Method and system for energy savings in TMP by high temperature LC/MC refining of pulp

• US 7,540,938 B2
• Filed: 06/02/2006
• Issued: 06/02/2009
• Est. Priority Date: 06/03/2005
• Status: Expired due to Fees

• Current Assignee: Andritz AG
• Original Assignee: Andritz AG
• Inventors: Munster, Heinrich
• Primary Examiner(s): Halpern; Mark
• Application Number:
  US11/421,784
• Publication Number:
  US 20070119557A1
• Time in Patent Office: 1,096 Days
• Field of Search: 162/47, 162/19, 162/17
• US Class Current: 162/47
• CPC Class Codes: D21B 1/12 by wet methods, by the use of steam beaters D21D1/00
• CPC Class Codes: D21C 3/22 Other features of pulping processes
• CPC Class Codes: D21C 9/007 by mechanical or physical means
• CPC Class Codes: D21D 1/20 Methods of refining
• CPC Class Codes: Y02P 70/10 Greenhouse gas [GHG] capture, material saving, heat recovery or other energy efficient measures, e.g. motor control, characterised by manufacturing processes, e.g. for rolling metal or metal working

Abstract

A method for recovering heat from a pulp refining process comprising: discharging pressurized pulp from a high pressure refiner, wherein the pressurized pulp comprises a pressurized slurry of fibers and liquid; introducing at least the liquid from the pressurized pulp slurry to a pressurized flash tank; exchanging heat from the pressurized flash tank with water, such that the water is heated, and using the heated water in the pulp refining process.

Claims

1. A method for recovering heat from a pulp refining process comprising:

discharging pressurized pulp from a high pressure mechanical refiner, wherein the pressurized pulp comprises a pressurized slurry of fibers and liquid;

introducing at least the liquid from the pressurized pulp to a pressurized flash tank;

separating pressurized steam from pressurized pulp in the pressurized flash tank, and

using the separated pressurized steam in the pulp refining process.

2. The method of claim 1 wherein the at least the liquid from the pressurized pulp comprises all of the pressurized pulp slurry which is introduced directly from the high pressure mechanical refiner to the pressurized flash tank.

3. The method of claim 1 further comprises discharging the pressurized pulp from the pressurized flash tank to a heat exchanger;

and

heating dilution water in the heat exchanger with heat from the pressurized pulp.

4. The method of claim 3 further comprising feeding the heated dilution water to a pressurized cyclone upstream of the high pressure mechanical refiner.

5. The method of claim 4 wherein the dilution water is fed to a water-lock of the cyclone.

6. The method of claim 4 wherein the pulp refining process takes place in a pulp mill and the separated pressurized steam from the pressurized cyclone is used as pressurized steam in a separate process in the pulp mill.

7. The method of claim 1 wherein the pressurized pulp is pressurized to between 3 to 6 bars in the high pressure mechanical refiner.

8. The method of claim 1 wherein the pressurized pulp is a low consistency pulp slurry and has a temperature of at least 140°

C. in the high pressure mechanical refiner.

9. The method of claim 1 wherein the pressurized pulp has a consistency of 4% to 5% fiber in the pressurized pulp slurry.

10. The method of claim 1 wherein the pressurized pulp is a medium consistency pulp slurry and has a temperature of at least 140°

C. in the high pressure mechanical refiner.

11. The method of claim 1 wherein the pressurized pulp has a pulp consistency of at least 10% in the pressurized pulp slurry, and the method further comprises introducing the discharged pressurized pulp to a press and extracting filtrate from the pressurized pulp slurry in the press which discharges the filtrate to the pressurized flash tank and the press discharges a pulp pressate having a consistency of 30% pulp to 35% pulp.

12. The method of claim 1 further comprising passing the discharged pressurized pulp through a screw press and extracting filtrate from the pressurized pulp and separately extracting a pulp pressate from the pressurized pulp, wherein the filtrate is introduced into the flash tank.

13. The method of claim 1 wherein the pulp refining process takes place in a pulp mill and the separated pressurized steam from the pressurized flash tank is used as pressurized steam in a separate process in the pulp mill.

14. A method to recover high pressure steam a mechanical pulp refining process comprising:

introducing a pressurized pulp slurry to a high pressure mechanical refiner, wherein the pulp slurry comprises fibers and liquid;

refining the pressurized pulp slurry in the refiner;

discharging a refined pressurized pulp slurry from the mechanical refiner;

introducing a least a liquid portion of the discharged refined pressurized pulp slurry to a pressurized flash tank;

separating pressurized steam from at least a liquid portion of the discharged refined pressurized pulp slurry in the pressurized flash tank;

applying the separated pressurized steam from the flash tank for use in another process in a pulp mill.

15. The method in claim 14 wherein the pressurized pulp slurry introduced to the high pressure mechanical refiner has a consistency of no more than 5% fibers.

16. The method in claim 14 further comprising:

introducing the pressurized pulp slurry to a pressurized cyclone, extracting steam from the pressurized pulp slurry;

using the pressurized pulp slurry discharged from the cyclone as the pressurized pulp slurry introduced to the high pressure mechanical refiner;

heating water in a heat exchanger with heat energy from the pressurized refined pulp discharged from the flash tank, and

introducing the heated water from the heat exchanger to the pressurized cyclone.

17. The method in claim 14 further comprising separating the liquid in the refined pressurized pulp slurry in a press, separating the liquid from the pulp slurry in the press and introducing to the pressurized flash tank the separated liquid.

18. The method in claim 14 wherein an entirety of the refined pressurized pulp slurry is introduced into the pressurized flash tank.