Method for making a spunbonded high loft nonwoven web
The invention relates to a method for making a spunbonded high loft nonwoven web comprising crimped multicomponent fibers, the process comprising continuously spinning the fibers, directing the fibers to a spin-belt by deflectors and/or air streams, laying down the fibers on the spinbelt and pre-consolidating the fibers after laydown using one or more pre-consolidation rollers to form a pre-consolidated web, wherein a first component of the fibers comprises a PP homopolymer and a second component of the fibers comprises a PP/PE copolymer, wherein the pre-consolidation rollers are operated at a temperature of smaller 110° C. and/or a linear contact force of smaller 5 N/mm.
1. A method for making a high loft spunbonded nonwoven web comprising crimped multicomponent fibers, the process comprising continuously spinning the fibers, directing the fibers to a spin-belt by deflectors or air streams or both, laying down the fibers on the spin-belt and pre-consolidating the fibers after laydown using one or more pre-consolidation rollers to form a pre-consolidated web, wherein a first component of the fibers comprises a polypropylene (PP) homopolymer and a second component of the fibers comprises a polypropylene/polyethylene (PP/PE) copolymer, wherein the pre-consolidation rollers are operated at a temperature of below 100° C. and a linear contact force of below 5 N/mm.
2. The method of claim 1 , wherein the pre-consolidation rollers are operated at a temperature of from 20° C. to less than 100° C.
3. The method of claim 1 , wherein the pre-consolidation rollers are operated at a linear contact force of 1-4 N/mm.
4. The method of claim 1 , wherein the content of ethylene-stemming repetitive units in the PP/PE copolymer is >0-5 wt %.
5. The method of claim 1 , wherein the PP/PE copolymer is a random copolymer.
6. The method of claim 1 , wherein the PP homopolymer is isotactic.
7. The method of claim 1 , wherein the melt flow rates or the polydispersities of the PP homopolymer and the PP/PE copolymer or both differ by less than 30%.
8. The method of claim 1 , wherein the melting points of the PP homopolymer and the PP/PE copolymer differ by 10° C. or more or by 20° C. or less, or both.
9. The method of claim 1 , wherein the multicomponent fibers are bicomponent fibers and/or have a side-by-side configuration.
10. The method of claim 1 , wherein the weight ratio of the first to second component in the multicomponent fibers is 40/60-80/20.
11. The method of claim 1 further comprising bonding the pre-consolidated web using one or more calandering rolls, at least one of which is embossed, and/or hot air through bonding.
12. The method of claim 11 , wherein the calandering rolls are operated at a temperature of and/or the air used in hot air through bonding has a temperature of 120-145° C.
13. The method of claim 1 , wherein the pre-consolidation rollers are operated at a temperature of 40-90° C.
14. The method of claim 1 , wherein the pre-consolidation rollers are operated at a temperature of 55-75° C.
15. The method of claim 1 , wherein the pre-consolidation rollers are operated at a linear contact force of 1-2.5 N/mm.
16. The method of claim 1 , wherein the melt flow rates or the polydispersities of the PP homopolymer and the PP/PE copolymer or both differ by less than 20%.
17. The method of claim 1 , wherein the weight ratio of the first to second component in the multicomponent fibers is 40/60-60/40.