Sodium sulfide pulping with hydrogen sulfide generation

• US 4,113,553 A
• Filed: 01/27/1977
• Issued: 09/12/1978
• Est. Priority Date: 02/05/1976
• Status: Expired due to Term

• Current Assignee: MO OCH Domsjo AB
• Original Assignee: MO OCH Domsjo AB
• Inventors: Samuelson, Hans Olof
• Primary Examiner(s): Corbin, Arthur L.
• Application Number:
  US05/763,203
• Time in Patent Office: 593 Days
• Field of Search: 162/29, 162/30 R, 162/30 K, 162/34, 162/35, 162/38, 162/82, 162/86, 162/90, 423/562, 423/573 R, 423/573 G, 423/DIG. 3
• US Class Current: 162/34
• CPC Class Codes: D21C 3/266 the same pulping agent being used in all stages D21C3/263 takes precedence
• CPC Class Codes: Y10S 423/03 Papermaking liquor

Abstract

A process for pulping hardwood to produce cellulose pulp in good yield and of high quality, with a low requirement for causticized pulping liquor, which comprises in a first pulping stage pulping the hardwood in an alkaline pulping liquor containing sodium sulfide at a pH of about 10.5 to about 13 and at a temperature within the range from about 110° to about 170° C while generating hydrogen sulfide in situ by reaction of sodium sulfide with organic acids liberated in the pulping; and then in a second pulping stage, following directly after the first pulping stage, continuing the pulping at a pH higher than said first stage pH, within the range of about 12.5 to about 14 and at a temperature higher than said first stage temperature within the range from about 145° to about 190° C, in the presence of added alkaline pulping liquor comprising sodium hydroxide and sodium sulfide until cellulose pulp is produced.

Claims

1. A process for pulping hardwood to produce cellulose pulp in good yield and of high quality, with a low requirement for causticized pulping liquor, which comprises in a first pulping stage, in the absence of added carbon dioxide, pulping the hardwood in an alkaline pulping liquor containing sodium sulfide at a pH within the range from about 10.5 to about 13 and at a temperature within the range from about 110°

to about 170°

C for a time sufficient to consume at least 3%, based on the dry weight of the wood, of alkali in the pulping liquor, determined as titratable alkali, in chemical reactions with the wood, thereby forming a large proportion of soluble organic acids in the pulping liquor, and generating hydrogen sulfide in situ in the alkaline pulping liquor by reaction of sodium sulfide with said organic acids; and

then in a second pulping stage, following directly after the first pulping stage, continuing the pulping at a pH higher than said first stage pH, within the range from about 12.5 to about 14, and at a temperature higher than said first stage temperature, within the range from about 145°

to about 190°

C, in the presence of added alkaline pulping liquor comprising sodium hydroxide and sodium sulfide until cellulose pulp is produced.

2. A process according to claim 1, in which the pulping liquor in the first pulping stage is a green liquor obtained in chemicals recovery in a sulfate pulping process.

3. a process according to claim 2, in which the green liquor is one recovered after combustion of a spent alkaline sulfate pulping liquor from a sulfate pulping process carried out at a sulfidity from about 30 to about 50%.

4. A process according to claim 2, in which the green liquor is one recovered after combustion of a spent liquor from a polysulfide pulping process.

5. A process according to claim 2, in which the green liquor is treated with carbon dioxide to convert the sodium carbonate present into sodium bicarbonate before the liquor is introduced into the first pulping stage.

6. A process according to claim 1, in which the pulping liquor in the first pulping stage is an aqueous alkaline solution enriched with sodium sulfide.

7. A process according to claim 1, in which spent alkaline liquor from the first pulping stage is utilized to prepare fresh pulping liquor for use in the first pulping stage with another batch of hardwood material, after replenishment of the amount of sodium sulfide consumed.

8. A process according to claim 1, in which the consumption of titratable alkali in the first digestion pulping stage is within the range from about 3% to about 15% calculated as percent of sodium hydroxide based on the dry weight of the wood.

9. A process according to claim 1, in which the pulping liquor in the first pulping stage comprises sodium sulfide and sodium carbonate.

10. A process according to claim 1, in which the first pulping liquor is enriched in sodium sulfide obtained from a smelt produced by combustion of spent pulping liquor in a reducing atmosphere.

11. A process according to claim 10, in which the enrichment in sodium sulfide is obtained by partial dissolution of sodium sulfide from the smelt.

12. A process according to claim 10, in which the enrichment is obtained by crystallizing sodium carbonate from a solution obtained by dissolution of the smelt.

13. A process according to claim 10, in which residue remaining after separation of sodium sulfide, which is enriched in sodium carbonate, is used to prepare bleaching liquor.

14. A process according to claim 10, in which residue remaining after separation of sodium sulfide, which is enriched in sodium carbonate, is used to prepare alkaline liquor for alkaline extraction.

15. A process according to claim 1, in which the first pulping stage is carried to a yeild within the range from about 75 to about 92% based on the dry weight of the wood.

16. A process according to claim 1, in which the second pulping liquor has a pH within the range about 12.8 to about 14.

17. A process according to claim 1, in which the partial pressure of hydrogen sulfide during the first pulping stage is within the range from about 0.1 to about 2.0 MPa.

18. A process according to claim 1, in which gaseous hydrogen sulfide is withdrawn during the first pulping stage.

19. A process according to claim 18, in which withdrawn hydrogen sulfide is used to prepare sodium polysulfide for pulping liquor.

20. A process according to claim 18, in which withdrawn hydrogen sulfide is oxidized to elementary sulfur.

21. A process according to claim 1, in which the charge of effective alkali in the second pulping stage is within the range from about 10 to about 15% based on the dry weight of the wood.

22. A process according to claim 1, in which the temperature during the first pulping stage is within the range from about 120°

to about 150°

C.

23. A process according to claim 1, in which the temperature during the second pulping stage is within the range from about 155°

to about 175°

C.