Chemithermomechanical pulping process employing separate alkali and sulfite treatments

• US 4,486,267 A
• Filed: 11/14/1983
• Issued: 12/04/1984
• Est. Priority Date: 11/14/1983
• Status: Expired due to Fees

• Current Assignee: MEAD Corporation Courthouse Plaza NE Dayton
• Original Assignee: MEAD Corporation (Meadwestvaco Corporation)
• Inventors: Prusas, Zenon C.
• Primary Examiner(s): SMITH, WILLIAM F
• Application Number:
  US06/551,392
• Time in Patent Office: 386 Days
• Field of Search: 162/25, 162/26, 162/28, 162/19, 162/71, 162/18, 162/83, 162/84, 162/86
• US Class Current: 162/25
• CPC Class Codes: D21B 1/021 by chemical means
• CPC Class Codes: D21C 1/06 with alkaline reacting compounds
• CPC Class Codes: D21C 1/08 with oxygen-generating compounds
• CPC Class Codes: D21C 3/12 sodium bisulfite

Abstract

A high yield chemithermomechanical (CTMP) process for obtaining high strength hardwood pulps is disclosed wherein hardwood chips are subjected to a two-stage chemical treatment prior to defibration, the first consisting of chip impregnation and reaction with an alkaline liquor followed by a second stage treatment with sulfite and/or bisulfite; in one embodiment peroxide is added to the alkaline liquor to enhance brightness.

Claims

1. A process for the production of hardwood chemithermomechanical pulp, said process being characterized by a pulp yield of at least 80% based on dry wood chips, said process comprising the steps of:

(a) impregnating hardwood chips with an alkaline liquor, said alkaline liquor being an aqueous solution containing about 3 to 10% sodium hydroxide based on bone dry chips;

(b) maintaining said impregnated chips of step (a) for a period of time sufficient to permit chemical softening of said chips;

(c) removing said alkaline liquor from said chips;

(d) impregnating said alkaline softened chips with a sulfite liquor, said sulfite liquor being an aqueous solution containing about 2 to 10% by weight sodium sulfite or sodium bisulfite based on dry wood chips;

(e) cooking the impregnated chips of step (d) in said sulfite liquor at a temperature of approximately 120°

to 180°

C. for a period of time sufficient to sulfonate the lignin in said chips and further soften said chips without removing substantial amounts of lignin; and

(f) defibrating the chips of step (e) by passing said chips through a refining apparatus.

2. The pulping process of claim 1 wherein said hardwood chips are destructured prior to said step (a).

3. The pulping process of claim 2 wherein said hardwood chips are subjected to steam prior to being destructured.

4. The pulping process of claim 3 wherein said hardwood chips are destructured by compressing said chips and said chips are impregnated with said alkaline liquor by allowing said compressed chips to expand in said liquor.

5. The pulping process of claim 4 wherein said alkaline softened chips of step (b) are compressed to remove said spent liquor from said chips and said chips are impregnated with said sulfite liquor by allowing said compressed chips to expand in said sulfite liquor.

6. The pulping process of claim 5 wherein said chips are maintained in said alkaline liquor for a period of approximately 5 minutes to 3 hours.

7. The pulping process of claim 6 wherein said chips are maintained in said sulfite liquor for a period of approximately 15 to 45 minutes.

8. The pulping process of claim 7 wherein said chips are defibrated at a consistency of approximately 10 to 35%.

9. The pulping process of claim 1 wherein said alkaline liquor additionally contains approximately 0.5 to 4% hydrogen peroxide based on dry wood chips.

10. The pulping process of claim 1 wherein said sulfite liquor has a ph of about 5 to 9.

11. A process for the production of chemithermomechanical hardwood pulp, said process being characterized by a pulp yield of at least 80% based on dry wood chips;

said process comprising the steps of;

(a) steaming hardwood chips;

(b) compressing said steamed chips to destructure said chips;

(c) impregnating said compressed chips with an alkaline peroxide liquor by allowing said compressed chips to expand in said alkaline peroxide liquor, said alkaline peroxide liquor being an aqueous solution containing about 0.5 to about 4% hydrogen peroxide, about 3 to about 10% sodium hydroxide, both based on dry wood chips;

(d) maintaining said impregnated chips of steps (c) in said alkaline liquor for a period of approximately 5 minutes to 3 hours to permit chemical softening of said chips;

(e) compressing said alkaline softened chips of step (d) to remove the said alkaline peroxide liquor,

(f) impregnating said alkaline softened chips with a sulfite liquor by allowing said compressed chips of step (e) to expand in said sulfite liquor, said sulfite liquor being an aqueous solution containing about 2 to 10% sodium sulfite or sodium bisulfite;

(g) cooking said impregnated chips of step (f) at a temperature of approximately 120°

to 180°

C. for approximately 15 to 45 minutes to permit further softening of said chips without removing substantial quantities of lignin from said chips;

(h) defibrating said chips of step (f) by passing said chips through a refining apparatus at a consistency of approximately 10 to 35%; and

(i) recovering said pulp from said refining apparatus.

12. The pulping process of claim 11 wherein said process is carried out on a continuous basis.

13. The pulping process of claim 11 wherein said sulfite liquor contains sodium sulfite.

14. The pulping process of claim 11 wherein said chips are maintained in said sulfite liquor at a temperature of about 140°

to 160°

C.

15. The pulping process of claim 11 wherein said steps (b) and (e) are carried out using a screw press.

16. The pulping process of claim 11 wherein said sulfite liquor has a pH of about 5 to 9.