Producing high tenacity, high modulus crystalline article such as fiber or film

• US 4,551,296 A
• Filed: 01/20/1984
• Issued: 11/05/1985
• Est. Priority Date: 03/19/1982
• Status: Expired due to Term

• Current Assignee: Allied Corp. (Honeywell International Inc.)
• Original Assignee: Allied Corp. (Honeywell International Inc.)
• Inventors: Kavesh, Sheldon, Prevorsek, Dusan C.
• Primary Examiner(s): Thurlow, Jeffery
• Application Number:
  US06/572,607
• Time in Patent Office: 655 Days
• Field of Search: 264/203-205, 264/184, 264/210.1, 264/210.8, 264/211, 264/177 F
• US Class Current: 264/203
• CPC Class Codes: D01F 6/02 from homopolymers obtained by reactions only involving carbon-to-carbon unsaturated bonds
• CPC Class Codes: D01F 6/04 from polyolefins
• CPC Class Codes: D01F 6/06 from polypropylene

Abstract

Solutions of ultrahigh molecular weight polymers such as polyethylene in a relatively non-volatile solvent are extruded through an aperture at constant concentration through the aperture and cooled to form a first gel of indefinite length. The first gels are extracted with a volatile solvent to form a second gel and the second gel is dried to form a low porosity xerogel. The first gel, second gel or xerogel, or a combination, are stretched. Among the products obtainable are polyethylene fibers of greater than 30 or even 40 g/denier tenacity and of modulus greater than 1000 or even 1600 or 2000 g/denier.

Claims

1. A process for producing a high strength, high modulus shaped thermoplastic article of substantially indefinite length which comprises the steps:

(a) forming a solution of a thermoplastic crystalline polymer selected from the group consisting of polyethylene, polypropylene, polyoxymethylene, polybutene-1, poly(vinylidene fluoride) and poly(4-methylpentene-1) in a first, non-volatile solvent at a first concentration of about 2 to 15% by weight of polymer per unit weight of first solvent, said thermoplastic polymer having a weight average molecular length between about 7×

10⁴ and about 71×

10⁴ backbone atoms and the solubility of said thermoplastic polymer in said first solvent at a first temperature being at least said first concentration;

(b) extruding said solution through an aperture, said solution being at a temperature no less than said first temperature upstream of the aperture and being substantially at the first concentration both upstream and downstream of the aperture;

(c) cooling the solution adjacent to and downstream of the aperture to a second temperature below the temperature at which a gel is formed to form a gel containing first solvent of substantially indefinite length;

(d) extracting the gel containing first solvent with a second, volatile solvent for a sufficient contact time to form a gel containing second solvent which gel is substantially free of first solvent and is of substantially indefinite length;

(e) drying the gel containing second solvent to form a xerogel of substantially indefinite length free of first and second solvent; and

,

(f) stretching at a sufficient temperature at least one of;

(i) the gel containing the first solvent,

(ii) the gel containing the second solvent and,

(iii) the xerogel

at a total stretch ratio;

(i) in the case of polyethylene which is sufficient to achieve a tenacity of at least about 20 g/denier and a modulus of at least about 600 g/denier,

(ii) in the case of polypropylene which is sufficient to achieve a tenacity of at least about 10 g/denier and a modulus of at least about 160 g/denier, and

(iii) in the case of polyoxymethylene, polybutene-1, poly(vinylidene fluoride) or poly(4-methylpentene-1) of at least about 10;

1.

2. The process of claim 1 wherein said aperture has an essentially circular cross-section;

said gel containing the first solvent and gel containing the second solvent are each gel fibers;

said xerogel is a xerogel fiber; and

said thermoplastic article is a fiber.

3. The process of claim 1 wherein said aperture has an essentially rectangular cross-section, said gel containing first solvent and gel containing second solvent are each gel films;

said xerogel is a gel film; and

said thermoplastic article is a film.

4. The process of claim 1 wherein said first temperature is between about 180°

C. and about 250°

C.;

said second temperature is between about -40°

C. and about 40°

C.;

the cooling rate between said first temperature and said second temperature is at least about 50°

C./min; and

said first solvent has a vapor pressure less than 20 kPa at said first temperature.

5. The process of claim 4 wherein said first solvent is a hydrocarbon and said second solvent is non-flammable and has an atmospheric boiling point less than 80°

C.

