System for the production of a spinning dope composition

1. A spinning dope composition production system comprising:

a homogenization unit adapted for receiving cellulosic pulp material and alkali solution, the homogenization unit comprising a high shear mixing means for homogenizing cellulosic pulp material in alkali solution, said homogenization unit being arranged to supply a power density of at least 150 kW/m 3 (kW supplied to agitators per mixed unit of liquid volume) to the high shear mixing means in the homogenization unit; and

a dissolution unit adapted for receiving cellulosic pulp material homogenized in alkali solution from the homogenization unit, the dissolution unit comprising mixing means for mixing cellulosic pulp material in alkali solution, said dissolution unit being arranged to supply a power density of maximum 75 kW/m 3 (kW supplied to agitators per mixed unit of liquid volume) to the mixing means in the dissolution unit.

2. The system according to claim 1 , wherein the homogenization unit is arranged to supply a power density to the high shear mixing means in the range of 150-4000 kW/m 3 and wherein the dissolution unit is arranged to supply a power density to the mixing means in the dissolution unit of maximum 50 kW/m 3 .

3. The system according to claim 1 , wherein the dissolution unit comprises cooling means being integral and/or external of said dissolution unit.

4. The system according to claim 1 , wherein the homogenization unit comprises cooling means being integral and/or external of said homogenization unit.

5. The system according to claim 1 , wherein the dissolution unit and/or homogenization unit comprises cooling means being integral and/or external and wherein the cooling means is arranged to enable to keep the temperature in the cellulosic pulp material in alkali solution within a range of from −8 to −3° C. during the homogenization and during at least part of the dissolution.

6. The system according to claim 1 , wherein the system is a continuous operation system.

7. The system according to claim 1 , wherein the homogenization unit is arranged to be operated according to a plug flow principle.

8. The system according to claim 1 , wherein the homogenization unit comprises a high shear rotor-stator mixer.

9. The system according to claim 1 , wherein the homogenization unit comprises a twin axis counter rotating agitator.

10. The system according to claim 1 , wherein the mixing means of the dissolution unit is arranged to provide a rotation speed of less than 300 rpm.

11. The system according to claim 1 , wherein the system also comprises a mechanical working unit in which the dissolution is finalized by exposing the pulp material in the alkali solution to high shear forces.

12. The system according to claim 11 , wherein the mechanical working unit comprises a refining unit connected to the dissolution unit, said refining unit comprising shearing means.

13. The system according to claim 12 , wherein the refining unit is arranged to supply a power density (kW supplied to the refiner per mixed unit of liquid volume) in the range of 1000-8000 kW/m 3 .

14. The system according to claim 1 , wherein the system comprises multiple homogenization units and/or multiple dissolution units.

15. The system according to claim 1 , wherein the system also comprises means for addition of at least one additive to the cellulosic pulp material and/or to the cellulosic pulp material in alkali solution.

16. The system according to claim 1 , wherein the system is connected to at least on pre-treatment unit arranged before the homogenization unit, said pre-treatment unit being arranged for pre-treatment of the cellulosic pulp material before the homogenizing of the cellulosic pulp material in alkali solution.

17. The system according to claim 1 , wherein the system is connected to a unit for subsequent treatment of the produced spinning dope composition in a coagulation bath.

18. The system according to claim 1 , wherein the system is complemented with a subsequent filter unit for filtration of produced spinning dope composition.

19. The system according to claim 1 , wherein the cellulosic pulp material being processed is a non-derivatised or low-derivatised cellulose pulp.

20. The system according to claim 1 , wherein the homogenization unit is arranged to supply a power density to the high shear mixing means in the range of 200-2000 kW/m 3 .

21. The system according to claim 1 , wherein the homogenization unit is arranged to supply a power density to the high shear mixing means in the range of 150-2500 kW/m 3 .

22. The system according to claim 1 , wherein the dissolution unit is arranged to supply a power density to the mixing means in the dissolution unit in the range of 2-50 kW/m 3 .

23. The system according to claim 1 , wherein the dissolution unit is arranged to supply a power density to the mixing means in the dissolution unit in the range of 5-30 kW/m 3 .

24. The system according to claim 1 , wherein the system is a continuous operation system and wherein the average residence time of the alkali solution and cellulosic pulp material in the dissolution unit is at least 5 times larger than the average residence time of the alkali solution and cellulosic pulp material in the homogenization unit.

25. The system according to claim 1 , wherein the system is a continuous operation system and wherein the average residence time of the alkali solution and cellulosic pulp material in the dissolution unit is at least 10 times larger than the average residence time of the alkali solution and cellulosic pulp material in the homogenization unit.

26. The system according to claim 1 , wherein the homogenization unit is arranged to be operated according to a plug flow principle, and wherein the dissolution unit is arranged to be operated according to a continuous stirred tank reactor principle.

27. The system according to claim 12 , wherein the refining unit is arranged to supply a power density (kW supplied to the refiner per mixed unit of liquid volume) in the range of 1000-6000 kW/m 3 .

28. The system according to claim 12 , wherein the refining unit is arranged to supply a power density (kW supplied to the refiner per mixed unit of liquid volume) in the range of 2000-6000 kW/m 3 .

29. The system according to claim 12 , wherein the refining unit is arranged to supply a power density (kW supplied to the refiner per mixed unit of liquid volume) in the range of 3000-5000 kW/m 3 .

30. The system according to claim 12 , wherein the refining unit comprises at least two discs, and wherein at least one disc is arranged to rotate in relation to the other disc.

31. The system according to claim 12 , wherein the refining unit comprises at least two discs, and wherein the two discs are refining discs arranged on a common axis with a distance between them.

32. The system according to claim 1 , wherein the system also comprises means for addition of at least one additive to the cellulosic pulp material and/or to the cellulosic pulp material in alkali solution, and wherein the system comprises means for addition of at least one additive before or in the homogenization unit.

33. The system according to claim 1 , wherein the system also comprises means for addition of at least one additive to the cellulosic pulp material and/or to the cellulosic pulp material in alkali solution, and wherein said at least one additive being an additive for gelation prevention.

34. The system according to claim 1 , wherein the system also comprises means for addition of at least one additive to the cellulosic pulp material and/or to the cellulosic pulp material in alkali solution, and wherein said at least one additive being urea or comprising zinc.