Process for acid bleaching of lignocellulose-containing pulp with a magnesium compound

• US 6,398,908 B1
• Filed: 11/22/1996
• Issued: 06/04/2002
• Est. Priority Date: 04/30/1991
• Status: Expired due to Fees

• Current Assignee: Eka Nobel AB (Nouryon Coöperatief UA)
• Original Assignee: Eka Nobel AB (Nouryon Coöperatief UA)
• Inventors: Andersson, Lennart, Holtinger, Lillemor, Hermansson, Wenche Elisabeth, Basta, Jiri, Linsten, Magnus
• Primary Examiner(s): Alvo, Steve
• Application Number:
  US08/754,884
• Time in Patent Office: 2,020 Days
• Field of Search: 162/65, 162/78, 162/76, 162/88, 162/89, 162/67, 162/82, 162/83, 162/84, 162/85, 162/87
• US Class Current: 162/65
• CPC Class Codes: D21C 9/1005 Pretreatment of the pulp, e.g. degassing the pulp
• CPC Class Codes: D21C 9/1036 Use of compounds accelerating or improving the efficiency of the processes
• CPC Class Codes: D21C 9/153 with ozone
• CPC Class Codes: D21C 9/163 with peroxides

Abstract

A process for delignification and bleaching of chemically digested lignocellulose-containing pulp. In a first embodiment, the pulp is acid treated at a pH of between about 1 and about 6, whereupon a water-soluble compound containing an alkaline earth metal is added at a pH of between about 1 and about 7 before the pulp is treated with a chlorine-free bleaching agent. In a second embodiment, the acid and alkaline earth metal treatments are carried out in a single step. The chlorine-free bleaching agent includes peroxide compounds, ozone, oxygen and sodium dithionite in an optional sequence or mixture. After the treatment according to the invention, the pulp may be finally bleached to the desired brightness, suitably with a chlorine-free bleaching agent, such as ozone, to completely avoid formation and discharge of AOX.

Claims

1. A process for delignification and bleaching of a chemically digested lignocellulose-containing pulp, wherein the pulp is bleached at a pH in the range from about 1 up to about 6 with a bleaching chemical selected from the group consisting of chlorine dioxide, ozone, peracetic acid and acid peroxides, whereupon a water-soluble chemical containing magnesium is added at a pH in the range from about 1 up to about 7 and in an amount of from about 0.01 up to about 10 kg/ton of dry pulp, calculated as magnesium, and that subsequently the pulp is bleached with hydrogen peroxide at a pH of from about 8 up to about 12.

2. A process according to claim 1, wherein the amount of hydrogen peroxide is at least 4 kg/ton dry pulp.

3. A process according to claim 1, wherein the chemically digested pulp is a sulphate pulp.

4. A process according to claim 1, wherein the water-soluble chemical containing magnesium is added at a pH of from 2 up to 6.

5. A process according to claim 1, wherein the water-soluble chemical containing magnesium consists of magnesium sulphate or magnesium chloride.

6. A process according to claim 1, wherein the pulp is washed after the acid bleaching.

7. A process according to claim 1, wherein the bleaching before addition of the water-soluble chemical containing magnesium is carried out at a pH in the range from 1.5 up to 5.

8. A process according to claim 1, wherein the pulp, after the bleaching with hydrogen peroxide, is finally bleached with ozone in one or more steps.

9. A process according to claim 1, wherein the acid bleaching step is carried out at a temperature of from about 10°

C. up to about 95°

C. for about 1 min up to about 120 min, the water-soluble chemical containing magnesium is added at a temperature of from about 10°

C. up to 95°

C. for about 1 min up to about 180 min and in an amount of from 0.5 up to 5 kg/ton of dry pulp, calculated as magnesium, the treated pulp having a pulp concentration of from about 3 up to about 35% by weight.