IP Library Granted Patent US 7,018,508
Granted Patent B2
US 7,018,508 · App. 10/051,872 · Granted Mar 28, 2006

Process for producing dried singulated crosslinked cellulose pulp fibers

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Quick Facts
Patent No.
US 7,018,508
App. No.
10/051,872
Granted
Mar 28, 2006
Kind
B2
Abstract

This invention provides a dried singulated crosslinked cellulose pulp fiber product as well as an apparatus and a method for forming singulated, crosslinked, and dried fibers. In accordance with the process, a feed pulp containing a crosslinker is delivered to a jet drier. The jet drier singulates and dries the feed pulp. The singulated and dried fibers are collected from the jet drier. The feed pulp may be further treated with a treatment substance. The jet drier may be maintained at negative pressure. The product fibers may have low knot count, a low fines count, as well improved kink, curl and twist. The apparatus for carrying out the process may include a pretreatment station for supplying the treatment substance, a pulp feed device designed for pulp, a pulp feed device designed for pulp and foam suspensions, and/or a fiber separation station having a vacuum conveyor.

Claims (36)

1. A process for producing crosslinked, singulated pulp fibers comprising:

treating never-dried wet pulp received directly from a pulp mill with a crosslinker;

introducing said never-dried wet pulp directly from a pulp mill and air into a jet drier;

thereafter drying and crosslinking said pulp in said jet drier to form singulated pulp fibers; and

removing said pulp from said jet drier and separating said dried pulp fibers from said air in said jet drier, thereby producing a crosslinked singulated pulp fibers having knots, fines and accepts.

2. The process of claim 1 , wherein said crosslinker is selected from the group consisting of polyacrylic acid, glyoxal, malic acid, and tartaric acid.

3. The process of claim 1 , wherein said wet pulp is at least partially dewatered prior to introducing said pulp into said drier.

4. The process of claim 1 , wherein said wet pulp is further treated with a treatment substance to reduce the knot content of said pulp fibers, selected from the group consisting of a surfactant and a mineral particulate.

5. The process of claim 4 , wherein said treatment substance is a mineral particulate.

6. The process of claim 5 , wherein the knot count of said dried pulp fibers are less than or equal to 2%, the accepts in said dried pulp fibers are greater than or equal to 77%, and the fines in said dried pulp fibers are less than or equal to 21%.

7. The process of claim 5 , wherein said treatment substance is a surfactant.

8. The process of claim 4 , wherein said dried pulp fibers have a knot count less than 15%.

9. The process of claim 8 , wherein said dried pulp fibers have a knot count less than 10%.

10. The process of claim 8 , wherein said dried pulp fibers have a knot count less than 5%.

11. The process of claim 8 , wherein said dried pulp fibers have a knot count less than 2%.

12. The process of claim 7 , wherein the knot count of said dried pulp fibers are less than or equal to 5%, the accepts in said dried pulp fibers are greater than or equal to 80%, and the fines in said dried pulp fibers are less than or equal to 15%.

13. The process of claim 7 , wherein the knot count of said dried pulp fibers is less than or equal to 5%, the accepts in said dried pulp fibers are greater than or equal to 80%, and the fines in said dried pulp fibers are less than or equal to 13%.

14. The process of claim 7 , wherein the knot count of said dried pulp fibers is less than or equal to 5%, the accepts in said dried pulp fibers are greater than or equal to 85%, and the fines in said dried pulp fibers are less than or equal to 15%.

15. The process of claim 7 , wherein the knot count of said dried pulp fibers is less than or equal to 2%, the accepts in said dried pulp fibers are greater than or equal to 80%, and the fines in said dried pulp fibers are less than or equal to 15%.

16. The process of claim 1 , wherein said wet pulp is further treated with a substance selected from the group consisting of a hydrophobic material, a superplasticizer, a foam, a surfactant and a water reducing agent.

17. The process of claim 1 , wherein the knot count of said dried pulp fibers is less than 15%.

18. The process of claim 17 , wherein the knot count of said dried pulp fibers is less than 10%.

19. The process of claim 17 , wherein the knot count of said dried pulp fibers is less than 5%.

20. The process of claim 17 , wherein the knot count of said dried pulp fibers is less than 2%.

21. The process of claim 1 , wherein the knot count of said dried pulp fibers is less than or equal to 5%, the accepts in said dried pulp fibers are greater than or equal to 80%, and the fines in said dried pulp fibers are less than or equal to 15%.

22. The process of claim 1 , wherein the knot count of said dried pulp fibers is less than or equal to 5%, the accepts in said dried pulp fibers are greater than or equal to 80%, and the fines in said dried pulp fibers are less than or equal to 13%.

23. The process of claim 1 , wherein the knot count of said dried pulp fibers is less than or equal to 5%, the accepts in said dried pulp fibers are greater than or equal to 85%, and the fines in said dried pulp fibers are less than or equal to 15%.

24. The process of claim 1 , wherein the knot count of said dried pulp fibers is less than or equal to 2%, the accepts in said dried pulp fibers are greater than or equal to 80%, and the fines in said dried pulp fibers are less than or equal to 15%.

25. The process of claim 1 , wherein said supply pulp has a consistency of from 0.01% to 10% before introduction into said jet drier.

26. The process of claim 25 , wherein said supply pulp has a consistency of from 3% to 10% before introduction into said drier.

27. The process of claim 1 , wherein said singulated pulp is dried to a moisture content of 2 percent to 10 percent by weight.

28. A process for producing crosslinked, singulated pulp fibers comprising:

treating never-dried wet pulp received directly from a pulp mill with a crosslinker;

introducing air and said never-dried wet pulp directly from a pulp mill without mechanical defibering into a jet drier;

thereafter drying said pulp in said jet drier to form singulated pulp fibers; and

removing said pulp from said jet drier and separating said dried pulp fibers from said air in said jet drier, thereby producing a crosslinked singulated pulp fibers having knots, fines and accepts.

Assignments (3)
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Aug 5, 2019
From: WEYERHAEUSER NR COMPANY
To: INTERNATIONAL PAPER COMPANY
Reel/Frame 049964/0838 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Apr 21, 2009
From: WEYERHAEUSER COMPANY
To: WEYERHAEUSER NR COMPANY
Reel/Frame 022835/0233 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Jan 16, 2002
From: YANCEY, MICHAEL J.; WESTER, BRIAN; VRBANAC, MICHAEL D.; DEZUTTER, RAMON CHARLES
To: WEYERHAEUSER COMPANY
Reel/Frame 012517/0219 →