A cellulose paper composite and process for preparation thereof
US-2020340182-A1 · Oct 29, 2020 · US
US9540767B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-9540767-B2 |
| Application number | US-201314390051-A |
| Country | US |
| Kind code | B2 |
| Filing date | Apr 3, 2013 |
| Priority date | Apr 3, 2012 |
| Publication date | Jan 10, 2017 |
| Grant date | Jan 10, 2017 |
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A method for bleaching pulp is provided. In the method at least one tertiary amine compound is introduced into a process stage of bleaching. This process stage is a stage which comprises mixing pulp and a chlorine compound capable of bleaching.
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The invention claimed is: 1. A method for bleaching pulp which pulp contains hexenuronic acid, lignin or corresponding aromatic chemical structures, wherein at least one tertiary amine compound of the general formula (1) is introduced as catalyst into a process stage of bleaching that consists essentially of mixing pulp and a chlorine compound capable of bleaching, and wherein X is N or C, and R 1 -R 12 is the same or different alkyl group, halide, ester, alkoxide or hydrogen wherein the amount of said tertiary amine compound is a catalytic amount from at least 0.01 kg/ton of pulp to less than 3 kg/ton of pulp. 2. The method according to claim 1 , wherein said tertiary amine is selected from the group consisting of quinuclidine, triethylenediamine and a mixture thereof. 3. The method according to claim 1 , wherein said tertiary amine compound is introduced as an aqueous solution. 4. The method according to claim 1 , wherein said chlorine compound comprises chlorine dioxide, elemental chlorine, chlorite, hypochlorous acid or hypochlorite salts. 5. The method according to; claim 1 , wherein said chlorine compound is selected from compounds forming hypochlorous acid in situ at said process stage. 6. The method according to claim 1 , wherein said chlorine compound is introduced into said process stage after the introduction of said tertiary amine compound. 7. The method according to claim 5 , wherein the amount of active chlorine present at said process stage is from 1 to 30 kg act. Cl/ton of pulp. 8. The method according to claim 1 , wherein the temperature at said process stage is below 100° C. 9. The method according to claim 1 , wherein said process stage is a chlorine dioxide bleaching stage. 10. The method according to claim 1 , wherein said tertiary amine compound is recovered after bleaching at said process stage. 11. The method according to claim 1 , wherein bleaching time at said process stage of bleaching is less than 10 min. 12. The method according to claim 8 , wherein said tertiary amine compound is introduced as an aqueous solution. 13. The method of claim 7 , wherein the amount of active chlorine present at said process stage is from 3 to 20 kg act. Cl/ton of pulp. 14. The method of claim 13 , wherein the amount of active chlorine present at said process stage is from 5 to 15 kg act. Cl/ton of pulp. 15. The method of claim 8 , wherein the temperature is below 90° C. 16. The method of claim 8 wherein the temperature is from 50 to 90° C. 17. The method according to claim 10 , wherein said tertiary amine compound is reused or recycled or both. 18. The method according to claim 11 , wherein the bleaching time is less than 5 min. 19. The method of claim 1 , wherein the amount of said tertiary amine compound is a catalytic amount, less than 2 kg/ton, but at least 0.1 kg/ton.
Nitrogen-containing compounds · CPC title
with ClO2 or chlorites · CPC title
with halogens or halogen-containing compounds (D21C9/16 takes precedence) · CPC title
Bleaching agents (bleaching cellulose pulp D21C9/10) · CPC title
with ClO2/Cl2 and other bleaching agents in a multistage process · CPC title
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