlling creepage in the extrusion of high molecular weight polyethylene having a molecular weight in excess of 1,000,000 and having a crystalline melting point of about 289*F. said method comprising steps of heating the resin to over 330*F. within the extruder, cooling the resin while in the extruder to a temperature in the range of 270* to 330*F., extruding the resin while at a temperature within the range of 270* to 330*F., and applying pressure on the extruded resin sheet in a direction transverse to its path of travel at a point spaced outwardly beyond the extruder while continuing to cool the extruded resin sheet, the application of pressure being sufficient to create an unconfined reservoir of resin of increased cross-sectional area between the extruder and said outwardly spaced pressure applying means.
Claim 12
Independent Claim 135 words
A method of controlling creepage in the extrusion of high molecular weight polyethylene having a molecular weight in excess of 1,000,000 and having a crystalline melting point of about 289*F. said method comprising steps of heating the resin to over 330*F. within the extruder, cooling the resin while in the extruder to a temperature in the range of 270* to 330*F., extruding the resin while at a temperature within the range of 270* to 330*F., and applying pressure on the extruded resin sheet in a direction transverse to its path of travel at a point spaced outwardly beyond the extruder while continuing to cool the extruded resin sheet, the application of pressure being sufficient to create an unconfined reservoir of resin of increased cross-sectional area between the extruder and said outwardly spaced pressure applying means.
Claim 13
Dependent Claim 43 words
A method of processing high molecular weight polyethylene according to claim 9 which includes the additional step of altering the cross-sectional dimension of the resin sheet within the extruder while cooling the resIn to a temperature within said range of 270* to 330*F.
Claim 14
Dependent Claim 42 words
A method of processing high molecular weight polymers according to claim 9 which includes the additional step of changing the cross-sectional dimension of the resin sheet after it leaves the extruder and beyond the reservoir while continuing to cool the resin sheet.
Claim 15
Dependent Claim 42 words
A method of processing high molecular weight polyethylene according to claim 10 which includes the additional step of changing the cross-sectional dimension of the resin sheet after it leaves the extruder and beyond the reservoir while continuing to cool the resin sheet.
Claim 16
Dependent Claim 104 words
Apparatus for altering the shape of extruded high molecular weight polymers while in an amorphous state following extrusion, said apparatus comprising a finishing die spaced outwardly from the outlet end of an extruder, said finishing die including a platen on opposite sides of the longitudinal axis of the extruded sheet, a spacer element arranged laterally on each side of the axis of the path of travel of the extruded sheet, each spacer element being of a height equal to the desired height of the extruded sheet, and said spacer elements being spaced apart a distance equal to the desired width of the finished sheet.
Claim 17
Dependent Claim 104 words
Apparatus for altering the shape of extruded high molecular weight polymers while in an amorphous state following extrusion, said apparatus comprising a finishing die spaced outwardly from the outlet end of an extruder, said finishing die including a platen on opposite sides of the longitudinal axis of the extruded sheet, a spacer element arranged laterally on each side of the axis of the path of travel of the extruded sheet, each spacer element being of a height equal to the desired height of the extruded sheet, and said spacer elements being spaced apart a distance equal to the desired width of the finished sheet.
Claim 18
Dependent Claim 41 words
A structure according to claim 13 wherein the height of the spacer elements is less than the corresponding internal dimension of the major die and wherein the distance between the spacer elements is greater than the width of the major die.
Claim 19
Dependent Claim 41 words
A structure according to claim 13 wherein the height of the spacer elements is greater than the corresponding dimension of the major die and wherein the distance between the spacer elements is less than the internal width of the major die.
Claim 20
Dependent Claim 45 words
A structure according to claim 13 wherein an altering die is interposed between the major die and said finishing die, said altering die having vertical and transverse dimensions falling between the corresponding dimensions of the finishing die and the inside dimensions of the major die.

References Cited (Backward Citations)

US3039142A Cited
US3239881A Cited
US3392224A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1978-05-12 1978-11-11 1979-05-13 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1982-05-12 1982-11-11 1983-05-13 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1986-05-12 1986-11-11 1987-05-13 $7700.00 Window Closed / Lapsed

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