Method and apparatus for making a nonwoven fabric from thermoplastic filaments
US-2016312384-A1 · Oct 27, 2016 · US
US10023663B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-10023663-B2 |
| Application number | US-201314411250-A |
| Country | US |
| Kind code | B2 |
| Filing date | Jun 27, 2013 |
| Priority date | Jun 27, 2012 |
| Publication date | Jul 17, 2018 |
| Grant date | Jul 17, 2018 |
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Propylene polymers having a melt flow index in the range from 3.0 dg/min to 8.0 dg/min can be particularly suited for high-tenacity fibers and yarns and nonwovens. The propylene polymers can be produced by a process that includes polymerizing propylene or propylene and at least one comonomer in presence of a Ziegler-Natta polymerization catalyst, an aluminium alkyl, and hydrogen.
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The invention claimed is: 1. A propylene polymer with up to and including 1.0 wt %, relative to the total weight of the propylene polymer, of at least one comonomer selected from the group of alpha-olefins consisting of ethylene, butane-1, pentene-1,4-methyl-pentene-1 and octene-1, said propylene polymer comprising: a melt flow index in the range from 3.0 to 8.0 dg/min, determined according to ISO 1133, condition L, 230° C., 2.16 kg, a xylene solubles content in the range from 1.0 wt % to 3.5 wt %, relative to the total weight of the propylene polymer, a polydispersity index of at least 3.0 and of at most 5.0, a content of mmmm pentads in the range from 97.0% to 99.0%, determined on the insoluble heptane fraction of the xylene insolubles fraction, and a recovery compliance in the range from 2.5·10 −4 Pa −1 to 5.5·10 −4 Pa −1 . 2. The propylene polymer according to claim 1 with up to and including 0.05 wt %, relative to the total weight of the propylene polymer, of at least one comonomer selected from the group of alpha-olefins consisting of ethylene, butene-1, pentene-1, 4 -methyl-pentene-1 and octene-1. 3. The propylene polymer according to claim 2 , wherein the melt flow index is in the range from 4.0 dg/min to 8.0 dg/min, determined according to ISO 1133, condition L, at 230° C. and 2.16 kg. 4. The propylene polymer according to claim 2 , wherein the xylene solubles content is in the range from 1.5 wt % to 3.5 wt %, relative to the total weight of the propylene polymer. 5. The propylene polymer according to claim 2 , wherein the recovery compliance is in the range from 4.0·10 −4 Pa −1 to 5.5·10 −4 Pa −1 . 6. The propylene polymer according to claim 1 , with from more than 0.05 wt % to 1.0 wt %, relative to the total weight of the propylene polymer, of at least one comonomer selected from the group of alpha-olefins consisting of ethylene, butene-1, pentene-1, 4 -methyl-pentene-1 and octane-1. 7. The propylene polymer according to claim 6 , wherein the melt flow index is in the range from 3.0 dg/min to 6.0 dg/min, determined according to ISO 1133, condition L, at 230° C. and 2.16 kg. 8. The propylene polymer according to claim 6 , wherein the xylene solubles content is in the range from 1.5 wt % to 3.0 wt %, relative to the total weight of the propylene polymer. 9. The propylene polymer according to claim 6 , wherein the recovery compliance is in the range from 3.0·10 −4 Pa −1 to 4.5·10 −4 Pa −1 . 10. Fibers or yarns comprising the propylene copolymer of claim 1 . 11. Nonwovens comprising the fibers of claim 10 . 12. A process for the production of the propylene polymer comprising the step of (a) polymerizing propylene or polymerizing propylene and at least one comonomer in presence of a Ziegler-Natta polymerization catalyst, an aluminium alkyl, and hydrogen, said Ziegler-Natta polymerization catalyst comprising a titanium compound, which has at least one titanium-halogen bond, and an internal donor, both supported on magnesium halide in active form, wherein the process is controlled so as to produce propylene polymer with: 1.0 wt %, relative to the total weight of the propylene polymer, of at least one comonomer; consisting of ethylene, butane-1, pentene-1,4 -methyl-pentene-1 and octane-1; a melt flow index in the range from 3.0 to 8.0 dg/min, determined according to ISO 1133, condition L, 230° C., 2.16 kg; a xylene solubles content in the range from 1.0 wt % to 3.5 wt %, relative to the total weight of the propylene polymer; a polydispersity index of at least 3.0 and of at most 5.0; a content of mmmm pentads in the range from 97.0% to 99.0%, determined on the insoluble heptane fraction of the xylene insolubles fraction; and a recovery compliance in the range from 2.5·10 −4 Pa −1 to 5.5·10 −4 Pa −1 . 13. The process according to claim 12 , wherein the Ziegler-Natta polymerization catalyst has an internal electron donor that comprises at least 80 wt % of a diether. 14. The process according to any of claim 12 , further comprising the steps of (b) melting the propylene copolymer obtained in step (a) in an extruder, (c) extruding the molten propylene copolymer of step (b) from a number of fine capillaries of a spinneret, thus obtaining molten fibers, and (d) subsequently solidifying the fibers of step (c). 15. The process according to claim 14 , further comprising the steps of (e) re-heating the solidified fibers of step (d) to a temperature of 130° C. or less, (f) drawing said re-heated fibers of step (e) with a draw ratio of at least 2.5, and (g) annealing said drawn fibers obtained in step (f). 16. The propylene polymer according to claim 1 , wherein the melt flow index is in the range from 4.5 dg/min to 7.5 dg/min, determined according to ISO 1133, condition L, at 230° C. and 2.16 kg. 17. The propylene polymer according to claim 1 , wherein the melt flow index is in the range from 5.0 dg/min to 7.0 dg/min, determined according to ISO 1133, condition L, at 230° C. and 2.16 kg.
Heat treatment (heating for finishing D02J13/00) · CPC title
Nonwoven fabric [i.e., nonwoven strand or fiber material] · CPC title
Stretch-spinning methods ({D01D5/098 takes precedence} finishing by stretching D02J1/22) · CPC title
Copolymers of polypropylene (B29K2023/16 takes precedence) · CPC title
comprising olefins as the major constituent · CPC title
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