IP Library › Granted Patent US 10,513,824
Granted Patent B2
US 10,513,824 · App. 15/576,845 · Granted Dec 24, 2019

Method for reducing pulp viscosity in production of dissolving pulp

Inventors: Leif Robertson (Parainen, FI); Veli-Matti Vuorenpalo (Espoo, FI); Jonas Konn (Espoo, FI); Kaisa Kaski (Vaasa, FI)
Assignee: Kemira Oyj
D21C9/004C07C409/26D21C1/02D21C3/00D21C3/022D21C3/04D21C3/222D21C3/26D21C9/10D21C9/1036D21C9/1052
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Quick Facts
Patent No.
US 10,513,824
App. No.
15/576,845
Granted
Dec 24, 2019
Kind
B2
Abstract

The invention relates to a method for reducing pulp viscosity in production of dissolving pulp. The method comprises producing cellulose pulp, whereby the obtained cellulose pulp has a cellulose content of at least 90%, and bleaching the obtained cellulose pulp. The cellulose pulp is treated after bleaching with performic acid.

Claims (20)

1. A method for reducing pulp viscosity in production of dissolving pulp, the method comprising:

producing a cellulose pulp having a cellulose content of at least 90%;

bleaching the obtained cellulose pulp;

and

decreasing

the viscosity of the bleached pulp by treating the bleached pulp with performic acid, while at the same time, keeping a brightness change of the pulp to less than 1% ISO,

wherein the brightness change is a difference between a brightness of the pulp measured before a treatment with the performic acid and a brightness of the pulp measured after a treatment with the performic acid, and

wherein the pH during treatment with the performic acid is in a range between 6-8.

2. The method according to claim 1 , wherein performic acid is used in amount of 0.1-7 kg/ton pulp.

3. The method according to claim 1 , wherein during the treatment with performic acid pH of the pulp changes less than one pH unit.

4. The method according to claim 1 , wherein the temperature during the treatment with performic acid is in a range of 30-100° C.

5. The method according to claim 1 , wherein the method is free from additional heating or cooling of the cellulose pulp before the treatment with performic acid.

6. The method according to claim 1 , wherein the pulp is treated with performic acid directly and immediately after the end of the bleaching step.

7. The method according to claim 1 , wherein the bleached pulp has a consistency of 5-15%, calculated as dry content.

8. The method according to claim 1 , wherein the performic acid is produced on-site and used directly for treating the obtained bleached cellulose pulp.

9. The method according to claim 1 , wherein distilled peracetic acid is added to the pulp after the bleaching in amount of 0.01-30 kg/ton dry pulp.

10. The method according to claim 1 , wherein the obtained cellulose pulp is produced by a kraft process with a prehydrolysis step.

11. The method according to claim 1 , wherein the obtained cellulose pulp, which is treated with performic acid, has a cellulose content of at least 92%.

12. The method according to claim 1 , wherein the obtained bleached cellulose pulp is treated by continuous addition of performic acid to the pulp after the bleaching.

13. The method according to claim 1 , wherein the viscosity decrease of the cellulose pulp is at least 30 dm 3 /kg.

Assignments (1)
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Dec 15, 2017
From: ROBERTSEN, LEIF; VUORENPALO, VELI-MATTI; KONN, JONAS; KASKI, KAISA
To: KEMIRA OYJ
Reel/Frame 044404/0071 →
Priority Claims (1)
FI 20155400 · May 27, 2015 · national
Continuity (1)
Related Publication 20180163344A1 · Jun 14, 2018