Process for high consistency oxygen delignification followed by ozone relignification

• US 5,188,708 A
• Filed: 08/26/1991
• Issued: 02/23/1993
• Est. Priority Date: 02/15/1989
• Status: Expired due to Fees

• Current Assignee: Union Camp Patent Holding, Inc.
• Original Assignee: Union Camp Patent Holding, Inc.
• Inventors: Gandek, Thomas P., Pikulin, Michael A., Griggs, Bruce F., Rosen, Allen
• Primary Examiner(s): ALVO, MARC S
• Application Number:
  US07/751,359
• Time in Patent Office: 547 Days
• Field of Search: 162/72, 162/76, 162/65, 162/78, 162/88, 162/89, 162/56, 162/57, 162/40, 162/71, 162/60
• US Class Current: 162/40
• CPC Class Codes: D21C 9/1005 Pretreatment of the pulp, e.g. degassing the pulp
• CPC Class Codes: D21C 9/1057 Multistage, with compounds cited in more than one sub-group D21C9/10, D21C9/12, D21C9/16
• CPC Class Codes: D21C 9/147 with oxygen or its allotropic modifications D21C9/16 takes precedence
• CPC Class Codes: D21C 9/153 with ozone

Abstract

A process for delignifying and bleaching a lignocellulosic pulp without the use of elemental chlorine by partially delignifying the pulp to a K No. of about 10 or less and a viscosity of greater than about 13 cps; and further delignifying the partially delignified pulp with an effective amount of ozone for a sufficient time to obtain a substantially delignified pulp having a K No. of about 5 or less, a viscosity of greater than about 10, and a GE brightness of at least about 50%. The substantially delignified pulp may be brightened by the addition of a bleaching agent such as chlorine dioxide or a peroxide to obtain a final product having a GE brightness of at least about 65%, preferably above 70% to as high as 90%. Because of the absence of elemental chlorine in this sequence, filtrate from all stages but the chlorine dioxide stage (if used) can be recovered without sewering. Major environmental improvements are thus achieved.

Claims

1. A process for delignifying and bleaching a lignocellulosic material which comprises:

forming a brownstock pulp having a K No. of from about 10-24 by Kraft pulping, Kraft-AQ pulping or extended delignification of a lignocellulosic material;

decreasing the consistency of said pulp to about 1 to 4.5% by weight;

treating the decreased consistency pulp with a quantity of alkaline material in an aqueous alkaline solution having a concentration of alkaline material of between about 20 and 120 g/l by uninterrupted mixing for a time of between about 1 and 15 minutes such that the concentration of alkaline material in the decreased consistency pulp during this treating step ranges from about 6.5 to 13 g/l, so as to complete a substantially uniform distribution of the alkaline material throughout the pulp;

increasing the consistency of the alkaline treated pulp to between about 20 to 35% by weight to generate pressate while retaining at least about 1.4% by weight based on oven dry pulp of alkaline material on the increased consistency pulp, said pulp fibers containing the alkaline material being directly passed from the combining step to the consistency increasing step;

recycling a substantial portion of the pressate to the pulp treating step; and

subjecting the increased consistency pulp to high consistency oxygen delignification to obtain enhanced delignification of the pulp without a corresponding decrease in pulp viscosity compared to pulp which is not treated with alkaline material at low consistencies;

directing the partially delignified pulp to ozone delignification without any intervening delignification or bleaching steps;

further delignifying said oxygen delignified pulp with an effective amount of ozone for a sufficient time to obtain a substantially delignified pulp having a second K No. of about 5 or less, a second viscosity of greater than about 10 cps and a GE brightness of at least about 50% prior to any additional bleaching steps;

combining the substantially delignified pulp with an effective amount of alkaline material in an aqueous alkaline solution for a predetermined time and at a predetermined temperature correlated to the quantity of alkaline material to solubilize a substantial portion of any lignin which remains in the pulp;

extracting a portion of aqueous alkaline solution so as to remove substantially all of the solubilized lignin therefrom and form a substantially lignin-free pulp; and

bleaching the substantially lignin-free pulp to raise the GE brightness thereof to at least about 70%.

2. The process of claim 1 wherein the GE brightness is raised to at least about 80%.

3. The process of claim 1 wherein the GE brightness is raised to at least about 90%.

4. The process of claim 1 which comprises decreasing the K No. of the increased consistency pulp by at least about 60% during the oxygen delignification step without significantly damaging the cellulose components of the pulp.

5. The process of claim 1 wherein the substantially lignin-free pulp is bleached with chlorine dioxide or a peroxide.

6. The process of claim 5 wherein the peroxide is hydrogen peroxide.

7. The process of claim 1 which further comprises adding a chelating agent to said pulp prior to ozone delignification to render metal ions substantially non-reactive to ozone.

8. The process of claim 7 wherein the chelating agent is DTPA, EDTA or oxalic acid.

9. The process of claim 1 which further comprises adjusting the pH of the pulp to a range of about 1 to 4 by adding to the pulp a sufficient quantity of an acidic material prior to ozone delignification.

10. The process of claim 1 which further comprises increasing the consistency of the pulp to between about 25-50% by weight prior to ozone delignification.

11. The process of claim 10 wherein the consistency of the pulp is increased to between about 35-45% by weight prior to ozone delignification.

12. The process of claim 1 which comprises comminuting said pulp to a diameter of less than about 5 mm after oxygen delignification and prior to ozone delignification.

