Process and apparatus for circulating backwater in a papermaking machine

• US 5,567,278 A
• Filed: 11/03/1994
• Issued: 10/22/1996
• Est. Priority Date: 05/19/1992
• Status: Expired due to Term

• Current Assignee: POM Technology Oy AB
• Original Assignee: POM Technology Oy AB
• Inventors: Meinander, Paul O.
• Primary Examiner(s): Czaja, Donald E.
• Assistant Examiner(s): PADGETT, CALVIN F
• Application Number:
  US08/331,537
• Time in Patent Office: 719 Days
• Field of Search: 162/190, 162/189, 162/203, 162/264, 162/299, 162/301, 162/335, 162/337, 162/339, 162/359
• US Class Current: 162/190
• CPC Class Codes: D21F 1/66 Pulp catching, de-watering, or recovering; Re-use of pulp-water

Abstract

The invention relates to a process and an apparatus for recycling backwater in a papermaking machine. According to the invention backwater draining through a forming fabric is collected into several collecting means (51, 52, 53, 54) and pumped by separate pumps (20) in at least two and preferably numerous separate flows (81 to 85) directly as substantially air free separate flows to the fibre process (12, 30, 40) of the short circulation in order to implement a fast, air free and split recycling of backwater from said forming fabric to said fibre process.

Claims

1. A process for making paper or board while recycling backwater in a papermaking machine, the machine including a short circulation wherein the backwater draining through a paper forming fabric of the machine is used for papermaking stock dilution, the process comprising:

splitting at least a portion of the backwater draining through the forming fabric into at least two separate backwater flows; and

pumping each of said backwater flows directly and separately without passing through any open air-containing vessels, such that said backwater flows are substantially air free separate flows to at least two essentially separate points of short circulation stock dilution.

2. The process according to claim 1 wherein the portion of the backwater draining through a forming zone of said forming fabric is split and conducted to said short circulation in a direct, separate and air-free manner.

3. The process according to claim 1 wherein the portion of the backwater is split into, five to ten of the backwater flows.

4. The process according to claim 1 wherein the portion of the backwater draining through said forming fabric is split in a machine direction of motion of the forming fabric into 3 to 50 and in a cross direction perpendicular to the machine direction into 2 to 20 separate flows.

5. The process according to claim 1 wherein the portion of the backwater drained immediately downstream of a headbox of said papermaking machine is fed to a dilution point immediately upstream of said head box.

6. The process according to claim 2 wherein the backwater is fed directly as separate flows in the consecutive order of draining in the machine direction so that the flow first drained is fed into a last dilution stage, the second flow drained is fed to a next to last dilution stage, and so on.

7. The process according claim 1 wherein the portion of the backwater draining through said forming fabric is collected as separate flows into flooded draining boxes disposed below said forming fabric.

8. A process according to claim 1 wherein air is removed from the drained backwater by means of gas separation pumps.

9. The process according to claim 8 wherein the portion of the backwater drained through said forming fabric is fed by gas separation pumps as multiple separate flows free of air and without open vessels to process stages of the process.

10. The process according to claim 2 wherein the backwater is split into five to ten separate flows.

11. The process according to claim 6 wherein air is removed from the drained backwater by means of gas separation pumps.

12. The process according to claim 1 wherein the portion of the backwater is split into 15 or more separate flows.

13. The process according to claim 1 wherein each of the backwater flows draining through a forming zone of the forming fabric is pumped directly to a respective one of the separate points of short circulation stock dilution.

14. The process according to claim 1 wherein the backwater flows are pumped through a common backwater distribution system prior to delivery to the separate points of short circulation stock dilution.

15. The process according to claim 1 wherein the backwater flows are maintained at a speed of at least 3 meters per second.

16. The process according to claim 2 wherein the portion of the backwater is split into 15 or more separate flows.

17. The process according to claim 16 wherein said pumps comprise gas separation pumps.

18. The process according to claim 1, including a respective pump in each of said separate backwater flows, each respective pump pumping to one of the separate points of short circulation stock dilution.

19. An apparatus for circulating backwater in a papermaking machine having a short circulation, the machine comprising

at least two stock dilution devices in flow communication with the short circulation,

a headbox (50),

a looped forming fabric (60),

at least two separate backwater collecting means (51, 52, 53, 54;

51A, 52A, 53A,

     53) for collecting backwater draining through said forming fabric (60), at least two of said collecting means being in direct flow communication with a respective pump (20;

20,

     21) for returning backwater collected therein directly and separately without passing through any open air-containing vessels, such that the backwater is in a substantially air-free condition, to said at least two separate stock dilution devices (12, 30, 40;

111, 112, 113, 114, 115,

     116) or substantially separate water distribution means in flow communication with the stock dilution devices (80),

whereby a fast, air free and split recycling of backwater is implemented.

20. The apparatus according to claim 19 wherein there are 3 to 50 backwater collecting means in a machine direction of motion of the forming fabric and 2 to 20 backwater collecting means in a cross direction perpendicular to the machine direction.

21. The apparatus according to claim 19 wherein said pumps (20, 21) comprise gas separation pumps.

22. The apparatus according to claim 19 wherein the backwater collected in backwater water collecting means (51) closest downstream of said headbox (50) is connected to a first dilution point (40;

41) closest upstream of said headbox (50).

23. The apparatus according to claim 22 wherein the backwater collected in further water collecting means (52) downstream of said headbox (50) is connected to the first dilution point or a second dilution point next to closest (30;

31) upstream of said headbox (50) .

24. The apparatus according to claim 22 wherein said first dilution point closest upstream of said headbox comprises a pressurized screen (40), which functions in one stage without recycling of rejects, and

said second dilution point next to closest upstream of said headbox comprises a centrifugal cleaner (30), which functions in one stage without recycling of rejects.

25. The apparatus according to claim 19 wherein said backwater collecting means (51A, 52A, 53A) at a forming zone (61) are flat draining boxes (51A, 51B) flooded by water.

26. The apparatus according to claim 20 wherein said pumps (20, 21) comprise gas separation pumps.

27. The apparatus according to claim 26 wherein the backwater collected in backwater water collecting means (51) closest downstream of said headbox (50) is connected to a dilution point (40;

41) closest upstream of said headbox (50).

28. The apparatus according to claim 19 including means for maintaining the backwater flows at a speed of at least 3 meters per second.

29. The apparatus according to claim 20 wherein said backwater collecting means in the machine direction are connected to separate respective pumps.

30. The apparatus according to claim 20 wherein said backwater collecting means in the cross direction are connected to separate respective pumps.

31. The apparatus according to claim 29 wherein said pumps comprise gas separation pumps.