High efficiency fiber bleaching process

Patent metadata

Field	Value
Publication number	US-11840805-B2
Application number	US-202318159700-A
Country	US
Kind code	B2
Filing date	Jan 26, 2023
Priority date	Sep 17, 2019
Publication date	Dec 12, 2023
Grant date	Dec 12, 2023

Abstract

A high efficiency bleaching method for cellulosic pulp includes: (a) providing a charge of aqueous cellulosic pulp to a bleaching vessel at a consistency of from 10% to 30% along with a peroxy bleaching agent and an alkaline agent effective to adjust pH of the charge to 9.5 to 12.5; and (b) bleaching the aqueous cellulosic pulp in the bleaching vessel while maintaining a bleaching temperature of from 110° F. (43° C.) to 135° F. (57° C.) and a pH of the charge from 9.5 to 12.5 for an extended bleaching retention time. The bleaching method is advantageously used to bleach low brightness recycle pulp, and/or as part of a multistage process with bleaching stages of lesser duration, and/or as a high peroxy efficiency, low dose bleaching process or in connection with concurrently storing and bleaching pulp.

First claim

What is claimed is:

1. A multi-stage bleaching process for aqueous cellulosic pulp comprising:
(a) bleaching the aqueous cellulosic pulp in an extended duration bleaching stage including: (i) providing the aqueous cellulosic pulp to the extended duration bleaching stage at a consistency of from 10% to 30% along with a peroxy bleaching agent and an alkaline agent effective to adjust pH of the charge to 9.5 to 12.5; (ii) bleaching the aqueous cellulosic pulp in a bleaching vessel while maintaining an extended duration bleaching temperature of from 43° C. to 57° C. and a pH of the charge from 9.5 to 12.5 for a bleaching retention time in the extended duration bleaching stage of at least 10 hours; and
(b) followed by a Y bleaching stage of lesser duration or a P bleaching stage of lesser duration or both, wherein the Y bleaching stage comprises bleaching with a reductive bleaching agent, for a retention time of from 5 minutes to 3.5 hours while maintaining a bleaching temperature of from 50° C. to 110° C. and the P bleaching stage comprises bleaching with a peroxy bleaching agent, for a retention time of from 5 minutes to 3.5 hours while maintaining a bleaching temperature of from 50° C. to 110° C.,

and wherein the aqueous cellulosic pulp is recycle pulp having an ISO brightness of from 40 to 65 prior to bleaching.

2. The process according to claim 1 , wherein the extended duration bleaching temperature is from 48° C. to 55° C.

3. The process according to claim 1 , wherein the bleaching retention time in the extended duration bleaching stage is from 10 hours to 20 hours.

4. The process according to claim 1 , wherein the extended duration bleaching stage is carried out at a pH of from 10 to 11.

5. The process according to claim 1 , wherein the extended duration bleaching stage is carried out with the peroxy bleaching agent applied to the aqueous cellulosic pulp in an amount of from 0.1 kg-moles bleaching agent/metric ton of dried pulp to 2.4 kg-moles bleaching agent/metric ton of dried pulp.

6. The process according to claim 1 , wherein the extended duration bleaching stage is carried out with the peroxy bleaching agent applied to the aqueous cellulosic pulp in an amount of from 0.15 kg-moles bleaching agent/metric ton of dried pulp to 2 kg-moles bleaching agent/metric ton of dried pulp.

7. The process according to claim 1 , wherein the extended duration bleaching stage is carried out with the peroxy bleaching agent applied to the aqueous cellulosic pulp in an amount of from 0.2 kg-moles bleaching agent/metric ton of dried pulp to 1.5 kg-moles bleaching agent/metric ton of dried pulp.

8. The process according to claim 1 , wherein the peroxy bleaching agent utilized in the extended duration bleaching stage is hydrogen peroxide applied to the aqueous cellulosic pulp in an amount of from 0.35% on dried pulp to 4% on dried pulp.

9. The process according to claim 1 , wherein the peroxy bleaching agent utilized in the extended duration bleaching stage is hydrogen peroxide applied to the aqueous cellulosic pulp in an amount of from 0.35% on dried pulp to 6% on dried pulp.

10. The process according to claim 1 , wherein the peroxy bleaching agent utilized in the extended duration bleaching stage is hydrogen peroxide applied to the aqueous cellulosic pulp in an amount of from 2% on dried pulp to 7% on dried pulp.

