Process of recovering sodium carbonate from spent pulping liquors

• US 4,138,312 A
• Filed: 05/16/1977
• Issued: 02/06/1979
• Est. Priority Date: 05/19/1976
• Status: Expired due to Term

• Current Assignee: Sappi Limited
• Original Assignee: Sappi Limited
• Inventors: Gill, Ronald A., Wheeler, Cecil M., Wojtowicz, Waldemar S., Berthold, Cornelius E.
• Primary Examiner(s): Bashore, S. Leon
• Assistant Examiner(s): Kratz, Peter F.
• Application Number:
  US05/797,563
• Time in Patent Office: 631 Days
• Field of Search: 162/30 R, 162/DIG. 8, 162/33, 423/182, 423/183, 423/184, 423/186, 423/189, 423/190, 423/207, 423/208, 423/421, 423/422, 423/425, 423/427, 423/DIG. 3
• US Class Current: 162/30.1
• CPC Class Codes: D21C 11/0064 Aspects concerning the production and the treatment of green and white liquors, e.g. causticizing green liquor

Abstract

The incinerator product obtained from the incineration of black liquor and other spent liquors from a soda pulping process is treated to remove contaminants including chlorides, sulphates and potassium compounds and to recover a high proportion of the sodium carbonate. The incinerator product is treated with water to form a slurry in which substantially pure sodium carbonate monohydrate is crystallized and a major proportion of the contaminants are dissolved, the sodium carbonate monohydrate is then separated and dissolved sodium carbonate is recovered as a bicarbonate or sesquicarbonate precipitate by carbonation of the solution. The preferred process involves an initial flue gas carbonation of the separated mother liquor after removal of sodium carbonate monohydrate to produce a sodium sesquicarbonate precipitate and a subsequent carbonation of the mother liquor, after separation of the sodium sesquicarbonate therefrom, with pure carbon dioxide to precipitate sodium bicarbonate.

Claims

1. A process for the manufacture of cellulose pulp by means of a soda process in which spent liquors are concentrated by evaporation and the concentrated liquors are incinerated in a fluidized bed incinerator to produce a granular sodium carbonate incinerator product contaminated by chlorides, sulphates and potassium compounds, the incinerator product being dissolved in water and causticized in known manner to form white liquor comprising essentially sodium hydroxide, which white liquor is re-used in the said soda process to provide a closed system, the improvement comprising:

treating the incinerator product with water to form a slurry, agitating the slurry so as to dissolve incinerator product with its contaminants and at the same time crystallize substantially pure sodium carbonate monohydrate leaving a major proportion of the contaminants in solution, separating the substantially pure sodium carbonate from the liquor containing the contaminants, and washing the separated sodium carbonate with water;

converting sodium carbonate remaining with the contaminants in solution to sodium bicarbonate by carbonation with carbon dioxide, separating the precipitate so formed from the mother liquor, and converting the precipitate thus recovered to substantially pure sodium carbonate;

utilizing sodium carbonate recovered in the formation of white liquor; and

discharging the contaminant bearing mother liquor from the system.

2. The process of claim 1 in which the temperature of the slurry is maintained above 35°

C.

3. The process of claim 2 in which the temperature of the slurry is maintained at approximately 85°

C.

4. The process of claim 1 in which a portion of the liquor obtained after separation of sodium carbonate from the slurry is recycled for the formation of slurry with incoming incinerator product, the solution of further contaminants and the precipitation of sodium carbonate monohydrate.

5. The process of claim 4 in which the portion of separated liquor not recycled is discharged, after carbonation with carbon dioxide, to maintain a balance between the mass of contaminants introduced with the incinerator product and the mass of contaminants discharged with said liquor.

6. The process of claim 5 in which make-up water is added to the slurry to replace losses of water, such make-up water being used for washing of sodium carbonate after separation from the liquor.

7. A process for the manufacture of cellulose pulp by means of a soda process in which spent liquors are concentrated by evaporation and the concentrated liquors are incincerated in a fluidized bed incinerator to produce a granular sodium carbonate incinerator product contaminated by chlorides, sulphates and potassium compounds, the incinerator product being dissolved in water and causticized in known manner to form white liquor comprising essentially sodium hydroxide, which white liquor is re-used in the said soda process to provide a closed system, the improvement comprising:

treating the incinerator product with water to form a slurry, agitating the slurry so as to dissolve incinerator product with its contaminants and at the same time crystallize substantially pure sodium carbonate monohydrate leaving a major proportion of the contaminants in solution, separating the substantially pure sodium carbonate from the first mother liquor containing the contaminants, and washing the separated sodium carbonate with water;

carbonating the first mother liquor with a flue gas containing carbon dioxide, maintaining the liquor at a temperature of about 45°

C. producing a precipitate consisting mainly of sodium sesquicarbonate, separating the precipitate from the resulting second mother liquor, and converting the precipitate to substantially pure sodium carbonate;

converting sodium carbonate in the second mother liquor to sodium bicarbonate by carbonation with substantially pure carbon dioxide, separating the sodium bicarbonate precipitate so formed from the mother liquor, and converting the precipitate thus recovered to substantially pure sodium carbonate;

utilizing sodium carbonate recovered in the formation of white liquor; and

discharging the contaminant bearing second mother liquor from the system.

8. The process of claim 7 in which the separated precipitates obtained after carbonation of the mother liquors are heated in known manner to form sodium carbonate, carbon dioxide and water and the carbon dioxide so formed is utilised as set out in the process of claim 7 to produce sodium bicarbonate.

9. A process for the manufacture of cellulose pulp by means of a soda process in which spent liquors are concentrated by evaporation and the concentrated liquors are incinerated in a fluidized bed incinerator to produce a granular sodium carbonate incinerator product contaminated by chlorides, sulphates and potassium compounds, the incinerator product being dissolved in water and causticized in known manner to form white liquor comprising essentially sodium hydroxide, which white liquor is re-used in the said soda process to provide a closed system, the improvement comprising:

treating the incinerator product with water to form a slurry, agitating the slurry so as to dissolve incinerator product with its contaminants and at the same time crystallize substantially pure sodium carbonate monohydrate leaving a major proportion of the contaminants in solution, separating the substantially pure sodium carbonate from the mother liquor containing the contaminants, and washing the separated sodium carbonate with water; and

carbonating the mother liquor with a flue gas containing carbon dioxide, maintaining the liquor at a temperature of about 45°

C. producing a precipitate consisting mainly of sodium sesquicarbonate, separating the precipitate from the mother liquor, and converting the precipitate to substantially pure sodium carbonate;

utilizing sodium carbonate recovered in the formation of white liquor; and

discharging the contaminant bearing second mother liquor from the system.