Pulping of lignocellulosic material with oxygen in two stages at increasing pH

• US 3,944,463 A
• Filed: 12/12/1973
• Issued: 03/16/1976
• Est. Priority Date: 12/19/1972
• Status: Expired due to Term

• Current Assignee: MO OCH Domsjo AB
• Original Assignee: MO OCH Domsjo AB
• Inventors: Samuelson, Hans Olof, Hagglund, Erik Olof Sture, Smedman, Leif Ake
• Primary Examiner(s): Bashore, S. Leon
• Assistant Examiner(s): Corbin, Arthur L.
• Application Number:
  US05/424,148
• Time in Patent Office: 825 Days
• Field of Search: 162/65, 162/78, 162/90, 8/111
• US Class Current: 162/65
• CPC Class Codes: D21C 3/263 at least one stage being in presence of oxygen

Abstract

A process is provided for producing cellulose pulp of high brightness, which comprises pulping lignocellulosic material such as wood with oxygen under superatmospheric pressure in two stages, in the first at a pH within the range from about 6 to about 9, and in the second at a more alkaline pH of at least about 10.

Claims

1. A process for preparing cellulose pulp which comprises pulping lignocellulosic material with oxygen under superatmospheric pressure in the presence of an alkaline compound in at least two oxygen pulping stages, in a first stage at a pH within the range from about 6 to about 9 and at a temperature within the range from about 110°

to about 160°

C; and

in a second stage at a pH of at least about 10 and at a temperature within the range from about 80°

to about 160°

C; and

continuing the pulping with oxygen under superatmospheric pressure at a temperature within the range from about 80°

to about 160°

C until cellulose pulp is obtained.

2. A process in accordance with claim 1 in which the alkaline compound is selected to allow pulping with oxygen at a pH within the stated range.

3. A process in accordance with claim 2 in which the alkaline compound is selected from the group consisting of alkali metal and alkaline earth metal carbonates, bicarbonates, and hydroxides, and mixtures thereof.

4. A process in accordance with claim 1 in which the amount of alkaline compound is within the range from about 1 to about 10 kilomoles per 1000 kg. of dry lignocellulosic material.

5. A process in accordance with claim 1 in which all of the alkali required for the pulping is added to the lignocellulosic material at the start of the process.

6. A process in accordance with claim 1 in which only a portion of the alkali required is added at the start of the process, and alkali is added to the system thereafter, in amounts to maintain the desired pH.

7. A process in accordance with claim 1, in which the oxygen pulping is preceded by a pretreatment of the lignocellulosic material with an aqueous liquor containing an alkaline compound at a temperature within the range from about 60°

to about 200°

C, until from about 5 to about 15% of the lignocellulosic material, based on the dry weight of the material, is dissolved in the pretreatment liquor.

8. A process in accordance with claim 7, in which the pH of the pretreatment liquor is within the range from about 6.5 to about 14 during the major portion of the pretreatment time.

9. A process according to claim 7 in which the pretreating liquor contains sodium carbonate, sodium bicarbonate or a mixture thereof, as the alkaline compound, and water or a spent pulping, bleaching or pretreating liquor as the aqueous phase.

10. A process in accordance with claim 7 in which spent pretreating liquor is separated from the lignocellulosic material before the oxygen pulping is begun, by washing out at least a part of the spent pretreating liquor from the pretreated lignocellulosic material with water or a waste oxygen pulping liquor derived from the oxygen pulping process.

11. A process in accordance with claim 1 in which in the first oxygen pulping stage the pH is at about 9 for the major portion, and is then allowed to decrease toward the lower end of the range during the remainder of the pulping time, thereby producing a low viscosity pulp.

12. A process in accordance with claim 1 in which in the first oxygen pulping stage the pH is within the range from about 6.5 to 8 during most of the pulping time, thereby producing a high viscosity pulp.

13. A process in accordance with claim 1 in which during the first oxygen pulping stage, the partial pressure of oxygen is within the range from about 3 to about 200 bars.

14. A process in accordance with claim 1 in which the partial pressure of oxygen during the first oxygen pulping stage is within the ragne from about 8 to about 50 bars, thereby producing a paper pulp.

15. A process in accordance with claim 1 in which the partial pressure of oxygen during the second oxygen pulping stage is within the range from about 1 to about 100 bars.

16. A process in accordance with claim 1, which includes washing first pulping liquor from the partially pulped cellulosic material from the first oxygen pulping stage and then contacting the partially pulped cellulosic material with a second pulping liquor for the second oxygen pulping stage.

17. A process in accordance with claim 16, in which the washing liquor is a spent pulping liquor from the second oxygen pulping stage.

18. A process in accordance with claim 1, in which the pulping is carried out in the presence of a degradation inhibitor which protects the cellulose and hemicellulose molecules against degradation.

19. A process in accordance with claim 18, in which the inhibitor is charged to the pulping liquor at an early stage of the pulping.

20. A process in accordance with claim 18, in which the inhibitor is added to a pretreatment liquor prior to the oxygen pulping.

21. A process in accordance with claim 18, in which the inhibitor is added to the oxygen pulping liquor before combination with lignocellulosic material.

22. A process in accordance with claim 18, in which the inhibitor is a magnesium compound.

23. A process in accordance with claim 1, in which the oxygen is pure oxygen gas.

24. A process in accordance with claim 1, in which the oxygen is in admixture with an inert gas.

25. A process in accordance with claim 1 in which carbon dioxide formed in the oxygen pulping at a pH from about 6 to about 9 is removed.

26. A process in accordance with claim 25 in which such carbon dioxide is absorbed in an alkaline liquid.

27. A process in accordance with claim 1 in which a peroxide is added to the pulping liquor during or at the end of the second oxygen pulping stage.

28. A process in accordance with claim 1 in which the superatmospheric pressure during the second oxygen pulping stage is less than the superatmospheric pressure in the first oxygen pulping stage.