Continuous process and apparatus for manufacturing conductive polymer components

• US 5,849,137 A
• Filed: 03/28/1997
• Issued: 12/15/1998
• Est. Priority Date: 08/15/1995
• Status: Expired due to Fees

• Current Assignee: Bourns, Multifuse (Hong Kong), Ltd.
• Original Assignee: Bourns, Multifuse (Hong Kong), Ltd.
• Inventors: Wiryana, Sidharta, Zhang, Mengruo, Hogge, Steven Darryl
• Primary Examiner(s): STEMMER, DANIEL J
• Application Number:
  US08/828,452
• Time in Patent Office: 627 Days
• Field of Search: 156/500, 156/244.27, 156/244.24, 156/244.22, 156/244.11, 156/351, 156/358, 156/360, 425/141, 425/145, 425/204, 425/114, 425/377
• US Class Current: 156/500
• CPC Class Codes: B29C 2948/92019 Pressure
• CPC Class Codes: B29C 2948/92152 Thickness
• CPC Class Codes: B29C 2948/9238 Feeding, melting, plasticising or pumping zones, e.g. the melt itself
• CPC Class Codes: B29C 2948/92438 Conveying, transporting or storage of articles
• CPC Class Codes: B29C 2948/92466 Auxiliary unit, e.g. for external melt filtering, re-combining or transfer between units
• CPC Class Codes: B29C 2948/926 Flow or feed rate
• CPC Class Codes: B29C 2948/92647 Thickness
• CPC Class Codes: B29C 2948/92828 Raw material handling or dosing, e.g. active hopper or feeding device
• CPC Class Codes: B29C 2948/92952 Drive section, e.g. gearbox, motor or drive fluids
• CPC Class Codes: B29C 48/08 flexible, e.g. films
• CPC Class Codes: B29C 48/37 Gear pumps
• CPC Class Codes: B29C 48/387 using a screw extruder and a gear pump
• CPC Class Codes: B29C 48/40 using two or more parallel screws or at least two parallel non-intermeshing screws, e.g. twin screw extruders
• CPC Class Codes: B29C 48/92 Measuring, controlling or regulating
• CPC Class Codes: B29K 2995/0005 Conductive
• CPC Class Codes: B32B 2309/10 linear, e.g. length, distance, width
• CPC Class Codes: B32B 2309/72 For measuring or regulating, e.g. systems with feedback loops
• CPC Class Codes: B32B 37/153 at least one layer is extruded and immediately laminated while in semi-molten state
• CPC Class Codes: H01C 1/028 the resistive element being embedded in insulation with outer enclosing sheath
• CPC Class Codes: H01C 1/1406 Terminals or electrodes formed on resistive elements having positive temperature coefficient
• CPC Class Codes: H01C 7/027 : consisting of conducting or semi-conducting material dispersed in a non-conductive organic material
• CPC Class Codes: Y10T 29/49083 : Heater type
• CPC Class Codes: Y10T 29/49085 : Thermally variable

Abstract

A direct extrusion process for manufacturing conductive polymer articles of manufacture employs a twin screw compounding extruder that compounds a polymeric mixture from materials received, in predetermined proportions, from gravimetric feeders, then extrudes a compounded conductive polymeric material in the melt phase. The extrudate is then fed into a gear pump that allows the extruder to discharge the compounded material, while it is still in the melt stage, at a relatively low pressure. The gear pump produces a substantially constant volumetric output of the compounded "melt phase" material at sufficiently high pressure for delivery into a sheet die. The sheet die forms the compounded material, while still in the melt phase, into a continuous web. The formed polymeric web, while at a temperature just below the melt temperature of the polymeric material, is fed into a mechanism that laminates a continuous web of conductive metal foil onto each side of the polymeric web, the foil webs being pre-heated to a temperature slightly above the melt temperature of the polymeric material. The continuous web of laminate may then be cut into measured lengths, prior to stamping or punching out the individual components. Uniformity in the conductive polymeric extrudate may be enhanced by controlling the extruder and the feeders through a feedback system using the pump inlet pressure as the control parameter. The thickness of the laminated web may be maintained within desired tolerances by closed loop feedback control of the sheet die and/or the laminating mechanism.

