Two-step process for preparing positive temperature coefficient polymer materials

• US 6,228,287 B1
• Filed: 09/17/1999
• Issued: 05/08/2001
• Est. Priority Date: 09/25/1998
• Status: Expired due to Fees

• Current Assignee: Bourns Incorporated
• Original Assignee: Bourns Incorporated
• Inventors: Wong, Alex
• Primary Examiner(s): KOPEC, MARK T
• Application Number:
  US09/399,298
• Time in Patent Office: 599 Days
• Field of Search: 252/510, 252/511, 264/40.1
• US Class Current: 252/511
• CPC Class Codes: B29C 2948/92019 Pressure
• CPC Class Codes: B29C 2948/92152 Thickness
• CPC Class Codes: B29C 2948/9259 Angular velocity
• 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 2948/92885 Screw or gear
• CPC Class Codes: B29C 48/405 Intermeshing co-rotating screws
• CPC Class Codes: B29C 48/41 Intermeshing counter-rotating screws
• CPC Class Codes: B29C 48/625 characterised by the ratio of the threaded length of the screw to its outside diameter [L/D ratio]
• CPC Class Codes: B29C 48/92 Measuring, controlling or regulating
• CPC Class Codes: H01B 1/24 the conductive material comprising carbon-silicon compounds, carbon or silicon
• CPC Class Codes: H01C 17/0652 containing carbon or carbides
• CPC Class Codes: H01C 17/06586 composed of organic material
• CPC Class Codes: H01C 17/24 by removing or adding resistive material H01C17/23, H01C17/232, H01C17/235 take precedence

Abstract

Positive temperature coefficient polymer (PTC) materials of high loading with uniformly distributed electrically conductive material are manufactured by first producing an intimate mixture (pre-mix or master batch) of a crystalline polymer (e. g. high density polyethylene) with an electrically conductive filler (e. g. carbon black) in proportions that is less rich in the filler than the final PTC product. The intimate mixture, pre-mix or master batch, is utilized in a subsequent step in a molten liquid form for admixing with more filler material in quantities to produce the desired loading of the filler in the polymer matrix. The resulting the admixture is extruded, shaped and formed by conventional equipment to provide a positive temperature coefficient polymer composition that, when equipped with electrodes, is suitable for forming positive temperature coefficient circuit protecting devices. Positive temperature coefficient polymer composition having electrically conductive filler, usually carbon black in ratios as high as 55 to 60 percent by weight can be obtained by the process.

Claims

1. A process for producing a positive temperature coefficient polymer composition comprising a crystalline polymer and an electrically conductive filler that is present in a predetermined proportion in the composition, the process comprising the steps of:

blending the crystalline polymer with the electrically conductive filler into a first intimate admixture in proportions wherein the electrically conductive filler is

less in the first intimate admixture than the predetermined proportion in the positive temperature coefficient polymer composition;

extruding said first admixture to obtain an extruded pre-mix of crystalline polymer and filler;

allowing the first admixture to solidify, and thereafter admixing the pre-mix with more electrically conductive filler in sufficient quantity to attain the predetermined proportion of filler in the composition, and melting and extruding the resulting mix to form said positive temperature coefficient polymer composition.

2. The process of claim 1 where the crystalline polymer is high density polyethylene and the electrically conductive filler is carbon black.

3. The process of claim 2 where the pre-mix comprises approximately 25 to 45 percent by weight of carbon black.

4. The process of claim 2 where the positive temperature coefficient polymer composition comprises approximately 50 to 60 percent by weight of carbon black.

5. The process of claim 1 where the step of blending the crystalline polymer with the electrically conductive filler into a first intimate admixture is performed at room temperature.

6. The process of claim 5 where the electrically conductive filler is carbon black having a particle size of approximately 20 to 100 nm.

7. The process of claim 6 wherein approximately 25 to 45 percent by weight of carbon black is blended with the crystalline polymer.

8. The process of claim 7 where the crystalline polymer is high density polyethylene.

9. The process of claim 1 where the step of admixing the pre-mix with more electrically conductive filler is performed in a compounding extruder.

10. The process of claim 9 where the pre-mix comprises approximately 25 to 45 percent by weight of carbon black and where sufficient carbon black is added to said pre-mix to raise the carbon black content of the positive temperature coefficient composition to approximately 50 to 60 percent by weight.

11. The process of claim 10 where the crystalline polymer is high density polyethylene.

12. The process of claim 1 further comprising the steps of measuring the electrical resistivity of the positive temperature coefficient polymer composition that is obtained in the process and generating a signal that is proportional to the difference between the measured resistivity and a pre-set resistivity value, and utilizing said difference signal to adjust the quantity of electrically conductive filler added to the pre-mix in the admixing step to minimize the value of said difference signal.

13. The process of claim 12 wherein the steps of measuring the electrical resistivity of the positive temperature coefficient polymer composition, generating a difference signal and utilizing said difference signal to adjust the quantity of electrically conductive filler added to the pre-mix is performed periodically and include-the application of a microprocessor.

14. The process of claim 12 wherein the steps of measuring the electrical resistivity of the positive temperature coefficient polymer composition, generating a difference signal and utilizing said difference signal to adjust the quantity of electrically conductive filler added to the pre-mix is performed continuously and include the application of a microprocessor.

15. A process for producing a positive temperature coefficient polymer composition comprising high density polyethylene and electrically conductive carbon black that is present in a predetermined proportion in the composition in the range of approximately 50 to 60 percent by weight, the process comprising the steps of:

blending high density polyethylene with carbon black into a first intimate admixture in proportions wherein the carbon black is substantially less in the first intimate admixture than the predetermined proportion of carbon black in the positive temperature coefficient polymer composition;

extruding said first admixture to obtain an extruded pre-mix of crystalline polymer and carbon black comprising carbon black in the range of approximately 25 to 45 percent by weight;

allowing the first admixture to solidify, and thereafter admixing the pre-mix with more carbon black in sufficient quantity to attain the predetermined proportion of carbon black in the composition,

and melting and extruding the resulting mix to form said positive temperature coefficient polymer composition.

16. The process of claim 15 wherein the step of dry blending is performed at substantially ambient temperature.

17. The process of claim 15 wherein the extruded pre-mix comprises carbon black in the range of approximately 30 to 35 percent by weight.

18. The process of claim 17 wherein in the step of admixing the pre-mix sufficient carbon black is added to attain said positive temperature coefficient polymer composition comprising a predetermined percentage of carbon black in the range of approximately 50 to 55 percent by weight.

19. The process of claim 15 further comprising the steps of measuring the electrical resistivity of the positive temperature coefficient polymer composition that is obtained in the process and generating a signal that is proportional to the difference between the measured resistivity and a pre-set resistivity value, and utilizing said difference signal to adjust the quantity of carbon black added to the pre-mix in the admixing step to minimize the value of said difference signal.

20. The process of claim 19 wherein the steps of measuring the electrical resistivity of the positive temperature coefficient polymer composition, generating a difference signal and utilizing said difference signal to adjust the quantity of carbon black added to the pre-mix is performed periodically and include the application of a microprocessor.

21. The process of claim 19 wherein the steps of measuring the electrical resistivity of the positive temperature coefficient polymer composition, generating a difference signal and utilizing said difference signal to adjust the quantity of carbon black added to the pre-mix is performed continuously and include the application of a microprocessor.