Fabric crepe process for making absorbent sheet

• US 20080245492A1
• Filed: 06/05/2008
• Published: 10/09/2008
• Est. Priority Date: 10/07/2002
• Status: Active Grant

• Current Assignee: GPCP IP Holdings LLC
• Original Assignee: Colin A. Jones, David P. Duggan, David W. Lomax, Dean J. Baumgartner, Guy H. Super, Jeffrey E. Krueger, Richard W. Eggen, Stephen J. Mccullough, Steven L. Edwards
• Inventors: Super, Guy H., McCullough, Stephen J., Edwards, Steven L., Eggen, Richard W., Krueger, Jeffrey E., Lomax, David W., Duggan, David P., Baumgartner, Dean J., Jones, Colin A.
• Granted Patent: US 7,704,349 B2
• Time in Patent Office: Days
• US Class Current: 162/111
• CPC Class Codes: D21F 11/006 Making patterned paper
• CPC Class Codes: D21F 11/14 Making cellulose wadding, filter or blotting paper
• CPC Class Codes: D21F 11/145 including a through-drying process
• CPC Class Codes: D21H 21/20 Wet strength agents
• CPC Class Codes: D21H 25/005 Mechanical treatment D21H25/08, D21H25/18 take precedence
• CPC Class Codes: D21H 27/40 at least one of the sheets being non-planar, e.g. crêped crêping or corrugating paper B31F
• CPC Class Codes: Y10T 428/24446 Wrinkled, creased, crinkled or creped
• CPC Class Codes: Y10T 428/24455 Paper
• CPC Class Codes: Y10T 428/24479 including variation in thickness

Abstract

A process for making absorbent cellulosic paper products such as sheet for towel, tissue and the like, includes compactively dewatering a nascent web followed by wet belt creping the web at an intermediate consistency of anywhere from about 30 to about 60 percent under conditions operative to redistribute the fiber on the belt, which is preferably a fabric. In preferred embodiments, the web is thereafter adhesively applied to a Yankee dryer using a creping adhesive operative to enable high speed transfer of the web of intermediate consistency such as a poly(vinyl alcohol)/polyamide adhesive. An absorbent sheet so prepared from a papermaking furnish exhibits an absorbency of at least about 5 g/g, a CD stretch of at least about 4 percent, and an MD/CD tensile ratio of less than about 1.1, and also exhibits a maximum CD modulus at a CD strain of less than 1 percent and sustains a CD modulus of at least 50 percent of its maximum CD modulus to a CD strain of at least about 4 percent. Products of the invention may also exhibit an MD modulus at break 1.5 to 2 times their initial MD modulus.

Claims

1. A method of making a belt-creped absorbent cellulosic sheet comprising:

a) compactively dewatering a papermaking furnish to form a nascent web having a generally random distribution of papermaking fiber;

b) applying the dewatered web having a generally random fiber distribution to a translating transfer surface moving at a first speed;

c) belt-creping the web from the transfer surface at a consistency of from about 30 to about 60 percent utilizing a patterned creping belt, the creping step occurring under pressure in a belt creping nip defined between the transfer surface and the creping belt wherein the belt is traveling at a second speed slower than the speed of said transfer surface, the belt pattern, nip parameters, velocity delta and web consistency being selected such that the web is creped from the surface and redistributed on the creping belt to form a web with a reticulum having a plurality of interconnected regions of different fiber orientation including at least (i) a plurality of fiber enriched regions of having an orientation bias in a direction transverse to the machine-direction, interconnected by way of (ii) a plurality of colligating regions whose fiber orientation bias is offset from the fiber orientation of the fiber enriched regions; and

d) drying the web.

2. The method according to claim 1, wherein the plurality of fiber enriched regions and colligating regions recur in a regular pattern of interconnected fibrous regions throughout the web where the orientation bias of the fibers of the fiber enriched regions and colligating regions are transverse to one another.

3. The method according to claim 1, wherein the fibers of the fiber enriched regions are substantially oriented in the CD.

4. The method according to claim 1, wherein the plurality of fiber enriched regions have a higher local basis weight than the colligating regions.

5. The method according to claim 1, wherein at least a portion of the colligating regions consist of fibers that are substantially oriented in the MD.

6. The method according to claim 1, wherein there is a repeating pattern including a plurality of fiber enriched regions, a first plurality of colligating regions whose fiber orientation is biased toward the machine-direction, and a second plurality of colligating regions whose fiber orientation is biased toward the machine-direction but offset from the fiber orientation bias of the first plurality of colligating regions.

7. The method according to claim 6, wherein the fibers of at least one of the plurality of colligating regions are substantially oriented in the MD.

8. The method according to claim 1, wherein the fiber enriched regions exhibit a plurality of U-shaped folds transverse to the machine-direction.

9. The method according to claim 1, wherein the creping belt is a creping fabric provided with CD knuckles defining creping surfaces transverse to the machine-direction.

10. The method according to claim 9, wherein the distribution of the fiber enriched regions corresponds to the arrangement of CD knuckles on the creping fabric.

11. A method of making a belt-creped absorbent cellulosic sheet comprising:

a) compactively dewatering a papermaking furnish to form a nascent web having an apparently random distribution of papermaking fiber;

b) applying the dewatered web having the apparently random fiber distribution to a translating transfer surface moving at a first speed;

c) belt-creping the web from the transfer surface at a consistency of from about 30 to about 60 percent utilizing a patterned creping belt, the creping step occurring under pressure in a belt creping nip defined between the transfer surface wherein the creping belt is urged into contact with the transfer surface over a nip length by way of a deformable creping roll wherein the belt is traveling at a second speed slower than the speed of said transfer surface, the belt pattern, nip parameters, velocity delta and web consistency being selected such that the web is creped from the transfer surface and redistributed on the creping belt; and

d) drying the web.

