Method and a system for adjusting PH of green liquor dregs

Patent metadata

Field	Value
Publication number	US-11655589-B2
Application number	US-202017633055-A
Country	US
Kind code	B2
Filing date	Aug 18, 2020
Priority date	Aug 22, 2019
Publication date	May 23, 2023
Grant date	May 23, 2023

Abstract

The specification relates to a method and a system for adjusting pH of green liquor dregs. The method comprises contacting a slurry containing green liquor dregs (100, 200, 300, 400, 500) with flue gas (101, 201, 301, 401, 501). The system comprises a recovery boiler (105) configured to burn black liquor to produce smelt, a smelt dissolving tank (107) configured to dissolve the smelt to produce green liquor comprising green liquor dregs, and a green liquor clarifier/filter (103) and/or a dregs filter (104) configured to separate a slurry containing green liquor dregs (100, 200, 300, 400, 500) from the green liquor. The system further comprises a vessel (102, 202, 302, 402) configured to receive a slurry containing green liquor dregs (100, 200, 300, 400, 500) and a gas inlet (210, 310, 410, 510) configured to convey flue gas (101, 201, 301, 401, 501) to be contacted with the slurry containing green liquor dregs (100, 200, 300, 400, 500).

First claim

The invention claimed is:

1. A method for adjusting pH of a slurry containing green liquor dregs, the method comprising the step of:
contacting a slurry containing green liquor dregs ( 100 , 200 , 300 , 400 , 500 ) with flue gas ( 101 , 201 , 301 , 401 , 501 ),
wherein:
the slurry containing green liquor dregs ( 100 , 200 , 300 , 400 , 500 ) is a slurry obtained solely from at least one of a green liquor clarifier/filter ( 103 ) or a dregs filter ( 104 ) configured to separate the slurry containing green liquor dregs ( 100 , 200 , 300 , 400 , 500 ) from green liquor and has a pH of 10-13,
a dry solids content of the slurry containing green liquor dregs ( 100 , 200 , 300 , 400 , 500 ) is from 1 to 40 wt. %,
the flue gas ( 101 , 201 , 301 , 401 , 501 ) contains carbon dioxide, and
a pH of the slurry containing green liquor dregs after contacting with the flue gas ( 101 , 201 , 301 , 401 , 501 ) is between 7-9.

2. The method according to claim 1 , wherein a temperature of the slurry containing green liquor dregs is at most 150° C. and a temperature of the flue gas is at most 400° C.

3. The method according to claim 2 , wherein a dry solids content of the slurry containing green liquor dregs is from 1 to 20 wt. %.

4. The method according to claim 2 , wherein the method comprises spraying the slurry containing green liquor dregs ( 300 ) in a counter-current manner to the flue gas ( 301 ).

5. The method according to claim 1 , wherein a dry solids content of the slurry containing green liquor dregs is from 1 to 20 wt. %.

6. The method according to claim 5 , wherein the method comprises spraying the slurry containing green liquor dregs ( 300 ) in a counter-current manner to the flue gas ( 301 ).

7. The method according to claim 1 , wherein the flue gas ( 101 , 201 , 301 , 401 , 501 ) originates from a recovery boiler ( 105 ).

8. The method according to claim 7 , wherein the method comprises spraying the slurry containing green liquor dregs ( 300 ) in a counter-current manner to the flue gas ( 301 ).

9. The method according to claim 1 , wherein the flue gas ( 101 , 201 , 301 , 401 , 501 ) originates from burning of at least a renewable fuel.

10. The method according to claim 9 , wherein the method comprises spraying the slurry containing green liquor dregs ( 300 ) in a counter-current manner to the flue gas ( 301 ).

11. The method according to claim 1 , wherein the method comprises bubbling the flue gas ( 101 , 201 , 301 , 401 , 501 ) into the slurry containing green liquor dregs ( 100 , 200 , 300 , 400 , 500 ).

12. The method according to claim 1 , wherein the method further comprises:
directing the slurry containing green liquor dregs ( 100 , 200 , 300 , 400 , 500 ) and the flue gas ( 101 , 201 , 301 , 401 , 501 ) to an injector arrangement ( 411 ); and
mixing the slurry containing green liquor dregs ( 100 , 200 , 300 , 400 , 500 ) and the flue gas ( 101 , 201 , 301 , 401 , 501 ) in the injector arrangement ( 411 ).

13. The method according to claim 1 , wherein the method comprises spraying the slurry containing green liquor dregs ( 300 ) in a counter-current manner to the flue gas ( 301 ).

14. The method according to claim 1 , wherein the slurry containing green liquor dregs is a non-pretreated slurry.

15. The method according to claim 1 , further comprising, after the contacting step, collecting and reusing treated green liquor dregs.

16. The method according to claim 15 , wherein the collecting step further comprises recirculating the treated green liquor dregs to an injector arrangement ( 411 ).

17. The method according to claim 16 , wherein the recirculating involves a subsequent contacting of the treated green liquor dregs with flue gas ( 101 , 201 , 301 , 401 , 501 ).

Assignees

• Valmet Technologies Oy

Inventors

• Vettenranta Aino

Classifications

• D21C11/0071 Primary

  Treatment of green or white liquors with gases, e.g. with carbon dioxide for carbonation; Expulsion of gaseous compounds, e.g. hydrogen sulfide, from these liquors by this treatment (stripping); Optional separation of solid compounds formed in the liquors by this treatment (oxidation of liquors (black, green or white) D21C11/0057; treatment of pulp gases D21C11/06) · CPC title

• D21C11/12

  Combustion of pulp liquors · CPC title

• D21C11/0078

  Treatment of green or white liquors with other means or other compounds than gases, e.g. in order to separate solid compounds such as sodium chloride and carbonate from these liquors; Further treatment of these compounds (fractionating of spent liquors D21C11/0042) · CPC title

• Y02P40/40

  Production or processing of lime, e.g. limestone regeneration of lime in pulp and sugar mills · CPC title

• D21C11/0064 Primary

  Aspects concerning the production and the treatment of green and white liquors, e.g. causticizing green liquor · CPC title