IP Library Granted Patent US 7,989,062
Granted Patent B2
US 7,989,062 · App. 12/091,834 · Granted Aug 2, 2011

Biodegradable continuous filament web

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Quick Facts
Patent No.
US 7,989,062
App. No.
12/091,834
Granted
Aug 2, 2011
Kind
B2
Abstract

A biodegradable nonwoven web comprising substantially continuous multicomponent filaments is provided. The filaments comprise a first component and a second component. The first component contains at least one high-melting point aliphatic polyester having a melting point of from about 160° C. to about 250° C. and the second component contains at least one low-melting point aliphatic polyester. The melting point of the low-melting point aliphatic polyester is at least about 30° C. less than the melting point of the high-melting point aliphatic polyester. The low-melting point aliphatic polyester has a number average molecular weight of from about 30,000 to about 120,000 Daltons, a glass transition temperature of less than about 25° C., and an apparent viscosity of from about 50 to about 215 Pascal-seconds, as determined at a temperature of 160° C. and a shear rate of 1000 sec −1 .

Claims (36)

1. A biodegradable nonwoven web comprising substantially continuous multicomponent filaments, wherein the multicomponent filaments comprise a first component and a second component, the first component containing a first aliphatic polyester having a melting point of from about 160° C. to about 250° C. and the second component containing a second aliphatic polyester, wherein the melting point of the second aliphatic polyester is at least about 30° C. less than the melting point of the first aliphatic polyester, and wherein the second aliphatic polyester has a number average molecular weight of from about 30,000 to about 120,000 Daltons, a glass transition temperature of less than about 25° C., and an apparent viscosity of from about 50 to about 215 Pascal-seconds, as determined at a temperature of 160° C. and a shear rate of 1000 sec −1 , wherein the second component is free of a multi-carboxylic acid nucleating agent.

2. The biodegradable nonwoven web of claim 1 , wherein the first aliphatic polyester is polylactic acid.

3. The biodegradable nonwoven web of claim 1 , wherein the second aliphatic polyester has an apparent viscosity of from about 80 to about 150 Pascal-seconds, as determined at a temperature of 160° C. and a shear rate of 1000 sec −1 .

4. The biodegradable nonwoven web of claim 1 , wherein the second aliphatic polyester has a melting point at least about 40° C. less than the melting point of the first aliphatic polyester.

5. The biodegradable nonwoven web of claim 1 , wherein the second aliphatic polyester has a melting point of from about 100° C. to about 140° C.

6. The biodegradable nonwoven web of claim 1 , wherein the second aliphatic polyester has a number average molecular weight of from about 40,000 to about 100,000 Daltons.

7. The biodegradable nonwoven web of claim 1 , wherein the second aliphatic polyester has a polydispersity index of from about 1.0 to about 3.0.

8. The biodegradable nonwoven web of claim 1 , wherein the second aliphatic polyester has a melt flow index of from about 20 to about 120 grams per 10 minutes, measured at a force of 2160 grams and temperature of 190° C. in accordance with ASTM Test Method D1238-E.

9. The biodegradable nonwoven web of claim 1 , wherein the second aliphatic polyester has a glass transition temperature of about 0° C. or less.

10. The biodegradable nonwoven web of claim 1 , wherein the second aliphatic polyester has a glass transition temperature of about −10° C. or less.

11. The biodegradable nonwoven web of claim 1 , wherein the second aliphatic polyester is polybutylene succinate.

12. The biodegradable nonwoven web of claim 1 , wherein the filaments have a sheath/core or side-by-side configuration.

13. The biodegradable nonwoven web of claim 1 , wherein the web exhibits a peak elongation in the machine direction of at least about 10%.

14. The biodegradable nonwoven web of claim 1 , wherein the web exhibits a peak elongation in the machine direction of at least about 35%.

15. The biodegradable nonwoven web of claim 1 , wherein the web exhibits a peak elongation in the cross machine direction of at least about 35%.

16. The biodegradable nonwoven web of claim 1 , wherein the web exhibits a peak elongation in the cross machine direction of at least about 50%.

17. The biodegradable nonwoven web of claim 1 , wherein the web exhibits a peak load in the machine direction of at least about 3500 grams-force per inch.

18. The biodegradable nonwoven web of claim 1 , wherein the web exhibits a peak elongation in the cross machine direction of at least about 1500 grams-force per inch.

19. The biodegradable nonwoven web of claim 1 , wherein the filaments are autogenously bonded at intermittent compacted areas.

20. The biodegradable nonwoven web of claim 19 , wherein at least a portion of the high melting point aliphatic polyester within the compacted areas retains a substantially fibrous form.

21. The biodegradable nonwoven web of claim 20 , wherein the substantially fibrous high melting point polymer is oriented in two or more directions.

22. A method for forming the biodegradable nonwoven web of claim 1 , the method comprising:

co-extruding a first thermoplastic composition and a second thermoplastic composition to form the multicomponent filaments, the first thermoplastic composition comprising the first aliphatic polyester and the second thermoplastic composition comprising the second aliphatic polyester;

randomly depositing the filaments onto a forming surface; and

melt-fusing the filaments at intermittent bond regions.

23. The method of claim 22 , wherein the second thermoplastic composition is extruded at a temperature ranging from about 145° C. to about 195° C.

24. The method of claim 22 , wherein the filaments are melt-fused by passing the web through a nip formed between two rolls.

25. The method of claim 24 , wherein one or both of the rolls are heated to a temperature of from about 50° C. to about 160° C.

26. The method of claim 24 , wherein one or both of the rolls are heated to a temperature of from about 100° C. to about 140° C.

27. The method of claim 24 , wherein a pressure of from about 5 to about 150 pounds per square inch is applied at the nip.

28. The method of claim 24 , wherein a pressure of from about 30 to about 60 pounds per square inch is applied at the nip.

29. The method of claim 22 , wherein the bond regions cover less than 50% of a surface of the web.

30. An absorbent article comprising an absorbent core positioned between a substantially liquid-impermeable layer and a liquid-permeable layer, wherein the substantially liquid-impermeable layer contains the biodegradable nonwoven web of claim 1 .

31. The absorbent article of claim 30 , wherein the substantially liquid-impermeable layer forms an outer cover of the absorbent article.

32. The absorbent article of claim 30 , wherein the biodegradable nonwoven web is laminated to a breathable film.

33. The biodegradable nonwoven web of claim 1 , wherein the second aliphatic polyester has a number average molecular weight of from about 45,000 to about 85,000 Daltons.

Assignments (1)
NAME CHANGE Recorded Feb 3, 2015
From: KIMBERLY-CLARK WORLDWIDE, INC.
To: KIMBERLY-CLARK WORLDWIDE, INC.
Reel/Frame 034880/0704 →