13. The process of claim 1 which further comprises maintaining the pulp at a temperature of less than about 120°

F. during ozone delignification.

14. The process of claim 1 wherein the ozone is provided by a mixture comprising ozone and oxygen.

15. The process of claim 14 wherein the ozone concentration in the mixture is between about 1 and 8 percent by volume.

16. The process of claim 1 wherein the ozone is provided by a mixture of ozone and air.

17. The process of claim 16 wherein the ozone concentration is between about 1 and 4 percent by volume.

18. The process of claim 1 which comprises advancing the partially delignified pulp during the ozone delignification step in a manner which subjects substantially all the pulp to ozone.

19. The process of claim 18 which comprises introducing the ozone countercurrently to the advancing pulp.

20. The process of claim 18 which comprises introducing the ozone cocurrently with the advancing pulp.

21. The process of claim 1 wherein the ozone delignification step comprises treating the particles with a gaseous mixture containing ozone in an amount sufficient to remove a substantial portion, but not all, of the lignin remaining in the pulp by intimately contacting and turbulently mixing the discrete particles with the ozone containing gaseous mixture in a dynamic reaction zone for a sufficient time and at a temperature sufficient to allow access of the ozone to surfaces of the pulp particles for reaction therewith while advancing the pulp particles through the reaction zone to obtain a substantially uniformly delignified pulp having said second K No., second viscosity and brightness.

22. The process of claim 1 wherein the ozone delignification step comprises increasing the consistency of the oxygen delignified pulp to at least about 28%, adjusting the pH of the pulp to below 4, forming discrete pulp particles of a size having a sufficiently small diameter and a sufficiently low density to facilitate substantially complete penetration of a majority of the particles by ozone gas, and intimately contacting and turbulently mixing the pulp particles with an ozone containing gaseous mixture having an amount of ozone sufficient to remove a substantial portion, but not all, of the lignin remaining in the pulp in a dynamic reaction zone for a sufficient time to allow access of the ozone gas to surfaces of the pulp particles for reaction therewith while the particles advance through the reaction zone, thus obtaining substantially uniform delignification throughout the pulp particles and said second K No., second viscosity and brightness.

23. A process for delignifying and bleaching lignocellulosic material which comprises:

forming an unbleached brownstock pulp having a K No. of from about 10-24 by Kraft pulping, Kraft-AQ pulping or extended delignification of a lignocellulosic material;

decreasing the consistency of said pulp to about 1 to 4.5% by weight;

uniformly mixing the decreased consistency pulp with a quantity of alkaline material in an aqueous alkaline solution having a concentration of alkaline material of between about 20 and 120 g/l without interruption for a time of between about 1 and 15 minutes such that the concentration of alkaline material in the decreased consistency pulp during this mixing step ranges from about 6.5 to 13 g/l, so as to complete a substantially uniform distribution of the alkaline material throughout the pulp;

increasing the consistency of the alkaline treated pulp after completion of the mixing step to between about 20 to 35% by weight by removing liquid to form high consistency brownstock while retaining at least about 1.4 percent by weight based on oven dry pulp of alkaline material on the increased consistency pulp, said pulp fibers containing the alkaline material being directly passed from the low consistency pulp mixing step to the consistency increasing step;

recycling substantially all of the liquid removed from the pulp in the consistency increasing step to the low consistency pulp mixing step;

subjecting the increased consistency pulp to high consistency oxygen delignification to obtain enhanced delignification of the pulp without a corresponding decrease in pulp viscosity compared to pulp which is not treated with alkaline material at low consistencies, to form a partially delignified pulp having a first K No. of about 10 or less and a first viscosity of greater than about 13 cps;

directing the partially delignified pulp to ozone delignification without any intervening delignification or bleaching steps;

further delignifying said oxygen delignified pulp with an effective amount of ozone for a sufficient time to obtain a substantially delignified pulp having a second K No. of about 5 or less, a second viscosity of greater than about 10 cps and a GE brightness of at least about 50% prior to any additional bleaching steps;

combining the substantially delignified pulp with an effective amount of alkaline material in an aqueous alkaline solution for a predetermined time and at a predetermined temperature correlated to the quantity of alkaline material to solubilize a substantial portion of any lignin which remains in the pulp;

extracting a portion of aqueous alkaline solution so as to remove substantially all of the solubilized lignin therefrom and form a substantially lignin-free pulp; and

bleaching the substantially lignin-free pulp to raise the GE brightness thereof to at least about 70%.

24. The process of claim 23 wherein the ozone delignification step comprises treating the particles with a gaseous mixture containing ozone in an amount sufficient to remove a substantial portion, but not all, of the lignin remaining in the pulp by intimately contacting and turbulently mixing the discrete particles with the ozone containing gaseous mixture in a dynamic reaction zone for a sufficient time and at a temperature sufficient to allow access of the ozone to surfaces of the pulp particles for reaction therewith while advancing the pulp particles through the reaction zone to obtain a substantially uniformly delignified pulp having said second K No., second viscosity and brightness.

25. The process of claim 23 wherein the ozone delignification step comprises increasing the consistency of the oxygen delignified pulp to at least about 28%, adjusting the pH of the pulp to below 4, forming discrete pulp particles of a size having a sufficiently small diameter and a sufficiently low density to facilitate substantially complete penetration of a majority of the particles by ozone gas, and intimately contacting and turbulently mixing the pulp particles with an ozone containing gaseous mixture having an amount of ozone sufficient to remove a substantial portion, but not all, of the lignin remaining in the pulp in a dynamic reaction zone for a sufficient time to allow access of the ozone gas to surfaces of the pulp particles for reaction therewith while the particles advance through the reaction zone, thus obtaining substantially uniform delignification throughout the pulp particles and said second K No., second viscosity and brightness.