Force spun sub-micron fiber and applications

1. A process comprising:

spinning a plurality of continuous polymeric filaments by passing a mixture of at least one polymeric component and a solvent through a rotating spinneret having a plurality of orifices,

wherein the at least one polymeric component comprises one selected from the group consisting of a poly(phenylene ether) component, a poly(phenylene ether)-polysiloxane block copolymer, and combinations thereof,

wherein the solvent comprises benzene, toluene, xylene, chlorobenzene, chloroform, carbon tetrachloride, alcohols, ketones, anisole, veratrole, dichloroethane, trichloroethane or a combination thereof,

wherein the mixture has a viscosity greater than 100 centipoise,

wherein each of the plurality of continuous polymeric filaments has a length to diameter ratio that is more than 1,000,000,

wherein each of the plurality of continuous polymeric filaments has a diameter ranging from 50 nanometers to 5 microns,

wherein the spinning is conducted in a non-electrospinning environment and at greater than or equal to 6000 rotations per minute,

wherein the spinning is conducted at a rate of at least 300 grams/hour/spinneret; and

producing a non-woven web comprising the plurality of continuous polymeric filaments,

wherein the non-woven web has a width of at least 150 mm.

2. The process of claim 1 , wherein producing the non-woven web comprises depositing the plurality of continuous filaments onto one selected from the group consisting of a carrier substrate, a functional sheet, a film, a non-woven, a rolled good product, and combinations thereof.

3. The process of claim 2 , wherein the carrier substrate is a reciprocating belt.

4. The process of claim 2 , further comprising solidifying the plurality of continuous polymeric filaments before the depositing step.

5. The process of claim 1 , wherein the non-woven web is unconsolidated.

6. The process of claim 1 , further comprising consolidating the non-woven web.

7. The process of claim 1 , further comprising consolidating the non-woven web under pressure.

8. The process of claim 1 , wherein the spinning is conducted at a rate of at least 7000 grams/hour/spinerret.

9. The process of claim 1 , wherein each of the plurality of continuous polymeric filaments is provided with at least one additional functionality imparting at least one selected from the group consisting of therapeutic activity, catalytic activity microelectronic activity, micro-optoelectronic activity, magnetic activity, biological activity, and combinations thereof.

10. The process of claim 1 , wherein none of the plurality of continuous polymeric filaments are bonded to adjacent filaments.

11. The process of claim 1 , wherein a portion of the plurality of continuous polymeric filaments are at least partially bonded to adjacent filaments.

12. The process of claim 1 , wherein each of the plurality of continuous polymeric filaments are at least partially bonded to adjacent filaments.

13. The process of claim 1 , further comprising entangling the the plurality of continuous polymeric filaments.

14. The process of claim 13 , wherein the entangling is one of needle-punching and fluid hydroentangement.

15. The process of claim 1 , wherein the poly(phenylene ether) component comprises repeating structural units having the formula:

wherein each occurrence of Z 1 is independently halogen, unsubstituted or substituted C1-C12 hydrocarbyl provided that the hydrocarbyl group is not tertiary hydrocarbyl, C1-C12 hydrocarbylthio, C1-C12 hydrocarbyloxy, or C2-C12 halohydrocarbyloxy wherein at least two carbon atoms separate the halogen and oxygen atoms; and

wherein each occurrence of Z 2 is independently hydrogen, halogen, unsubstituted or substituted C1-C12 hydrocarbyl provided that the hydrocarbyl group is not tertiary hydrocarbyl, C1-C12 hydrocarbylthio, C1-C12 hydrocarbyloxy, or C2-C12 halohydrocarbyloxy wherein at least two carbon atoms separate the halogen and oxygen atoms.

16. The process of claim 1 , wherein the poly(phenylene ether)-polysiloxane block copolymer is prepared by an oxidative copolymerization method.

17. The process of claim 1 , wherein the poly(phenylene ether) component comprises a homopolymer or copolymer of monomers selected from the group consisting of 2,6 dimethylphenol, 2,3,6 trimethylphenol, and combinations thereof.

18. The process of claim 1 , further comprising at least partially removing the solvent from the plurality of continuous polymeric filaments before the plurality of continuous polymeric filaments are deposited.

19. The process of claim 1 , wherein the solvent is a chlorinated solvent.

20. The process of claim 1 , wherein the non-woven web contains less than 10 wt % of a material selected from the group consisting of polyvinyl pyrrolidine, polymethyl methacrylate, polyvinylidence fluoride, polypropylene, polycarbonate, polyethylene oxide, agarose, polyvinylidene fluoride, polylactic glycolic acid, nylon 6, polycaprolactone, polylactic acid, polybutylene terepthalate, polyetherimide homopolymers, polyetherimide co-polymers, polyetherether ketones homopolymers, polyetherether ketones copolymers, polyphenylene sulfones homopolymers, polyphenylene sulfones copolymers, polycarbonate homopolymers, polycarbonate copolymers, and combinations thereof.

21. The process of claim 1 , wherein the process excludes any detectable amount of a material selected form the group consisting of polyvinyl pyrrolidine, polymethyl methacrylate, polyvinylidene fluoride, polypropylene, polycarbonate, polyethylene oxide, agarose, polyvinylidene fluoride, polylactic glycolic acid, nylon 6, polycaprolactone, polylactic acid, polybutylene terepthalate, and combinations thereof.

22. A process of forming a non-woven web, said process comprising:

spinning a plurality of continuous polymeric filaments comprising one selected from the group consisting of a poly(phenylene ether) component, a poly(phenylene ether)-polysiloxane block copolymer, and combinations thereof,

the plurality of continuous polymeric filaments having a length to diameter ratio that is more than 1,000,000, and a diameter ranging from 50 nanometers to 5 microns;

said spinning comprising passing a mixture of at least one polymer and a solvent through a rotating spinneret having a plurality of orifices at greater than or equal to 6000 rotations per minute in a non-electrospinning environment;

chopping the plurality of continuous filaments and obtaining a plurality of chopped nano-fibers;

forming the plurality of chopped nano-fibers into a non-woven web;

the spinning being conducted at a rate of at least 300 grams/hour/spinneret, and

wherein the solvent comprises benzene, toluene, xylene, chlorobenzene, chloroform, carbon tetrachloride, alcohols, ketones, anisole, veratrole, dichloroethane, trichloroethane or a combination thereof, wherein the mixture has a viscosity greater than 100 centipoise.

23. The process of claim 22 , wherein none of the plurality of continuous polymeric filaments are bonded to adjacent filaments.

24. The process of claim 22 , wherein a portion of the plurality of continuous polymeric filaments are at least partially bonded to adjacent filaments.

25. The process of claim 22 , wherein each of the plurality of continuous polymeric filaments are at least partially bonded to adjacent filaments.

26. The process of claim 22 , further comprising entangling the plurality of continuous polymeric filaments.

27. The process of claim 22 , wherein the non-woven web contains less than 10 wt % of a material selected from the group consisting of polyvinyl pyrrolidine, polymethyl methacrylate, polyvinylidene fluoride, polypropylene, polycarbonate, polyethylene oxide, agarose, polyvinylidene fluoride, polylactic glycolic acid, nylon 6, polycaprolactone, polylactic acid, polybutylene terepthalate, polyetherimide homopolymers, polyetherimide co-polymers, polyetherether ketones homopolymers, polyetherether ketones copolymers, polyphenylene sulfones homopolymers, polyphenylene sulfones copolymers, polycarbonate homopolymers, polycarbonate copolymers, and combinations thereof.