Kraft smelt solidification in a fluidized bed reactor

• US 5,545,292 A
• Filed: 09/09/1994
• Issued: 08/13/1996
• Est. Priority Date: 09/09/1994
• Status: Expired due to Fees

• Current Assignee: Hughes Aircraft Company (Rtx Corporation), Sony Corporation (Sony Group Corp.), Sony Music Entertainment Incorporated (Sony Group Corp.), Georgia Tech Research Corporation (University System of Georgia)
• Original Assignee: Institute of Paper Science and Technology Incorporated
• Inventors: Empie, H. Jeff
• Primary Examiner(s): Czaja, Donald E.
• Assistant Examiner(s): NGUYEN, TAN D
• Application Number:
  US08/303,614
• Time in Patent Office: 704 Days
• Field of Search: 162/30.1, 162/30.11, 162/68, 422/185, 422/139, 422/164, 110/245, 48/209, 423/DIG.3
• US Class Current: 162/30.11
• CPC Class Codes: D21C 11/0064 Aspects concerning the production and the treatment of green and white liquors, e.g. causticizing green liquor
• CPC Class Codes: D21C 11/122 Treatment, e.g. dissolution, of the smelt
• CPC Class Codes: Y02P 40/40 Production or processing of lime, e.g. limestone regeneration of lime in pulp and sugar mills
• CPC Class Codes: Y02P 70/10 Greenhouse gas [GHG] capture, material saving, heat recovery or other energy efficient measures, e.g. motor control, characterised by manufacturing processes, e.g. for rolling metal or metal working

Abstract

An improved black liquor recovery system for use in a kraft pulping mill is provided. Molten kraft smelt from a black liquor recovery boiler or recovery system is fed into a fluidized bed reactor where it is cooled and solidified to form solid kraft smelt particles. The solid kraft smelt particles are then fed into a dissolving tank containing an aqueous solution to form a green liquor. The green liquor, after clarification, is treated with lime to form a white liquor containing the regenerated pulping chemicals. Waste steam is an especially preferred fluidizing gas for use in the fluidized bed reactor. This process provides improved energy recovery and process productivity, reduction in gaseous sulfur-containing emissions, reduction in landfilled wastes, and improved safety as compared to a conventional kraft smelt treatment process.

Claims

1. A process for treatment of molten kraft smelt in a kraft recovery process, said process comprising

(1) feeding molten kraft smelt from a black liquor recovery system to a fluidized bed reactor containing particulate solids fluidized with a non-oxidizing fluidizing gas, wherein the fluidized bed reactor is operated at a temperature of about 600°

to 900°

F.;

(2) solidifying the molten kraft smelt within the fluidized bed reactor to form solid kraft smelt particles;

(3) removing the solid kraft smelt particles from the fluidized bed reactor; and

(4) feeding the solid kraft smelt particles to a dissolving tank containing an aqueous solution whereby a kraft green liquor is formed.

2. A process as defined in claim 1, wherein the molten kraft smelt is fed into the central portion of the fluidized bed reactor and the solid kraft smelt particles are removed from the lower portion of the fluidized bed reactor.

3. A process as defined in claim 1, wherein the molten kraft smelt is fed into the fluidized bed reactor by gravity via a ceramic supply line.

4. A process as defined in claim 1, wherein the particulate solids used to start up the fluidized bed reactor are selected from the group consisting of sand, water insoluble salts, and ground-up solid kraft smelt.

5. A process as defined in claim 1, wherein the particulate solids used to start up the fluidized bed reactor are ground-up solid kraft smelt.

6. A process as defined in claim 1, wherein the non-oxidizing fluidizing gas is steam which is essentially oxygen free.

7. A process as defined in claim 1, wherein the molten kraft smelt is fed into the central portion of the fluidized bed reactor by gravity via a ceramic supply line, wherein the solid kraft smelt particles are removed from the lower portion of the fluidized bed reactor, wherein the particulate solids used to start up the fluidized bed reactor are ground-up solid kraft smelt, and wherein the non-oxidizing fluidizing gas is steam which is essentially oxygen free.

8. A process as defined in claim 7, wherein the solid kraft smelt particles are fed into the dissolving tank sufficiently below the surface of the aqueous solution so that essentially all the volatile, sulfur-containing materials which are thereby liberated are recondensed and reabsorbed in the aqueous solution.

9. A process as defined in claim 8, wherein the solid kraft smelt particles removed from the fluidized bed reactor and fed into the dissolving tank are at a temperature of about 600°

to 750°

F. whereby the temperature of the aqueous solution in the dissolving tank is maintained at a temperature of about 180°

to 205°

F.

10. A process as defined in claim 1, wherein the solid kraft smelt particles are fed into the dissolving tank sufficiently below the surface of the aqueous solution so that essentially all the volatile, sulfur-containing materials which are thereby liberated are recondensed and reabsorbed in the aqueous solution.

11. A process as defined in claim 1, wherein the solid kraft smelt particles removed from the fluidized bed reactor and fed into the dissolving tank are at a temperature of about 600°

to 750°

F. whereby the temperature of the aqueous solution in the dissolving tank is maintained at a temperature of about 180°

to 205°

F.