Claims

1. Apparatus for manufacturing an article of manufacture comprising a conductive polymer layer laminated between first and second metallic layers, the apparatus comprising:

a compounding extruder mechanism for making a conductive polymer extrudate in the melt phase from a polymer material and a conductive filler material and for discharging the extrudate at a first pressure and at a controllable extrusion rate, the first pressure being at least partly determined by the extrusion rate;

a feed mechanism for separately and controllably feeding the polymer material and the conductive filler material to the compounding extruder mechanism in predetermined proportions at controllable feed rates;

a die mechanism for forming the extrudate into a continuous conductive polymer web having top and bottom surfaces;

a laminating mechanism for laminating a first continuous metallic foil web onto the top surface of the polymer web and a second metallic foil web onto the bottom surface of the polymer web, thereby forming a continuous laminated web having a polymer layer laminated between first and second metallic layers; and

a pressure control system, responsive to the first pressure, that maintains the first pressure substantially equal to a predetermined set point pressure value, the pressure control system comprising;

a pressure transducer that measures the first pressure and that generates a measured pressure signal having a value indicative of the first pressure;

a microprocessor that is responsive to the measured pressure signal by periodically comparing the value thereof with the set point pressure value, and that generates a pressure difference signal having a value that is proportional to the difference between the value of the measured pressure signal and the set point pressure value; and

a pressure control mechanism, operable on the feed mechanism and the extruder mechanism, that responds to the pressure difference signal by controlling the feed rates and the extrusion rate so as to minimize the absolute value of the pressure difference signal.

2. The apparatus of claim 1, wherein the compounding extruder mechanism discharges the extrudate at a first pressure, and wherein the apparatus further comprises:

a pump fluidly connected between the compounding extruder mechanism and the die mechanism for feeding the extrudate to the die mechanism at a second pressure that is higher than the first pressure.

3. The apparatus of claim 1, wherein the compounding extruder mechanism comprises a twin screw compounding extruder.

4. The apparatus of claim 1, further comprising:

a thickness control system, responsive to the thickness of the laminated web, for maintaining the thickness of the laminated web substantially at a predetermined set point thickness.

5. The apparatus of claim 4, wherein the die mechanism is controllable to vary the thickness of the polymer web, and wherein the thickness control system comprises:

a thickness gauge disposed so as to measure the thickness of the laminated web and to generate a measured thickness signal having a value indicative of the measured thickness thereof;

a microprocessor that is responsive to the measured thickness signal by periodically comparing the value thereof with the set point thickness value, and that generates a thickness difference signal having a value that is proportional to the difference between the value of the measured thickness signal and the set point thickness value; and

a thickness control mechanism, operable on the die mechanism, that responds to the thickness difference signal by controlling the die mechanism so as to minimize the absolute value of the thickness difference signal.

6. The apparatus of claim 4, wherein the laminating mechanism is controllable to vary the thickness of the laminated web, and wherein the thickness control system comprises:

a thickness gauge disposed so as to measure the thickness of the laminated web and to generate a measured thickness signal having a value indicative of the measured thickness thereof;

a microprocessor that is responsive to the measured thickness signal by periodically comparing the value thereof with the set point thickness value, and that generates a thickness difference signal having a value that is proportional to the difference between the value of the measured thickness signal and the set point thickness value; and

a thickness control mechanism, operable on the laminating mechanism, that responds to the thickness difference signal by controlling the laminating mechanism so as to minimize the absolute value of the thickness difference signal.