11. The process according to claim 1 , wherein the Y bleaching stage of lesser duration or the P bleaching stage of lesser duration or both are carried out for a retention time of from 5 minutes to 2.5 hours.

12. The process according to claim 1 , wherein the Y bleaching stage of lesser duration or the P bleaching stage of lesser duration or both includes a Y bleaching stage.

13. The process according to claim 1 , wherein the Y bleaching stage of lesser duration or the P bleaching stage of lesser duration or both includes a P bleaching stage.

14. A high efficiency bleaching method for cellulosic pulp comprising:
(a) providing a charge of aqueous cellulosic pulp to a bleaching vessel at a consistency of from 10% to 30% along with a peroxy bleaching agent and an alkaline agent effective to adjust pH of the charge to 9.5 to 12.5; and
(b) bleaching the aqueous cellulosic pulp in the bleaching vessel while maintaining a bleaching temperature of from 43° C. to 57° C. and a pH of the charge from 9.5 to 12.5 for a bleaching retention time of at least 10 hours such that from 0.1 kg-moles bleaching agent/metric ton of dried pulp to 2.4 kg-moles bleaching agent/metric ton of dried pulp are consumed in bleaching the aqueous cellulosic pulp in this step (b),

and wherein the aqueous cellulosic pulp is recycle pulp having an ISO brightness of from 40 to 65 prior to bleaching;
(c) followed by a Y bleaching stage or a P bleaching stage or both, wherein the Y bleaching stage comprises bleaching with a reductive bleaching agent, for a retention time of from 5 minutes to 3.5 hours while maintaining a bleaching temperature of from 50° C. to 110° C. and the P bleaching stage comprises bleaching with a peroxy bleaching agent, for a retention time of from 5 minutes to 3.5 hours while maintaining a bleaching temperature of from 50° C. to 110° C.

15. The high efficiency bleaching method according to claim 14 , wherein the bleaching of step (b) is carried out with the peroxy bleaching agent applied to the aqueous cellulosic pulp such that from 0.2 kg-moles bleaching agent/metric ton of dried pulp to 1.5 kg-moles bleaching agent/metric ton of dried pulp are consumed in bleaching the aqueous cellulosic pulp in step (b).

16. The high efficiency bleaching method according to claim 14 , wherein the peroxy bleaching agent utilized in the bleaching of step (b) is hydrogen peroxide applied to the aqueous cellulosic pulp such that from 0.35% hydrogen peroxide on dried pulp to 8% hydrogen peroxide on dried pulp are consumed in bleaching the aqueous cellulosic pulp in step (b).

17. The high efficiency bleaching method according to claim 14 , wherein the peroxy bleaching agent utilized in the bleaching of step (b) is hydrogen peroxide applied to the aqueous cellulosic pulp such that from 0.35% hydrogen peroxide on dried pulp to 6% hydrogen peroxide on dried pulp are consumed in bleaching the aqueous cellulosic pulp in step (b).

18. The high efficiency bleaching method according to claim 14 , wherein the peroxy bleaching agent utilized in the bleaching of step (b) is hydrogen peroxide applied to the aqueous cellulosic pulp such that from 0.35% hydrogen peroxide on dried pulp to 4% hydrogen peroxide on dried pulp are consumed in bleaching the aqueous cellulosic pulp in step (b).

19. The high efficiency bleaching method according to claim 14 , wherein the peroxy bleaching agent utilized in the bleaching of step (b) is hydrogen peroxide applied to the aqueous cellulosic pulp such that from 0.35% hydrogen peroxide on dried pulp to 3% hydrogen peroxide on dried pulp are consumed in bleaching the aqueous cellulosic pulp in step (b).

20. The high efficiency bleaching method according to claim 14 , wherein the peroxy bleaching agent utilized in bleaching of step (b) is hydrogen peroxide applied to the aqueous cellulosic pulp such that from 0.5% hydrogen peroxide on dried pulp to 2.75% hydrogen peroxide on dried pulp are consumed in bleaching the aqueous cellulosic pulp in step (b).

Assignees

• Gpcp Ip Holdings Llc

Inventors

• Lee Jeffrey A

Classifications

• D21C9/16 Primary

  with per compounds · CPC title

• D21C5/022

  Chemicals therefor · CPC title

• D21C9/1057

  Multistage, with compounds cited in more than one sub-group D21C9/10, D21C9/12, D21C9/16 · CPC title

• D21C9/1063

  with compounds not otherwise provided for, e.g. activated gases · CPC title

• D21C9/1084

  with reducing compounds · CPC title