Process for ozone bleaching of oxygen delignified pulp while conveying the pulp through a reaction zone

• US 5,409,570 A
• Filed: 11/25/1992
• Issued: 04/25/1995
• Est. Priority Date: 02/15/1989
• Status: Expired due to Term

• Current Assignee: Union Camp Patent Holding, Inc.
• Original Assignee: Union Camp Patent Holding, Inc.
• Inventors: Rosen, Allen, Ali, Omar F., Gandek, Thomas P., Pikulin, Michael A., Friend, William H., White, David E., Eachus, Spencer W., Griggs, Bruce F., Terrett, Stuart T.
• Primary Examiner(s): Alvo, Steve
• Application Number:
  US07/981,467
• Time in Patent Office: 881 Days
• Field of Search: 162/57, 162/60, 162/65, 162/78, 162/29, 162/30, 162/30.1, 162/30.11, 162/88, 162/89, 162/76, 162/56, 162/5.19, 162/37, 162/72, 162/52, 162/237, 162/243, 162/90
• US Class Current: 162/40
• CPC Class Codes: B01F 27/0724 directly mounted on the rotating axis
• CPC Class Codes: D21C 9/10 Bleaching ; Apparatus therefor
• 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
• CPC Class Codes: D21C 9/163 with peroxides

Abstract

A process for delignifying and bleaching a lignocellulosic pulp without the use of elemental chlorine or chlorine-containing compounds by oxygen delignifying the pulp to a K No. of about 14 or less and a viscosity of greater than about 10 cps and thereafter further delignifying the partially delignified pulp by lifting, displacing and tossing the pulp in a radial direction while advancing it in an axial direction in a plug flow-like manner with an effective amount of ozone for a sufficient time to obtain a substantially delignified pulp having a K No. of about 6 or less, a viscosity of at least about 7 cps and a GE brightness of at least about 35. The substantially delignified pulp may then be brightened to a final product having a GE brightness of at least about 75, or alternately up to about 83 or more by contacting the ozonated pulp with chlorine dioxide or a peroxide compound. 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 the manufacture of a bleached pulp having a certain GE brightness and a certain strength as indicated by a certain viscosity which comprises:

chemically digesting a lignocelluloeic material to initially form a pulp;

oxygen delignifying the pulp to remove a substantial portion of the lignin therefrom, with the combination of the digesting and oxygen delignifying steps being conducted to form an intermediate pulp. having a specified amount of lignin and a specified viscosity; and

ozone delignifying the intermediate pulp with a gaseous mixture that contains ozone by adjusting the consistency of the pulp to a high consistency of above about 20%, adjusting the pH of the pulp to below about 4, and treating the pulp with an amount of the ozone containing gaseous mixture sufficient to remove a substantial portion, but not all, of the remaining lignin by intimately contacting and turbulently mixing the pulp particles with the gaseous mixture in a dynamic reaction zone by introducing the high consistency pulp into the reaction zone to fill the zone to at least about 10% by volume, dispersing the pulp substantially completely throughout the reaction zone while simultaneously conveying the pulp through the reaction zone in a plug flow-like manner at a dispersion index of about 7 or less thus exposing substantially all of the pulp to the ozone for reaction therewith for a sufficient time and at a temperature sufficient to allow access of the ozone to substantially all of the pulp for reaction therewith while the pulp advances through substantially all of the reaction zone, thus obtaining substantially uniform delignification of a significant portion of the pulp and forming a delignified pulp having a reduced amount of lignin and the certain strength, viscosity and GE brightness;

wherein the specified amount of lignin of the intermediate pulp is such that, after ozone delignification, the delignified pulp attains the certain GE brightness, and wherein the specified viscosity of the intermediate pulp is sufficiently high to permit the delignified pulp, after ozone delignification, to attain the certain strength as evidenced by the certain viscosity.

2. The process of claim 1 wherein the reaction zone is a horizontal chamber.

3. The process of claim 1 wherein the ozone delignification of the intermediate pulp is carried out by:

introducing the ozone containing gaseous mixture into the reaction zone for contact with the pulp; and

intimately contacting and mixing the pulp with the ozone by lifting, displacing and tossing the pulp in a radial direction to disperse the pulp and expose substantially all of the pulp to the gaseous bleaching agent while advancing the dispersed pulp axially through the reactor in a plug-flow like manner and at said dispersion index for a predetermined time to obtain substantially uniform bleaching of the pulp and to form a bleached pulp having the certain GE brightness, certain strength and certain viscosity.

4. The process of claim 1 wherein the ozone delignifying step comprises:

increasing the consistency of said intermediate pulp to at least about 28%;

comminuting the increased consistency pulp into discrete particles of a predetermined particle size having a sufficiently small diameter and a sufficiently low density to facilitate substantially complete penetration of a majority of the pulp particles by ozone gas without causing significant degradation of the cellulose components of the pulp; and

uniformly contacting said comminuted pulp particles and said ozone containing gaseous mixture during said turbulent mixing while the pulp is advanced through the reaction zone for a sufficient time to obtain substantially uniform delignification of a majority of the pulp particles.

5. The process of claim 1 which further comprises:

comminuting the pulp into pulp particles having a relatively low bulk density prior to introducing said pulp particles into the reaction zone; and

maintaining a substantially constant and predetermined fill level of said pulp particles in the reaction zone by initially advancing said relatively low bulk density pulp particles at a first rate thus increasing the low bulk density, and advancing said increased bulk density particles at a second rate less than said first rate.

