Process for improving chlorine dioxide bleaching of pulp
View Patent ↗The invention is directed to a method for increasing brightness of pulp, wherein the method includes: contacting a pulp slurry with chlorine dioxide in a final D (ClO 2 ) bleaching stage; and adding a brightening additive to the final D bleaching stage after at least a portion of the chlorine dioxide has been consumed, in an amount sufficient to increase brightness of the pulp; wherein the brightening additive is an inorganic compound chosen from hypochlorous acid, one or more precursor compounds that form hypochlorous acid in said final D bleaching stage, or a mixture thereof.
1. A method for increasing brightness of pulp, said method comprising:
a) contacting a pulp slurry with chlorine dioxide in a final D (ClO 2 ) bleaching stage having a pre-selected bleaching time;
b) adding a brightening additive to said final D bleaching stage after 60% of the final D stage has been completed, in an amount in the range from about 0.625 to about 10 kg of additive/ton of dry pulp;
wherein said brightening additive is an inorganic compound chosen from hypochlorous acid, one or more precursor compounds that form hypochlorous acid in said final D bleaching stage, or a mixture thereof; and
wherein the pH of the pulp slurry in the Final D bleaching stage at the time said brightening additive is added is in the range from about 3 to about 10.
2. The method according to claim 1 , wherein the final D bleaching stage has a retention time from 30 to 180 minutes.
3. The method according to claim 1 , wherein the brightening additive is added during the period of time beginning from about the last 10% of remaining time to the end of the bleaching stage.
4. The method according to claim 3 , wherein the brightening additive is added during the period of time beginning from about the last 5% of remaining time to the end of the bleaching stage.
5. The method according to claim 4 , wherein the brightening additive is added during the period of time with less than about 5 minutes remaining in the final D bleaching stage.
6. The method according to claim 5 , wherein the brightening additive is one or more precursors compounds that form hypochlorus acid chosen from Cl, Cl water, sodium hypochlorite, or mixtures thereof.
7. The method according to claim 6 , wherein the pH of the pulp slurry in the Final D bleaching stage at the time said brightening additive is added is in the range from about 3 to about 8.
8. The method according to claim 7 , wherein the pH of the pulp slurry is in the range from about 4 to about 7.
9. The method according to claim 7 , wherein the brightening additive is added in an amount in the range from about 1 to about 10 kg of additive/ton of dry pulp.
10. The method according to claim 7 , wherein additional ClO 2 is added to said final D bleaching stage with said brightening additive in an amount sufficient to reduce viscosity drop of the pulp slurry.
11. The method according to claim 3 , wherein the brightening additive is one or more precursors compounds that form hypochlorus acid chosen from Cl, Cl water, sodium hypochlorite, or mixtures thereof.
12. The method according to claim 11 , wherein the pH of the pulp slurry in the Final D bleaching stage at the time said brightening additive is added is in the range from about 3 to about 8.
13. The method according to claim 12 , wherein the pH of the pulp slurry is in the range from about 4 to about 7.
14. The method according to claim 12 , wherein the brightening additive is added in an amount in the range from about 1 to about 10 kg of additive/ton of dry pulp.
15. The method according to claim 12 , wherein additional ClO 2 is added to said final D bleaching stage with said brightening additive in an amount sufficient to reduce viscosity drop of the pulp slurry.
16. The method according to claim 1 , wherein the brightening additive is one or more precursors compounds that form hypochlorus acid chosen from Cl, Cl water, sodium hypochlorite, or mixtures thereof.
17. The method according to claim 1 , wherein the pH of the pulp slurry in the Final D bleaching stage at the time said brightening additive is added is in the range from about 3 to about 8.
18. The method according to claim 17 , wherein the pH of the pulp slurry is in the range from about 4 to about 7.
19. The method according to claim 1 , wherein the brightening additive is added in an amount in the range from about 1 to about 10 kg of additive/ton of dry pulp.
20. The method according to claim 1 , wherein additional ClO 2 is added to said final D bleaching stage with said brightening additive in an amount sufficient to reduce viscosity drop of the pulp slurry.