12. A continuous process for treatment of molten kraft smelt in a kraft recovery process, said process comprising

(1) continuous feeding molten kraft smelt from a black liquor recovery system to a fluidized bed reactor containing particulate solids fluidized with a non-oxidizing fluidizing gas, wherein the fluidized bed reactor is operated at a temperature of about 600°

to 900°

F.;

(2) solidifying the molten kraft smelt within the fluidized bed reactor to form solid kraft smelt particles;

(3) removing the solid kraft smelt particles from the lower portion of the fluidized bed reactor; and

(4) feeding the solid kraft smelt particles removed from the fluidized bed reactor to a dissolving tank containing an aqueous solution whereby a kraft green liquor is formed, wherein the solid smelt particles are introduced sufficiently below the surface of the aqueous solution so that essentially all gaseous sulfur-containing compounds liberated upon introduction of the solid smelt particles are absorbed in the aqueous solution;

wherein the relative rates of molten kraft smelt fed into the fluidized reactor and solid kraft smelt particles removed from the fluidized bed reactor are adjusted to achieve an essentially steady state operation.

13. A continuous process as defined in claim 12, wherein the molten kraft smelt is fed into the fluidized bed reactor by gravity via a ceramic supply line from the black liquor recovery system and wherein the non-oxidizing fluidizing gas is essentially oxygen-free steam.

14. A continuous process as defined in claim 13, wherein the particulate solids used to start up the fluidized bed reactor are ground-up solid kraft smelt.

15. A continuous process as defined in claim 14, wherein the solid kraft smelt particles removed from the fluidized bed reactor and fed into the dissolving tank are at a temperature of about 600°

to 750°

F. whereby the temperature of the aqueous solution in the dissolving tank is maintained at a temperature of about 180°

to 205°

F.

16. A continuous process as defined in claim 13, wherein the solid kraft smelt particles removed from the fluidized bed reactor and fed into the dissolving tank are at a temperature of about 600°

to 750°

F. whereby the temperature of the aqueous solution in the dissolving tank is maintained at a temperature of about 180°

to 205°

F.

17. A continuous process as defined in claim 13, wherein the fluidizing gas exiting the fluidized bed reactor is used as superheated steam.

18. A continuous process as defined in claim 12, wherein the particulate solids used to start up the fluidized bed reactor are selected from the group consisting of sand, water insoluble salts, and ground-up solid kraft smelt.

19. A continuous process as defined in claim 12, wherein the solid kraft smelt particles removed from the fluidized bed reactor and fed into the dissolving tank are at a temperature of about 600°

to 750°

F. whereby the temperature of the aqueous solution in the dissolving tank is maintained at a temperature of about 180°

to 205°

F.

20. An integrated process for the recovery of pulping chemicals from black liquor from a kraft pulping mill, said process comprising

(1) burning black liquor from a kraft pulping mill in a boiler to produce high pressure steam;

(2) collecting molten kraft smelt from the bottom of the boiler;

(3) feeding the molten kraft smelt into a fluidized bed reactor containing a particulate substrate fluidized with a non-oxidizing fluidizing gas and operated at a temperature at least 100°

F. below the melting point of the molten kraft smelt, whereby the molten kraft smelt cools and solidifies upon contact with the fluidized particulate substrate to form solid kraft smelt particles;

(4) removing the solid kraft smelt particles from the fluidized bed reactor;

(5) feeding the solid kraft smelt particles to a dissolving tank containing an aqueous solution at about 180°

to 205°

F. to form a kraft green liquor, wherein the solid kraft smelt particles are fed at a sufficient depth below the surface of the aqueous solution so that steam and volatile sulfur-containing compounds are recondensed and reabsorbed in the aqueous solution;

(6) clarifying the kraft green liquor by removing dregs; and

(7) treating the clarified kraft green liquor with lime to form a kraft white liquor containing the pulping chemicals.

21. An integrated process as defined in claim 20, wherein the fluidizing gas is low-grade steam which is essentially oxygen free, wherein off-gases from the fluidized bed reactor are treated in a scrubber to remove sulfur-containing compounds, and wherein the treated off-gases are used as superheated steam.

22. An integrated process as defined in claim 21, wherein the molten kraft smelt fed into the fluidized bed reactor is about 1350°

to 1550°

F., wherein the fluidized bed reactor is operated at about 600°

to 900°

F., wherein the dissolving tank is operated at about 180°

to 205°

F., and wherein the green liquor is clarified at about 180°

to 200°

F.

23. An integrated process as defined in claim 22, wherein the molten kraft smelt fed into the fluidized bed reactor is about 1400°

to 1500°

F., wherein the fluidized bed reactor is operated at about 600°

to 750°

F., wherein the dissolving tank is operated at about 190°

to 200°

F., and wherein the green liquor is clarified at about 180°

to 200°

F.

24. An integrated process as defined in claim 22, wherein the relative rates of molten kraft smelt fed into the fluidized reactor and solid kraft smelt particles removed from the fluidized bed reactor are adjusted to achieve an essentially steady state operation, and wherein the particulate substrate used to start up the fluidized bed reactor is ground up solid kraft smelt.

25. An integrated process as defined in claim 21, wherein the relative rates of molten kraft smelt fed into the fluidized reactor and solid kraft smelt particles removed from the fluidized bed reactor are adjusted to achieve an essentially steady state operation, and wherein the particulate substrate used to start up the fluidized bed reactor is ground up solid kraft smelt.

26. An integrated process as defined in claim 20, wherein the relative rates of molten kraft smelt fed into the fluidized reactor and solid kraft smelt particles removed from the fluidized bed reactor are adjusted to achieve an essentially steady state operation, and wherein the particulate substrate used to start up the fluidized bed reactor is ground up solid kraft smelt.