Method for producing chemical pulp from hardwood chips

• US 5,413,677 A
• Filed: 04/05/1993
• Issued: 05/09/1995
• Est. Priority Date: 04/05/1993
• Status: Expired due to Term

• Current Assignee: Kamyr, Inc.
• Original Assignee: Kamyr, Inc.
• Inventors: Collins, Robert H.
• Primary Examiner(s): Jones, W. Gary
• Assistant Examiner(s): NGUYEN, TAN D
• Application Number:
  US08/041,572
• Time in Patent Office: 764 Days
• Field of Search: 162/19, 162/17, 162/29, 162/39, 162/42, 162/242, 162/249
• US Class Current: 162/42
• CPC Class Codes: D21C 3/24 Continuous processes
• CPC Class Codes: D21C 7/06 Feeding devices

Abstract

Chemical pulp is produced from hardwood chips in a simplified manner utilizing a continuous digester. An inverted top separator is provided in the circulatory loop between the high pressure feeder and the top of the continuous digester for thermally isolating circulations on either side of the inverted top separator. Relatively cool liquor circulates between the inverted top separator and high pressure feeder, at a temperature such that it will not flash into steam in a high pressure feeder, while in the circulatory loop from the high pressure feeder to the digester the chips are in cooking liquor at cooking temperature. Since hardwood chips require less cooking than softwood chips, a single heating source for heating the liquor to cooking temperature is provided, external of the digester, and a conventional cooking circulation loop within the digester is not required.

Claims

1. A method of producing chemical pulp from hardwood chips, using a vertical digester having a top and a bottom and a cooking zone, and a high pressure feeder, comprising the steps of continuously and substantially sequentially:

(a) steaming the hardwood chips;

(b) entraining the hardwood chips in alkaline cooking liquor at a relatively cool temperature, so that the liquor will not significantly flash into steam in a high pressure feeder;

(c) feeding the chips entrained in relatively cool liquor under high pressure to a point external of the top of the digester using the high pressure feeder;

(d) at said point external of the digester, replacing the relatively cool liquor entraining the chips with relatively hot cooking liquor, at cooking temperature, and recirculating the replaced relatively cool liquor to the high pressure feeder, so as to thermally isolate the high pressure feeder from the digester;

(e) feeding the hardwood chips entrained in cooking liquor at cooking temperature directly to the cooking zone at the top of the digester;

(f) at the top of the digester, separating some liquor from the chips;

(g) recirculating and reheating the liquor separated from the chips in step (f), to provide a significant part of the cooking liquor in step (d); and

(h) cooking the chips in the digester in a cooking zone, to ultimately produce chemical hardwood pulp, and removing the hardwood pulp from the bottom of the digester.

2. A method as recited in claim 1 wherein step wherein steps (b) and (c) are practiced with cooking liquor at a temperature of roughly 240°

F., and wherein steps (d) and (g) are practiced with cooking liquor at roughly 290°

F.

3. A method as recited in claim 2 comprising the further step of adding cooking liquor to the liquor separated during the practice of step (f), prior to reheating in step (g).

4. A method as recited in claim 3 wherein step (h) is practiced without the addition of heat during the cooking zone, utilizing only the heat provided from the cooking liquor added in step (d).

5. A method as recited in claim 4 comprising the further steps of, after step (h):

further cooking the chips in a modified cooking zone;

washing the chips in a washing zone in the digester; and

withdrawing, heating, and recirculating liquors in the modified cooking and washing zones.

6. A method as recited in claim 5 wherein step (d) is practiced utilizing an inverted top separator.

7. A method as recited in claim 1 comprising the further step of adding cooking liquor to the liquor separated during the practice of step (f), prior to reheating in step (g).

8. A method as recited in claim 1 wherein step (h) is practiced without the addition of heat during the cooking zone, utilizing only the heat provided from the cooking liquor added in step (d).

9. A method as recited in claim 1 comprising the further steps of, after step (h):

further cooking the chips in a modified cooking zone;

washing the chips in a washing zone in the digester; and

withdrawing, heating, and recirculating liquors in the modified cooking and washing zones.

10. A method as recited in claim 1 wherein step (d) is practiced utilizing an inverted top separator.

11. A method as recited in claim 1 wherein the cooking liquor is kraft cooking liquor, and wherein steps (a)-(h) are practiced to produce kraft pulp.

12. A method as recited in claim 11 wherein steps (b) and (c) are practiced with cooking liquor at a temperature of roughly 240°

F., and wherein steps (d) and (g) are practiced with cooking liquor at roughly 290°

F.

13. A method as recited in claim 12 comprising the further step of adding cooking liquor to the liquor separated during the practice of step (f), prior to reheating in step (g).

14. A method as recited in claim 13 wherein step (h) is practiced without the addition of heat during the cooking zone, utilizing only the heat provided from the cooking liquor added in step (d).

15. A method as recited in claim 14 comprising the further steps of, after step (h):

further cooking the chips in a modified cooking zone;

washing the chips in a washing zone in the digester; and

withdrawing, heating, and recirculating liquors in the modified cooking and washing zones.

16. A method as recited in claim 15 wherein step (d) is practiced utilizing an inverted top separator.