6. The process of claim 1 wherein the oxygen delignification step comprises forming a low to medium consistency pulp;

treating the low to medium consistency pulp with an aqueous solution of an alkaline material for a predetermined time and at a predetermined temperature relative to the quantity of the alkaline material to substantially uniformly distribute the alkaline material throughout the low to medium consistency pulp;

raising the consistency of the pulp to a high consistency; and

subjecting the resulting high consistency pulp to high consistency oxygen delignification to obtain the intermediate pulp.

7. The process of claim 6 wherein the consistency of the pulp in the oxygen stage, prior to treatment with alkaline material, is reduced to less than about 5% by weight;

at least some of the alkaline material is applied to the high consistency pulp; and

at least a portion of the liquid removed from the consistency increasing step is directly recycled to the pulp treating step.

16. The process of claim 1 wherein the intermediate pulp has a K No. of about 14 or less and a viscosity of greater than about 10 cps;

the delignified pulp has a K No. of about 6 or less, a viscosity of greater than about 7 cps and a GE brightness of at least about 35%; and

the intermediate pulp is directed to ozone delignification without any intervening delignification or bleaching steps.

17. The process of claim 16 wherein the lignocellulosic material is a softwood and, after the oxygen step, the K No. is about 11 or less and the viscosity is greater than about 12 cps, while after the ozone step, the K No. is about 5 or less, the viscosity is greater than about 9 cps and the GE brightness is at least about 45%.

18. The process of claim 16 wherein the lignocellulosic material is a hardwood and, after the oxygen step, the K No. is about 9 or less and the viscosity is greater than about 12 cps, while after the ozone step, the K No. is about 5 or less, the viscosity is greater than about 9 cps and the GE brightness is at least about 55%.

19. The process of claim 1 which further comprises bleaching the delignified pulp after ozone delignification with a brightening agent to further increase the GE brightness of the pulp.

20. The process of claim 19 which further comprises combining the delignified pulp with an effective amount of alkaline material in an alkaline aqueous solution at a predetermined temperature, correlated to the amount of alkaline material combined, to solubilize a substantial portion of any lignin remaining in the bleached pulp;

and thereafter extracting a portion of the aqueous alkaline solution so as to remove substantially all of the solubilized lignin therefrom and form an extracted pulp.

21. The process of claim 19 wherein the brightening agent is a peroxide compound and which further comprises contacting said pulp with a sufficient amount of the peroxide compound with continuous mixing to raise the GE brightness thereof to at least about 75.

22. The process of claim 19 wherein the brightening agent is chlorine dioxide having a reduced amount of residual chlorine content and which further comprises contacting said pulp with a sufficient amount of the chlorine dioxide compound to raise the GE brightness thereof to at least about 80.

8. The process which further comprises:

oxygen delignifying the pulp by;

applying a first amount of alkaline material to brownstock pulp having a low consistency of less than about 5% by weight by combining the low consistency pulp with a sufficient quantity of alkaline material with uninterrupted mixing in a manner to ensure that all pulp fibers are exposed to the alkaline material to obtain a substantially uniform distribution of alkaline material throughout the pulp and then increasing the consistency of the alkaline material containing pulp to at least about 18% by weight to obtain high consistency pulp and to remove liquid while retaining the first amount of alkaline material substantially uniformly distributed throughout the high consistency pulp, said pulp fibers containing the alkaline material being directly passed from the combining step to the consistency increasing step;

applying a second amount of alkaline material onto the high consistency pulp to obtain a total amount of alkaline material on the pulp of at least about 0.8 to 7 percent by weight based on the oven dry weight of the pulp, wherein at least about 55% of the total amount of alkaline material is applied to the pulp during the alkaline material combining step; and

subjecting the increased consistency alkaline material containing 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 combined with alkaline material at low consistencies and form an intermediate pulp having a specified amount of lignin and having a specified viscosity.

9. The process of claim 8 wherein the total amount of alkaline material is applied upon the low consistency pulp.

10. The process of claim 8 wherein the consistency of the pulp which is combined with the aqueous alkaline solution prior to oxygen delignification ranges between about 1 and 4.5% by weight, the consistency of the pulp is increased to at least about 25% by weight prior to the oxygen delignification step and recycing a significant portion of the removed liquid can be directly to the alkaline material combining step.

11. The process of claim 8 wherein, prior to the alkaline material combining step, the pulp has a consistency which is equal to or greater than that of the high consistency pulp which is to be formed so that substantially all removed liquid can be directly recycled to the alkaline material combining step.

12. The process of claim 8 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 and increasing the consistency of the pulp to at least about 20% by weight prior to ozone delignification.

13. The process of claim 12 wherein the ozone delignification step comprises acidifying the pulp and treating the acidified pulp 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 pulp 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 substantially all of the pulp for reaction therewith while advancing the pulp through the reaction zone to obtain a substantially uniformly delignified pulp having said certain strength, viscosity and GE brightness.

14. The process of claim 8 wherein the pulp is unbleached softwood pulp and the amount of alkaline material applied to said pulp is between about 1.5 and 4 percent by weight.

15. The process of claim 8 wherein the pulp is unbleached hardwood pulp and the amount of alkaline material applied to said pulp is between about 1 and 3.8 percent by weight.