6. The process of claim 1 wherein said cooling comprises quenching.

7. The process of claim 1 wherein said stretching is conducted in at least two stages.

8. The process of claim 7 wherein a first stretching stage is of the gel containing the first solvent.

9. The process of claim 8 wherein a second stretching stage is of the gel containing the first solvent.

10. The process of claim 7 wherein at least one stage of said stretching is performed on the xerogel.

11. The process of claim 1 wherein steps a, b, and c are preformed continuously in sequence.

12. The process of claim 1 wherein said thermoplastic crystalline polymer is polyethylene.

13. A process for producing a high strength, high modulus shaped thermoplastic article of substantially indefinite length which comprises the steps:

(a) forming a solution of a thermoplastic crystalline polymer selected from the group consisting of polyethylene, polypropylene, polyoxymethylene, polybutene-1, poly(vinylidene fluoride) and poly(4-methylpentene-1) in a first, non-volatile solvent at a first concentration between about 2 and 15% by weight of polymer per unit weight of first solvent, said thermoplastic polymer having a weight average molecular length between about 7×

10⁴ and about 71×

10⁴ backbone atoms and the solubility of said thermoplastic polymer in said first solvent at a first temperature being at least said first concentration;

(b) extruding said solution through an aperture, said solution being at a temperature no less than said first temperature upstream of the aperture and being substantially at the first concentration both upstream and downstream of the aperture;

(c) cooling the solution adjacent to and downstream of the aperture to a second temperature below the temperature at which a gel is formed, forming a gel containing first solvent of substantially indefinite length;

(d) extracting the gel containing first solvent with a second, volatile solvent for a sufficient contact time to form a gel containing second solvent which gel is substantially free of first solvent and is of substantially indefinite length;

(e) stretching at a sufficient temperature at least one of;

(i) the gel containing the first solvent, and

(ii) the gel containing the second solvent,

(f) drying the gel containing second solvent to form a xerogel of substantially indefinite length free of first and second solvent, which

(i) in the case of polyethylene has a tenacity of at least about 20 g/denier and a modulus of at least about 600 g/denier,

(ii) in the case of polypropylene has a tenacity of at least about 10 g/denier and a modulus of at least about 160 g/denier, and

(iii) in the case of polyoxymethylene, polybutene-1, poly(venylidene fluoride) or poly(4-methylpentene-1) been stretched at a ratio of at least about 10;

1.

14. The process of claim 13 wherein said stretching is conducted in at least two stages.

15. The process of claim 13 further comprising the step of stretching the xerogel.

16. The process of claim 13 wherein each gel and the xerogel are fibers.

17. The process of claim 13 wherein each gel and the xerogel are films.

18. The process of claim 13 wherein said cooling comprises quenching.

19. A process for producing a high strength, high modulus shaped thermoplastic article of substantially indefinite length which comprises the steps:

(a) forming a solution of a thermoplastic crystalline polymer selected from the group consisting of polyethylene and polypropylene in a first, nonvolatile solvent at a first concentration of between about 4 and 10% by weight of polymer per unit weight of first solvent, said thermoplastic polymer having a weight average molecular length between about 7×

10⁴ and about 71×

10⁴ backbone atoms and the solubility of said thermoplastic polymer in said first solvent at a first temperature being at least said first concentration;

(b) extruding said solution through an aperture, said solution being at a temperature no less than said first temperature upstream of the aperture and being substantially at the first concentration both upstream and downstream of the aperture;

(c) cooling the solution adjacent to and downstream of the aperture to a second temperature below the temperature at which a rubbery gel is formed, forming a gel containing first solvent of substantially indefinite length;

(d) extracting the gel containing first solvent with a second, volatile solvent for a sufficient contact time to form a gel containing second solvent which gel is substantially free of first solvent and is of substantially indefinite length;

(e) stretching at a sufficient temperature at least one of;

(i) the gel containing the first solvent, and

(ii) the gel containing the second solvent; and

(f) drying the gel containing second solvent to form a xerogel of substantially indefinite length free of first and second solvent, and

(i) in the case of polyethylene a tenacity of at least about 30 g/denier and/or a modulus of at least about 1000 g/denier, and

(ii) in the case of polypropylene a tenacity of at least about 10 g/denier and a modulus of at least about 160 g/denier.

