Method of producing oxidized white liquor using dregs containing carbon particles

• US 5,972,165 A
• Filed: 01/17/1997
• Issued: 10/26/1999
• Est. Priority Date: 01/17/1997
• Status: Expired due to Fees

• Current Assignee: BOC Group, Inc. (Messer Adolf Family)
• Original Assignee: BOC Group, Inc. (Messer Adolf Family)
• Inventors: Sethna, Rustam H., Kirschner, Mark J.
• Primary Examiner(s): NGUYEN, TAN D
• Application Number:
  US08/785,262
• Time in Patent Office: 1,012 Days
• Field of Search: 162/29, 162/30.11, 422/185, 423/551, 423/562, 423/564.2, 423/566.2, 423/566.3
• US Class Current: 162/30.11
• CPC Class Codes: D21C 11/0057 Oxidation of liquors, e.g. in order to reduce the losses of sulfur compounds, followed by evaporation or combustion if the liquor in question is a black liquor deodorisation of gases D21C11/08; combustion D21C11/12, D21C11/14
• CPC Class Codes: D21C 11/0078 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

Abstract

White liquor produced from black liquor is partially or completed oxidized. The white liquor contains dregs that are utilized as a carbon based catalyst. Dregs are produced by separating the dregs from green liquor an intermediate product between the black liquor and the oxidized white liquor. After formation of the oxidized white liquor, the dregs are separated therefrom to form a waste dreg stream which can be recycled so that part of the dregs present within the dregs containing white liquor stream to be oxidized is contributed by the waste dreg stream.

Claims

1. A method of producing oxidized white liquor from black liquor comprising:

converting said black liquor into a white liquor stream having dregs containing carbon particles; and

oxidizing said dreg containing white liquor stream to produce an oxidized white liquor.

4. The method of claim 2 or claim 1, further comprising:

separating said dregs from said oxidized white liquor to form a waste dreg stream; and

recycling at least part of said waste dreg stream to said white liquor stream so that part of said dregs present within said dregs containing white liquor stream is contributed by said waste dreg stream.

5. The method of claim 4, wherein said dregs are present within said dreg containing white liquor stream at a concentration of no more than about 10.0 grams/liter.

6. The method of claim 5, wherein said oxidizing is at a temperature of between about 120°

C. to about 180°

C. and at a pressure of between about 120 and 250 psig and such that sodium sulfide content of said dreg containing white liquor is substantially converted to sodium sulfate.

7. The method of claim 5, wherein said oxidizing is at a temperature of about 170°

C. and a pressure of about 250 psig and such that sodium sulfide content of said dreg containing white liquor is substantially converted to sodium sulfate.

8. The method of claim 5, wherein said oxidizing is at a temperature of between about 60°

C. to about 110°

C. and at a pressure of between about 70 psig and about 100 psig and such that sodium sulfide content of said dreg containing white liquor is substantially converted to sodium thiosulfate.

9. The method of claim 5, wherein said oxidizing is at a temperature of about 100°

C. and a pressure of about 100 psig and such that sodium sulfide content of said dreg containing white liquor is substantially converted to sodium thiosulfate.

10. The method of claim 2 or claim 1 or claim 3, wherein said dregs are present within said dreg containing white liquor stream at a concentration of no more than about 10.0 grams/liter.

11. The method of claim 10, wherein said oxidizing is at a temperature of between about 120°

C. to about 180°

C. and at a pressure of between about 120 and 250 psig and such that sodium sulfide content of said dreg containing white liquor is substantially converted to sodium sulfate.

12. The method of claim 10, wherein said oxidizing is at a temperature of about 170°

C. and a pressure of about 250 psig and such that sodium sulfide content of said dreg containing white liquor is substantially converted to sodium sulfate.

13. The method of claim 10, wherein said oxidizing is at a temperature of between about 60°

C. to about 110°

C. and at a pressure of between about 70 psig and about 100 psig and such that sodium sulfide content of said dreg containing white liquor is substantially converted to sodium thiosulfate.

14. The method of claim 10, wherein said oxidizing is at a temperature of about 100°

C. and a pressure of about 100 psig and such that sodium sulfide content of said dreg containing white liquor is substantially converted to sodium thiosulfate.

2. A method of producing oxidized white liquor from black liquor comprising:

converting said black liquor to green liquor;

separating dregs containing carbon particles from said green liquor;

concentrating said dregs to produce a solid component and an aqueous solution containing said dregs;

converting said green liquor into said white liquor;

combining streams of said aqueous solution and said white liquor to produce a white liquor stream having dregs containing carbon particles; and

oxidizing said dreg containing white liquor stream to produce an oxidized white liquor.

3. A method of oxidizing white liquor containing dregs comprising:

oxidizing a white liquor stream having dregs containing carbon particles to produce an oxidized white liquor;

separating said dregs from said oxidized white liquor to form a waste dreg stream; and

recycling at least part of said waste dreg stream to said white liquor stream so that part of said dregs present within said dreg containing white liquor stream is contributed by said waste dreg stream.