Process for producing a pulp suitable for papermaking from nonwood fibrous materials

• US 6,302,997 B1
• Filed: 08/30/1999
• Issued: 10/16/2001
• Est. Priority Date: 08/30/1999
• Status: Expired due to Term

• Current Assignee: Hurterconsult Incorporated, North Carolina State University (University of North Carolina System)
• Original Assignee: Hurterconsult Incorporated, North Carolina State University (University of North Carolina System)
• Inventors: Hurter, Robert W., Byrd, Medwick V. Jr.
• Primary Examiner(s): NGUYEN, TAN D
• Application Number:
  US09/385,154
• Time in Patent Office: 778 Days
• Field of Search: 162/65, 162/78, 162/99, 162/80, 162/90, 162/91, 162/96, 162/97, 162/98, 162/94, 162/95
• US Class Current: 162/65
• CPC Class Codes: D21C 3/02 with inorganic bases or alkaline reacting compounds, e.g. sulfate processes
• CPC Class Codes: D21C 5/00 Other processes for obtaining cellulose, e.g. cooking cotton linters obtaining fibres for spinning D01C; Processes characterised by the choice of cellulose-containing starting materials
• CPC Class Codes: D21C 9/1005 Pretreatment of the pulp, e.g. degassing the pulp
• CPC Class Codes: D21C 9/153 with ozone

Abstract

A process for producing a pulp suitable for papermaking from a nonwood fiber source material. Representative nonwood fiber source materials include corn stover and wheat straw. The process includes the steps of providing a nonwood fiber source material; digesting the nonwood fiber source material with an alkaline pulping solution at at least about atmospheric pressure; reducing the pH of the nonwood fiber source material to an acidic pH with an acid solution; treating the nonwood fiber source material having an acidic pH with ozone; and treating the nonwood fiber source material with a bleaching solution to form a papermaking pulp.

Claims

1. A process for producing a pulp suitable for making paper from a nonwood fiber source material, the process comprising:

(a) providing a nonwood fiber source material;

(b) extracting the nonwood fiber source material with an alkaline pulping solution at at least about atmospheric pressure;

(c) reducing the pH of the nonwood fiber source material pH formed in step (b) to an acidic pH with an acid solution;

(d) treating the nonwood fiber source material having an acidic pH formed in step (c) with ozone; and

(e) treating the nonwood fiber source material of step (d) with a bleaching solution comprising a bleaching agent different from the ozone of step (d) to form a papermaking pulp, wherein the pulp has a freeness level of at least 400 mL CSF or greater and a brightness level of at least 70% ISO.

2. The method of claim 1, wherein the nonwood fiber source material is selected from a group comprising corn stover, kenaf, industrial hemp, sisal, rye grass straw, wheat straw, rice straw, bagasse, hesperaloe, flax straw and combinations thereof.

3. The method of claim 2, wherein the nonwood fiber source material is corn stover, wheat straw, bagasse or combinations thereof.

4. The process of claim 1, wherein said extracting the nonwood fiber source material with an alkaline pulping solution occurs at a temperature ranging from about 80°

C. to about 120°

C.

5. The process of claim 1, wherein said alkaline pulping solution comprises an alkaline hydroxide pulping solution.

6. The process of claim 5, wherein alkaline hydroxide is present in said alkaline hydroxide pulping solution in a dosage ranging from about 10% weight to about 30% weight on ODF.

7. The process of claim 5, wherein alkaline hydroxide in said alkaline hydroxide pulping solution is selected from the group consisting of sodium hydroxide, potassium hydroxide, ammonium hydroxide, calcium hydroxide and combinations thereof.

8. The process of claim 1, wherein the pH is reduced in step (c) to a pH within a range of about 1 to about 3.

9. The process of claim 1, wherein said reducing the pH of the nonwood fiber source material to an acidic pH with an acid solution occurs at a temperature ranging from about 50°

C. to about 70°

C. and for a time ranging from about 20 minutes to about 30 minutes.

10. The process of claim 1, wherein the acid solution comprises an acid selected from the group consisting of a mineral acid, an organic acid and combinations thereof.

11. The process of claim 10, wherein the acid is selected from the group consisting of sulfuric acid, nitric acid, phosphoric acid, acetic acid and combinations thereof.

12. The process of claim 1, wherein the acid solution further comprises a chelating agent.

13. The process of claim 1, wherein the ozone is present in a dosage ranging from about 0.4% weight to about 1% weight on ODF.

14. The process of claim 1, wherein said treating the nonwood fiber source material having an acidic pH with ozone produces a pulp having a Kappa number of at least as low as 5.

15. The process of claim 1, wherein said treating the nonwood fiber source material with a bleaching solution occurs at a temperature of at least about 100°

C. and said bleaching solution comprises an alkaline peroxide bleaching solution.

16. The process of claim 15, wherein the temperature is a temperature ranging from about 105°

C. to about 110°

C.

17. The process of claim 15, wherein said alkaline peroxide bleaching solution comprises sodium hydroxide, hydrogen peroxide, magnesium sulfate, sodium silicate and a chelant.