20. The process of claim 19 wherein said cooling comprises quenching.

21. The process of claim 19 further comprising the step of stretching the xerogel.

22. A process for producing a high strength, high modulus shaped polyethylene article of substantially indefinite length which comprises the steps:

(a) forming a solution of polyethylene in a first, nonvolatile solvent at a first concentration of about 2 to 15 percent by weight of polymer per unit weight of first solvent, said polyethylene having a weight average molecular weight between about one million and about ten million and the solubility of said polyethylene in said first solvent at a first temperature being at least said first concentration;

(b) extruding said solution through an aperture, said solution being at a temperature no less than said first temperature upstream of the aperture and being substantially at the first concentration both upstream and downstream of the aperture;

(c) cooling the solution adjacent to and downstream of the aperture to a second temperature below the temperature which rubbery gel is formed, including quenching in a quench bath, forming a gel containing first solvent of substantially indefinite length;

(d) extracting the gel containing first solvent with a second, volatile solvent for a sufficient contact time to form a gel containing second solvent which gel is substantially free of first solvent and is of substantially indefinite length;

(e) stretching at a sufficient temperature at least one of;

(i) the gel containing the first solvent, and

(ii) the gel containing the second solvent; and

(f) drying the gel containing second solvent to form a xerogel of substantially indefinite length free of first and second solvent

the xerogel having a tenacity of at least about 20 g/denier, and a modulus of at least about 600 g/denier.

23. The process of claim 22 further comprising the step of stretching the xerogel.

24. The process of claim 22 wherein each gel and the xerogel are fibers, and the thermoplastic article is a fiber.

25. The process of claim 22 wherein each gel and the xerogel are films, and the thermoplastic article is a film.

26. A process for producing a high strength, high modulus shaped polyethylene article of substantially indefinite length which comprises the steps:

(a) forming a solution of polyethylene in a first, nonvolatile solvent at a first concentration of about 2 to 15 percent by weight of polymer per unit weight of first solvent, said polyethylene having a weight average molecular weight between about one million and about ten million and the solubility of said polyethylene in said first solvent at a first temperature being at least said first concentration;

(b) extruding said solution through an aperture, said solution being at a temperature no less than said first temperature upstream of the aperture and being substantially at the first concentration both upstream and downstream of the aperture;

(c) cooling the solution adjacent to and downstream of aperture to a second temperature below the temperature which rubbery gel is formed, including quenching in a quench bath, forming a gel containing first solvent of substantially indefinite length;

(d) extracting the gel containing first solvent with a second, volatile solvent for a sufficient contact time to form a gel containing second solvent which gel is substantially free of first solvent and is of substantially indefinite length;

(e) drying the gel containing second solvent to form a xerogel of substantially indefinite length free of first and second solvent, which xerogel has a pore volume less than about 10%; and

(f) stretching at a sufficient temperature at least one of;

(i) the gel containing the first solvent,

(ii) the gel containing the second solvent and,

(iii) the xerogel,

at a total stretch ratio which is sufficient to achieve a tenacity of at least about 20 g/denier and a modulus of at least about 600 g/denier.

27. The process of claim 26 wherein at least a portion of stretching is performed at a temperature between about 120°

C. and about 160°

C.

28. The process of claim 27 wherein the stretching is performed in at least two stages and wherein the stretching at the latest stage is performed at a temperature of between about 135°

C. and about 150°

C.

29. The process of claim 28 wherein said latest stage is performed on the xerogel.

30. A process for producing a high strength, high modulus shaped polyethylene article of substantially indefinite length which comprises the steps:

(a) forming a solution of polyethylene in a first, novolatile solvent at a first concentration of between about 2 and about 15% by weight of polymer per unit weight of first solvent, said polyethylene having a weight average molecular weight between about one million and about ten million and the solubility of said polyethylene in said first solvent at a first temperature being at least said first concentration;

(b) extruding said solution through an aperture, said solution being at a temperature no less than said first temperature upstream of the aperture and being substantially at the first concentration both upstream and downstream of the aperture;

(c) cooling the solution adjacent to and downstream of the aperture to a second temperature below the temperature which rubbery gel is formed, including quenching in a quench bath, forming a gel containing first solvent of substantially indefinite length;

(d) extracting the gel containing first solvent with a second, volatile solvent for a sufficient contact time to form a gel containing second solvent which gel is substantially free of first solvent and is of substantially indefinite length;

(e) stretching at a sufficient temperature at least one of;

(i) the gel containing the first solvent,

(ii) the gel containing the second solvent;

(f) drying the gel containing second solvent to form a xerogel of substantially indefinite length free of first and second solvent having a pore volume less than about 10%;

(g) stretching to xerogel to produce a stretched polyethylene article having a tenacity of at least about 20 g/denier and a modulus of at least about 1000 g/denier.