12. The method according to claim 11, wherein the creping roll is provided with a deformable cover having a thickness of at least 25% of the nip length.

13. The method according to claim 11, wherein the creping roll is provided with a deformable cover having a thickness of at least 50% of the nip length.

14. A method of making a belt-creped absorbent cellulosic sheet comprising:

a) compactively dewatering a papermaking furnish to form a nascent web having an apparently random distribution of papermaking fiber;

b) applying the dewatered web having the apparently random fiber distribution to a translating transfer surface moving at a first speed;

c) belt-creping the web from the transfer surface at a consistency of from about 30 to about 60 percent utilizing a patterned creping belt, the creping step occurring under pressure in a belt creping nip defined between the transfer surface and the creping belt wherein the belt is traveling at a second speed slower than the speed of said transfer surface, the belt pattern, nip parameters, velocity delta and web consistency being selected such that the web is creped from the transfer surface and redistributed on the creping belt to form a web with a reticulum having a plurality of interconnected regions of different local basis weights including at least (i) a plurality of fiber enriched pileated regions of high local basis weight, interconnected by way of (ii) a plurality of lower local basis weight linking regions whose fiber orientation is biased toward the direction between pileated regions;

d) transferring the web from the creping belt to a drying cylinder at the consistency of from about 30 to about 60 percent, wherein the web is adhered to the drying cylinder with a hygroscopic, re-wettable adhesive adapted to secure the web to the drying cylinder;

e) drying the web on the drying cylinder; and

f) creping the web from the drying cylinder.

15. The method according to claim 14, wherein the web is creped from the transfer cylinder at a consistency of from about 35 percent to about 55 percent.

16. The method according to claim 14, wherein the web is creped from the transfer cylinder at a consistency of from about 40 percent to about 50 percent.

17. The method according to claim 14, wherein the adhesive is a substantially non-crosslinking adhesive.

18. The method according to claim 14, wherein the creping adhesive comprises poly(vinyl alcohol).

19. The method according to claim 14, wherein the creping adhesive comprises from about 10 to about 90 percent poly(vinyl alcohol) based on the resin content of the adhesive.

20. The method according to claim 14, wherein the creping adhesive comprises poly(vinyl alcohol) and at least a second resin and wherein the weight ratio of poly(vinyl alcohol) to the combined weight of poly(vinyl alcohol) and the second resin is at least about 3:

4.

21. The method according to claim 14, wherein the creping adhesive comprises poly(vinyl alcohol) and at least a second resin and wherein the weight ratio of poly(vinyl alcohol) to the combined weight of poly(vinyl alcohol and the second resin is at least about 5:

6.

22. The method according to claim 14, wherein the creping adhesive comprises poly(vinyl alcohol) and at least a second resin and wherein the weight ratio of poly(vinyl alcohol) to the combined weight of poly(vinyl alcohol) and the second resin is at least about 5:

6 and at most about 7;

8.

23. The method according to claim 14, wherein said creping adhesive consists essentially of poly(vinyl alcohol) and an amide polymer, optionally including one or more modifiers.

24. The method according to claim 14, wherein the adhesive contains a modifier comprising a quaternary ammonium complex with at least one non-cyclic amide.

25. The method according to claim 14, operated at a production line speed of at least about 1000 fpm.

26. The method according to claim 14, operated at a production speed of at least 2000 fpm.

27. The method according to claim 14, operated at a production speed of at least 3000 fpm.

28. The method according to claim 14, operated at a production speed of at least 5000 fpm.

29. The method according to claim 14, wherein the step of drying the web on the drying cylinder includes drying the web with high velocity heated air impinging on the web in a drying hood about the drying cylinder.

30. The method according to claim 29, wherein the impinging air has a jet velocity of from about 15,000 fpm to about 30,000 fpm.

31. The method according to claim 30, wherein a Yankee dryer dries the web at a rate of from about 20 (lbs. water/f²-hr) to about 50 lbs. water/ft²-hr.

32. The method according to claim 14, wherein the web is dewatered to a consistency of at least 10 percent prior to applying it to the transfer surface.

33. The method according to claim 14, wherein the web is dewatered to a consistency of at least about 30 percent prior to applying it to the transfer surface.

34. The method according to claim 14, wherein the web is dewatered by wet pressing it with a papermaking felt while applying the web to the transfer cylinder.

35. The method according to claim 34, wherein the step of wet-pressing the web with a papermaking felt while applying it to the transfer surface is carried out in a shoe press.

36. The method according to claim 14, wherein the transfer roll is a shoe press roll and the partially dewatered web is dewatered by wet-pressing the web while applying it to the transfer roll.

37. The method according to claim 14, operated at an Aggregate Crepe of at least about 20 percent.

38. The method according to claim 14, operated at an Aggregate Crepe of at least about 40 percent.

39. The method according to claim 14, operated at an Aggregate Crepe of at least about 50 percent.

40. The method according to claim 14, operated at an Aggregate Crepe of at least about 60 percent.

41. The method according to claim 14, operated at an Aggregate Crepe of at least about 80 percent.