18. The process of claim 1, wherein the bleaching solution comprises a chlorine dioxide or other chlorine-based bleaching solution.

19. The process of claim 1, further comprising cleaning the nonwood fiber source material with at least one filtering screen after the step of treating the nonwood fiber source material having an acidic pH with ozone and before the step of treating the nonwood fiber source material with a bleaching solution.

20. The process of claim 1, further comprising adjusting the nonwood fiber source material to a consistency of at least about 35% after the step of reducing the pH of the nonwood fiber source material to an acidic pH with an acid solution, and then diluting the nonwood fiber source material to a lower consistency with or without washing the nonwood fiber source material prior to the step of treating the nonwood fiber source material having an acidic pH with ozone.

21. The process of claim 20, wherein the consistency of the nonwood fiber source material ranges from about 3% to about 10%.

22. The process of claim 1, further comprising diluting the nonwood fiber source material having an acidic pH to a consistency ranging from about 1% to about 10%.

23. The process of claim 1, wherein the papermaking pulp has a brightness level of at least 80% ISO.

24. The process of claim 1, wherein the papermaking pulp has a freeness level of at least 550 mL CSF or greater.

25. The process of claim 1, wherein the papermaking pulp has a Kappa value of at least as low as 5.

26. The process of claim 25, wherein the papermaking pulp has a Kappa value ranging downwardly from about 5 to about 1.

27. A process for producing a pulp suitable for making paper from a nonwood fiber source material, the process comprising the sequential steps of:

(a) providing a nonwood fiber source material;

(b) extracting the nonwood fiber source material with an alkaline pulping solution for about 1 to about 90 minutes at a pressure ranging from about atmospheric pressure to about 30 psig and at a temperature ranging from about ambient temperature to about 150°

C.;

(c) treating the nonwood fiber source material with an acid solution at a temperature ranging from ambient temperature to about 90°

C. and for a time ranging from about 30 to about 60 minutes to reduce the pH to an acidic pH;

(d) dewatering the nonwood fiber source material to a consistency of at least about 35% and then diluting the nonwood fiber source material to a lower consistency ranging from about 1% to about 10%;

(e) treating the nonwood fiber source material having an acidic pH with ozone; and

(f) treating the nonwood fiber source material with a bleaching comprising a bleaching agent different from the ozone of step (e) to form a papermaking pulp having a Kappa value of at least as low as 5, a freeness level of at least 400 mL CSF or greater and a brightness level of at least 70% ISO.

28. The method of claim 27, wherein the nonwood fiber source material is selected from a group comprising corn stover, kenaf, industrial hemp, sisal, rye grass straw, wheat straw, rice straw, bagasse, hesperaloe, flax straw and combinations thereof.

29. The method of claim 28, wherein the nonwood fiber source material is corn stover, wheat straw, bagasse or combinations thereof.

30. The process of claim 27, wherein said digesting the nonwood fiber source material with an alkaline pulping solution occurs at a temperature ranging from about 80°

C. to about 120°

C. and for a time ranging from about 30 minutes to about 60 minutes.

31. The process of claim 27, wherein said alkaline pulping solution comprises an alkaline hydroxide pulping solution.

32. The process of claim 31, wherein alkaline hydroxide is present in said alkaline hydroxide pulping solution in a dosage ranging from about 10% weight to about 30% weight on ODF.

33. The process of claim 31, wherein said alkaline hydroxide pulping solution comprises an alkaline hydroxide selected from the group consisting of sodium hydroxide, potassium hydroxide, ammonium hydroxide, calcium hydroxide and combinations thereof.

34. The process of claim 27, wherein the pH is reduced in step (c) to a pH ranging from about 1 to about 3.

35. The process of claim 27, wherein said treating of the nonwood fiber source material with an acid solution occurs at a temperature ranging from about 50°

C. to about 70°

C. and for a time ranging from about 20 minutes to about 30 minutes.

36. The process of claim 27, wherein the acid solution comprises an acid selected from the group consisting of a mineral acid, an organic acid and combinations thereof.

37. The process of claim 36, wherein the acid is selected from the group consisting of sulfuric acid, nitric acid, phosphoric acid, acetic acid and combinations thereof.

38. The process of claim 27, wherein the acid solution further comprises a chelating agent.

39. The process of claim 27, wherein further comprising adjusting the nonwood fiber source material to a consistency of at least about 35% after the step of reducing the pH of the nonwood fiber source material to an acidic pH with an acid solution, and then diluting the nonwood fiber source material to a lower consistency with or without washing the nonwood fiber source material prior to the step of treating the nonwood fiber source material having an acidic pH with ozone.

40. The process of claim 27, wherein the consistency of the nonwood fiber source material ranges from about 3% to about 10%.

41. The process of claim 27, wherein the ozone is present in a dosage ranging from about 0.4% weight to about 1% weight on ODF.

