Methods for producing high-freeness pulp

• US 8,753,476 B2
• Filed: 09/22/2011
• Issued: 06/17/2014
• Est. Priority Date: 10/06/2010
• Status: Active Grant

• Current Assignee: Andritz Technology and Asset Management GmbH
• Original Assignee: Andritz Technology and Asset Management GmbH
• Inventors: Sabourin, Marc
• Primary Examiner(s): CALANDRA, ANTHONY J
• Application Number:
  US13/239,756
• Publication Number:
  US 20120085505A1
• Time in Patent Office: 999 Days
• Field of Search: 162/23, 162/24, 162/25, 162/26
• US Class Current: 162/24
• CPC Class Codes: D21B 1/02 Pretreatment of the raw materials by chemical or physical means removal of bark B27L
• CPC Class Codes: D21B 1/021 by chemical means
• CPC Class Codes: D21B 1/12 by wet methods, by the use of steam beaters D21D1/00
• CPC Class Codes: D21B 1/30 Defibrating by other means
• CPC Class Codes: D21D 1/30 Disc mills

Abstract

Methods of producing mechanical pulps from lignocellulosic material including partial defibration of lignocellulosic material in a chip press followed by liquid impregnation, preheating the lignocellulosic material for 20 seconds or less at a pressure between 7.5 and 12 bar (gauge) prior to mechanically refining the lignocellulosic material in a primary mechanical refiner at a pressure between 7.5 and 12 bar (gauge), thus obtaining a high freeness pulp.

Claims

1. A method of producing a mechanical pulp from lignocellulosic material in a pulping system comprising

a pretreatment subsystem comprising a pressure separated feeding device, a high compression device, and an impregnator, and

a production subsystem comprising a variable speed pressurized conveyor and a primary mechanical refiner,

the method comprising the following steps:

providing lignocellulosic material to the pressure separated feeding device and then transferring the lignocellulosic material to the high compression device;

wherein the step of destructuring the lignocellulosic material in the high compression device results in a destructured lignocellulosic material in which over 50% of the destructured lignocellulosic material by weight passes through a 16 mm screen perforation;

transferring the lignocellulosic material from the high compression device to the impregnator and impregnating the lignocellulosic material;

transferring the lignocellulosic material to the variable speed pressurized conveyor, wherein a residence time of the lignocellulosic material in the variable speed pressurized conveyor is 20 seconds, and wherein the variable speed pressurized conveyor operates at a pressure between 7.5 and 12 bar (gauge) and preheats the lignocellulosic material with steam;

transferring the lignocellulosic material to the primary mechanical refiner; and

mechanically refining the lignocellulosic material in the primary mechanical refiner at a pressure between 7.5 and 12 bar (gauge) to obtain a high freeness pulp.

2. The method of claim 1 further comprising the step of mixing the lignocellulosic material with at least a first chemical useful in chemi-mechanical pulping in the impregnator following the high compression device.

3. The method of claim 2, wherein the first chemical useful in chemi-mechanical pulping is selected from the group consisting of sodium sulfite, sodium bisulfite, sodium hydrosulfite, alkaline peroxide liquors, water, and white water.

4. The method of claim 1, further comprising the step of operating the pretreatment subsystem at a pressure of 0.1 to 3.0 bar (gauge).

5. The method of claim 1, further comprising operating the pretreatment subsystem such that the lignocellulosic material has a retention time of 5 to 20 seconds between the pressure separated feeding device and a chip plug in the high compression device.

6. The method of claim 1, wherein the pretreatment subsystem further comprises an atmospheric presteam bin and a second pressure separated feeding device between the impregnator and variable speed pressurized conveyor.

7. The method of claim 1 further comprising the step of operating the pretreatment subsystem under atmospheric pressure.

8. The method of claim 1 further comprising the step of mechanically refining the lignocellulosic material in the primary mechanical refiner at a speed greater than or equal to 2100 rpm.

9. The method of claim 1 further comprising the step of mechanically refining the lignocellulosic material in the primary mechanical refiner at a speed greater than or equal to 2500 rpm.

10. The method of claim 1 further comprising the step of operating the variable speed pressurized conveyor and the primary mechanical refiner at a pressure of 8.5 to 11 bar (gauge).

11. The method of claim 1, further comprising a step of impregnating the lignocellulosic material with at least a first chemical useful in chemi-mechanical pulping in the impregnator such that the impregnation results in a destructured lignocellulosic material in which over 65% of the destructured lignocellulosic material by weight passes through a 16 mm screen perforation.

12. The method of claim 1, wherein the production subsystem further comprises secondary refiner, the method further comprising the step of mechanically refining the lignocellulosic material in the secondary mechanical refiner downstream of the primary mechanical refiner, wherein the secondary refiner operates at a disc rotation rate lower than that of the primary mechanical refiner.

13. The method of claim 1, wherein the method makes a pulp having a freeness in a range between 300 ml to 600 ml.

14. The method of claim 1, wherein the method makes a fluff pulp, a tissue pulp, a towel pulp, or an absorbency pulp at freeness levels between 400 ml to 700 ml.

15. The method of claim 1, wherein the method makes a pulp suitable for paperboard.

16. The method of claim 1, wherein the method makes a pulp having a higher Scott Bond at a constant bulk than a comparative pulp made by a method in which the variable speed pressurized conveyor has a residence time of 100 seconds and operates at a pressure of 6.5 bar (gauge).

17. The method of claim 1, wherein the method makes a pulp having a lower skives content at a freeness of 600 ml than a comparative pulp made by a method in which the retention time between the feed screw and primary refiner has a residence time of 100 seconds and operates at a pressure of 6.5 bar (gauge).

18. The method of claim 1, wherein the method makes a pulp having a higher brightness than a comparative pulp made by a method in which the variable speed pressurized conveyor has a residence time of 100 seconds and operates at a pressure of 6.5 bar (gauge).

19. A method of producing a mechanical pulp from lignocellulosic material in a pulping system comprising a pretreatment subsystem comprising

a pressure separated feeding device, a high compression device, and an impregnator, and

a production subsystem comprising a variable speed pressurized conveyor and a primary mechanical refiner,

the method comprising the following steps:

providing lignocellulosic material to the pressure separated feeding device and then transferring the lignocellulosic material to the high compression device;

wherein the step of destructuring the lignocellulosic material in the high compression device results in a destructured lignocellulosic material in which over 50% of the destructured lignocellulosic material by weight passes through a 16 mm screen perforation;

transferring the lignocellulosic material from the high compression device to the impregnator and impregnating the lignocellulosic material;

transferring the lignocellulosic material to the variable speed pressurized conveyor, wherein a residence time of the lignocellulosic material in the variable speed pressurized conveyor is 20 seconds, and wherein the variable speed pressurized conveyor operates at a pressure between 7.5 and 12 bar (gauge) and preheats the lignocellulosic material with steam;

transferring the lignocellulosic material to the primary mechanical refiner; and

mechanically refining the lignocellulosic material in the primary mechanical refiner at a speed greater than or equal to 2000 rpm and at a pressure between 7.5 and 12 bar (gauge) to obtain a high freeness pulp.

20. The method of claim 19, wherein the step of impregnating the lignocellulosic material in the impregnator is performed with a chemical useful in chemi-mechanical pulping selected from the group consisting of sodium sulfite, sodium bisulfite, sodium hydrosulfite, alkaline peroxide liquors, water, and white water.