7. Apparatus for manufacturing an article of manufacture comprising a conductive polymer layer laminated between first and second metallic layers, the apparatus comprising:

a compounding extruder mechanism for making a conductive polymer extrudate in the melt phase from a polymer material and a conductive filler material;

a feed mechanism for separately and controllably feeding the polymer material and the conductive filler material to the compounding extruder mechanism in predetermined proportions;

a die mechanism for forming the extrudate into a continuous conductive polymer web having top and bottom surfaces;

a laminating mechanism for laminating a first continuous metallic foil web onto the top surface of the polymer web and a second metallic foil web onto the bottom surface of the polymer web, thereby forming a continuous laminated web having a polymer layer laminated between first and second metallic layers, the laminating mechanism being controllable to vary the thickness web; and

a thickness control system, responsive to the thickness of the laminated web, for maintaining the thickness of the laminated web substantially at a predetermined set point thickness, the thickness control system comprising;

a thickness gauge that measures the thickness of the laminated of the laminated web and that generates a measured thickness signal having a value indicative of the measured thickness thereof;

a microprocessor that is responsive to the measured thickness signal by periodically comparing the value thereof with the set point thickness value, and that generates a thickness difference signal having a value that is proportional to the difference between the value of the measured thickness signal and the set point thickness value; and

a thickness control mechanism, operable on the laminating mechanism, that responds to the thickness difference signal by controlling the laminating mechanism so as to minimize the absolute value of the thickness difference signal.

8. The apparatus of claim 7, wherein the compounding extruder mechanism discharges the extrudate at a first pressure, the apparatus further comprising:

a pressure control system, responsive to the first pressure, that maintains the first pressure substantially equal to a predetermined set point pressure value.

9. The apparatus of claim 8, wherein the feed mechanism is operable to feed the polymer material and the filler material at controllable feed rates and the compounding extruder mechanism is operable to discharge the extrudate at a controllable extrusion rate, the first pressure being at least partly determined by the extrusion rate, and wherein the pressure control system comprises:

a pressure transducer disposed so as to measure the first pressure and to generate a measured pressure signal having a value indicative of the first pressure;

a microprocessor that is responsive to the measured pressure signal by periodically comparing the value thereof with the set point pressure value, and that generates a pressure difference signal having a value that is proportional to the difference between the value of the measured pressure signal and the set point pressure value; and

a pressure control mechanism, operable on the feed mechanism and the compounding extruder mechanism, that responds to the pressure difference signal by controlling the feed rates and the extrusion rate so as to minimize the absolute value of the pressure difference signal.

10. Apparatus for manufacturing an article of manufacture comprising a conductive polymer layer laminated between first and second metallic layers, the apparatus comprising:

a compounding extruder mechanism for making a conductive polymer extrudate in the melt phase from a polymer material and a conductive filler material and for discharging the extrudate at a first pressure;

a feed mechanism for separately and controllably feeding the polymer material and the conductive filler material to the compounding extruder mechanism in predetermined proportions;

a die mechanism for forming the extrudate into a continuous conductive polymer web having top and bottom surfaces;

a laminating mechanism for laminating a first continuous metallic foil web onto the top surface of the polymer web and a second metallic foil web onto the bottom surface of the polymer web, thereby forming a continuous laminated web having a polymer layer laminated between first and second metallic layers, the laminating mechanism being controllable to vary the thickness of the laminated web;

a pressure control system, responsive to the first pressure, that maintains the first pressure substantially equal to a predetermined set point pressure value; and

a thickness control system, responsive to the thickness of the laminated web, for maintaining the thickness of the laminated web substantially at a predetermined set point thickness, the thickness control system comprising;

a thickness gauge that measures the thickness of the laminated of the laminated web and that generates a measured thickness signal having a value indicative of the measured thickness thereof;

a microprocessor that is responsive to the measured thickness signal by periodically comparing the value thereof with the set point thickness value, and that generates a thickness difference signal having a value that is proportional to the difference between the value of the measured thickness signal and the set point thickness value; and

a thickness control mechanism, operable on the laminating mechanism, that responds to the thickness difference signal by controlling the laminating mechanism so as to minimize the absolute value of the thickness difference signal.