Process for the manufacture of pulp using sodium carbonate and oxygen

• US 4,045,279 A
• Filed: 09/09/1976
• Issued: 08/30/1977
• Est. Priority Date: 01/17/1972
• Status: Expired due to Term

• Current Assignee: New Oji Paper Co., Ltd. (Oji Holdings Corporation)
• Original Assignee: Toyo Pulp Co., Ltd. (Oji Holdings Corporation)
• Inventors: Takeda, Katsuhiko, Nagano, Tadashi, Miyao, Saisei
• Primary Examiner(s): Corbin, Arthur L.
• Application Number:
  US05/722,000
• Time in Patent Office: 355 Days
• Field of Search: 162/17, 162/19, 162/25, 162/31, 162/37, 162/40, 162/65, 162/90, 210/38 B, 210/42 R, 210/51, 210/52, 210/63 R, 423/24, 423/37, 423/139, 423/140, 241/15, 241/17, 241/18, 241/21, 241/27, 241/28
• US Class Current: 162/25
• CPC Class Codes: D21C 11/00 Regeneration of pulp liquors or effluent waste waters
• CPC Class Codes: D21C 11/12 Combustion of pulp liquors
• CPC Class Codes: D21C 3/00 Pulping cellulose-containing materials digesters D21C7/00
• CPC Class Codes: D21C 3/02 with inorganic bases or alkaline reacting compounds, e.g. sulfate processes
• CPC Class Codes: D21C 9/10 Bleaching ; Apparatus therefor

Abstract

A process for preparing pulp in a closed system by pre-cooking fibrous raw material in an alkaline aqueous solution of sodium carbonate or a mixture of sodium carbonate and sodium bicarbonate as the only alkaline ingredients at 90°-190° C, defibrating the pre-cooked material, pulping the defibrated material in an alkaline aqueous solution of sodium carbonate or a mixture of sodium carbonate and sodium bicarbonate as the only alkaline ingredients in a pressurized vessel at 90°-170° C in the presence of an oxygen-containing gas, subjecting waste liquor discharged from the pre-cooking and pulping steps to wet combustion to recover an alkaline aqueous substance and recycling the alkaline aqueous substance resulting from combustion to the pre-cooking and/or pulping steps.

Claims

1. A process for the manufacture of pulp in a closed system, which comprisesmixing a fibrous raw material with an alkaline aqueous solution of sodium carbonate or a mixture of a major proportion of sodium carbonate and a minor proportion of sodium bicarbonate as the only alkaline ingredients, which alkaline aqueous solution is completely free of sulfite and sulfide compounds and sulfur-containing ions resulting from dissolution of said compounds, the amount of sodium carbonate or mixture of sodium carbonate and sodium bicarbonate being 5 - 20% by weight, as sodium oxide, based on the weight of the raw material,pre-cooking the fibrous raw material in the alkaline aqueous solution at a temperature of 90°

to 190°

C,

3. defibrating the pre-cooked material by mechanical means,

4. removing a major proportion of waste liquor, formed during the pre-cooking step, from the defibrated material,

5. pulping the defibrated material in an alkaline aqueous solution of sodium carbonate or a mixture of a major proportion of sodium carbonate and a minor proportion of sodium bicarbonate as the only alkaline ingredients, which alkaline aqueous solution is completely free of sulfite and sulfide compounds and sulfur-containing ions resulting from dissolution of said compounds, the amount of sodium carbonate or mixture of sodium carbonate and sodium bicarbonate being 5 - 20% by weight, as sodium oxide, based on the weight of the raw material, in a pressurized pulping vessel at a temperature of 90°

to 170°

C in the presence of an oxygen-containing gas,

6. discharging waste liquor, formed during the pulping step, from the pulping vessel,

7. subjecting the waste liquor discharged from at least one of the pre-cooking and pulping steps to wet combustion, in which the waste liquor is treated at a temperature exceeding 230°

C in the presence of an oxygen-containing gas, to recover an alkaline aqueous substance containing sodium carbonate or a mixture of a major proportion of sodium carbonate and a minor proportion of sodium bicarbonate as the only alkaline ingredients and

8. recycling the recovered alkaline aqueous substance, without any chemical treatment thereof, to at least one of the pre-cooking and pulping steps.

2. The process according to claim 1, wherein after the defibration of the pre-cooked material, a major proportion of waste liquor formed during the pre-cooking step is separated from the defibrated material, the alkaline aqueous substance recovered from the wet combustion treatment is added to the defibrated material and pulping of the defibrated material is carried out.

3. The processs according to claim 1, wherein heavy metals contained in the recovered alkaline aqueous substance are removed from the substance after the wet combustion treatment by adsorbing the metal ions on a cation-exchange resin or by precipitating the metal ions as their sulfides.

4. The process according to claim 1, wherein after defibration of the pre-cooked material, a major proportion of waste liquor formed during the pre-cooking step is separated from the defibrated material, a supplementary alkaline aqueous solution of sodium carbonate as the only alkaline ingredient, which alkaline aqueous solution is completely free of sulfite and sulfide compounds and sulfur-containing ions resulting from dissolution of said compounds, is added to said defibrated material and pulping of said defibrated material is carried out.

5. The process according to claim 1, wherein the entire amount of the alkaline aqueous solution employed in the pulping step is present in admixture with the defibrated material before commencing the pulping step.