42. The process of claim 27, wherein said treating the nonwood fiber source material having an acidic pH with ozone produces a pulp having a Kappa number of at least as low as 5.

43. The process of claim 27, wherein said treating the nonwood fiber source material with a bleaching solution occurs at a temperature of at least about 100°

C. and said bleaching solution comprises an alkaline peroxide bleaching solution.

44. The process of claim 43, wherein the temperature is a temperature ranging from about 105°

C. to about 110°

C.

45. The process of claim 43, wherein said alkaline peroxide bleaching solution comprises sodium hydroxide, hydrogen peroxide, magnesium sulfate, sodium silicate and a chelant.

46. The process of claim 27, wherein the bleaching solution comprises a chlorine dioxide or other chlorine-based bleaching solution.

47. The process of claim 27, further comprising the step of cleaning the nonwood fiber source material with at least one filtering screen after the step of treating the nonwood fiber source material having an acidic pH with ozone and before the step of treating the nonwood fiber source material with a bleaching solution.

48. The process of claim 27, wherein the papermaking pulp has a brightness level of at least 80% ISO.

49. The process of claim 27, wherein the papermaking pulp has a freeness level of at least 550 mL CSF or greater.

50. The process of claim 27, wherein the papermaking pulp has a Kappa value ranging downwardly from about 5 to about 1.

51. A process for producing a pulp suitable for making paper from a nonwood fiber source material, the process comprising the sequential steps of:

(a) providing a nonwood fiber source material;

(b) extracting the nonwood fiber source material with an alkaline hydroxide pulping solution for about 30 to about 60 minutes at a pressure ranging from about atmospheric pressure to about 30 psig and at a temperature ranging from about 80°

C. to about 120°

C., wherein alkaline hydroxide in the alkaline hydroxide pulping solution is present in a dosage of ranging from about 10% weight to about 30% weight on ODF;

(c) reducing the pH of the nonwood fiber source material to a pH ranging from about 1 to about 3 with an acid solution at a temperature ranging from about 50°

C. to about 70°

C. and for a time ranging from about 20 minutes to about 30 minutes;

(d) dewatering the nonwood fiber source material to a consistency of at least about 35% and then diluting the nonwood fiber source material to a lower consistency ranging from about 1% to about 10%;

(e) treating the nonwood fiber source material having an acidic pH with ozone at about ambient temperature for about 5 to about 15 minutes, wherein the ozone is present in a dosage ranging from about 0.4% weight to about 1% weight on ODF;

(f) cleaning the nonwood fiber source material with at least one filtering screen; and

(g) treating the nonwood fiber source material with a bleaching solution comprising a bleaching agent different from the ozone of step (e) at a temperature ranging from about 70°

C. to about 110°

C. to form a papermaking pulp having a Kappa value of at least as low as 5, a freeness level of at least 400 mL CSF or greater and a brightness level of at least 80% ISO.

52. The method of claim 51, wherein the nonwood fiber source material is selected from a group comprising corn stover, kenaf, industrial hemp, sisal, rye grass straw, wheat straw, rice straw, bagasse, hesperaloe, flax straw and combinations thereof.

53. The method of claim 52, wherein the nonwood fiber source material is corn stover, wheat straw, bagasse or combinations thereof.

54. The process of claim 51, wherein said alkaline hydroxide solution comprises an alkaline hydroxide selected from the group consisting of sodium hydroxide, potassium hydroxide, ammonium hydroxide, calcium hydroxide and combinations thereof.

55. The process of claim, 51, wherein the acid solution comprises an acid selected from the group consisting of a mineral acid, an organic acid and combinations thereof.

56. The process of claim 55, wherein the acid is selected from the group consisting of sulfuric acid, nitric acid, phosphoric acid, acetic acid and combinations thereof.

57. The process of claim 51, wherein the acid solution further comprises a chelating agent.

58. The process of claim 51, further comprising adjusting the nonwood fiber source material to a consistency of at least about 35% after the step of reducing the pH of the nonwood fiber source material to an acidic pH with an acid solution, and then diluting the nonwood fiber source material to a lower consistency with or without washing the nonwood fiber source material prior to the step of treating the nonwood fiber source material having an acidic pH with ozone.

59. The process of claim 51, wherein the consistency of the nonwood fiber source material ranges from about 3% to about 10%.

60. The process of claim, 51, wherein said treating the nonwood fiber source material having an acidic pH with ozone produces a pulp having a Kappa number of at least as low as 5.

61. The process of claim 51, wherein said treating the nonwood fiber source material with a bleaching solution occurs at a temperature of at least about 100°

C. and said bleaching solution comprises an alkaline peroxide bleaching solution.

62. The process of claim 61, wherein the temperature is a temperature ranging from about 105°

C. to about 110°

C.

63. The process of claim 61, wherein said alkaline peroxide bleaching solution comprises sodium hydroxide, hydrogen peroxide, magnesium sulfate, sodium silicate and a chelant.

64. The process of claim 51, wherein the bleaching solution comprises a chlorine dioxide or other chlorine-based bleaching solution.