Process and apparatus for manufacturing a styrene polymer in a mechanically stirred reactor
View Patent ↗Process and apparatus for the (co) polymerization of styrene. The process is carried out by employing a liquid polymerization reaction mixture that includes styrene, in a mechanically stirred reactor in the form of a vessel comprising a side wall having the shape of a cylinder of revolution with a vertical axis (A), a bottom head and a top head that are joined to the side wall. The vessel is provided with a mechanical stirring device comprising (i) a central shaft of vertical axis coincident with the axis (A), connected to a drive system comprising a motor for rotating the central shaft, (ii) at least one baffle attached to the vessel. The baffle is away from the side wall of the vessel and takes the form of a cylinder of vertical axis and of rhomboidal cross section.
1. Process for the (co)polymerization of styrene, carried out by employing a liquid polymerization reaction mixture that includes styrene, in a mechanically stirred reactor in the form of a vessel comprising a side wall having the shape of a cylinder of revolution with a vertical axis (A), a bottom head and a top head that are joined to the side wall, the vessel being provided with a mechanical stirring device comprising (i) a central shaft of vertical axis coincident with the axis (A), connected to a drive system comprising a motor for rotating the central shaft, (ii) at least one stirring member attached to the central shaft and (iii) at least one baffle attached to the vessel, wherein the baffle is away from the side wall of the vessel and takes the form of a cylinder of vertical axis and of cross section chosen from one of the three following shapes:
a first shape comprising a rhombus possessing a long diagonal and a short diagonal, which have respective lengths (D) and (d) such that the ratio (D/d) is chosen within a range from 0.1/1 to 0.9/1, the short diagonal being directed along a radial direction with respect to the axis (A) or along a direction making an angle (α) of greater than 0 and less than or equal to 45° to the said radial direction;
a second shape comprising a rhombus identical to that of the first shape, except that each of the two acute angles located at the ends of the long diagonal is replaced with an identical or different circular arc, having a centre located on the long diagonal, a radius of length (r) such that the ratio (2r/d) is chosen within a range from 0.1/1 to 0.8/1, and two ends contiguous with the two respective sides of the acute angle; and
a third shape comprising a rhombus identical to that of the second shape, except that only the acute angle located at the end of the long diagonal and facing in the opposite direction to the rotation of the central shaft is replaced with the circular arc.
2. Process according to claim 1 , wherein the stirring member or members are chosen from members generating radial flow.
3. Process according to claim 1 , wherein the stirring member or members are chosen from dual-flow screw impellers, screw impellers with thin-profile blades or profiled blades, turbine impellers with inclined blades, single-spiral or double-spiral Archimedian screws and single-, double-, triple- or quadruple-helical ribbon stirrers, optionally combined with an Archimedian screw.
4. Process according to claim 1 , wherein the stirring member or members are chosen from screw impellers having thin-profile blades or profiled blades and inclined turbine impellers, and from among single-, double- or triple-helical ribbon stirrers.
5. Process according to claim 1 , wherein the stirring member or members are chosen from single-, double- or triple-helical ribbon stirrers, combined with a bottom stirring member.
6. Process according to claim 1 , wherein the ratio (d/D) is chosen within a range from 0.2/1 to 0.8/1.
7. Process according to claim 1 , wherein the ratio (2r/d) is chosen within a range from 0.2/1 to 0.7/1.
8. Process according to claim 1 , wherein, in the second or third shape of the cross section of the baffle, each end of the circular arc is joined to the respective side of the acute angle to which the arc is joined, along a tangent to the circular arc which, at the joining point, is coincident with the direction of the said side.
9. Process according to claim 1 , wherein the styrene (co)polymerization is a radical polymerization reaction initiated thermally or using at least one catalyst that generates free radicals.
10. Process according to claim 1 , wherein the liquid polymerization reaction mixture comprises:
styrene and, optionally, at least one comonomer, a natural or synthetic rubber, and/or at least one polymerization initiator; or
styrene, an organic solvent and, optionally, at least one comonomer, a natural or synthetic rubber, and/or a polymerization initiator; or
styrene, water, at least one suspension or emulsion stabilizer and, optionally, at least one comonomer, a natural or synthetic rubber, and/or at least one polymerization initiator.
11. Process according to claim 1 , wherein the stirring member or members generate a shear rate of 2 to 60 s −1 .
12. Process according to claim 1 , wherein the central shaft rotates at a speed of 10 to 50 revolutions per minute.
13. Process according to claim 1 , wherein the stirring member or members are chosen from members generating axial or essentially axial flow.
14. Process according to claim 4 , wherein the stirring member or members are chosen from screw impellers having thin-profile blades or profiled blades and inclined turbine impellers in an aqueous suspension polymerization process, and from among single-, double- or triple-helical ribbon stirrers in a bulk or solution polymerization process.
15. Process according to claim 5 , wherein the stirring member or members are chosen from single-, double- or triple-helical ribbon stirrers, combined with a bottom stirring member having the shape of an anchor and which is attached to the same central rotation shaft.
16. Process according to claim 6 , wherein the ratio (d/D) is chosen within a range from 0.25/1 to 0.65/1.
17. Process according to claim 7 , wherein the ratio (2r/d) is chosen within a range from 0.35/1 to 0.65/1.
18. Process according to claim 10 , wherein the natural or synthetic rubber is a polybutadiene and the polymerization initiator is a free radical generator.
19. Process according to claim 11 , wherein the stirring member or members generate a shear rate of 5 to 50 s −1 .
20. Process according to claim 12 , wherein the central shaft rotates at a speed of 12 to 45 revolutions per minute.
21. Polymerization apparatus, capable of (co)polymerizing styrene, comprising a mechanically stirred reactor in the form of a vessel comprising a side wall having the shape of a cylinder of revolution with a vertical axis (A), a bottom head and a top head that are joined to the side wall, the vessel being provided with a mechanical stirring device comprising (i) a central shaft of vertical axis coincident with the axis (A), connected to a drive system comprising a motor for rotating the central shaft, (ii) at least one stirring member attached to the central shaft and (iii) at least one baffle attached to the vessel, wherein the baffle is away from the side wall of the vessel and takes the form of a cylinder of vertical axis and of cross section chosen from one of the three following shapes:
a first shape comprising a rhombus possessing a long diagonal and a short diagonal, which have respective lengths (D) and (d) such that the ratio (d/D) is chosen within a range from 0.1/1 to 0.9/1, the short diagonal being directed along a radial direction with respect to the axis (A) or along a direction making an angle (α) of greater than 0 and less than or equal to 45° to the said radial direction;
a second shape comprising a rhombus identical to that of the first shape, except that each of the two acute angles located at the ends of the long diagonal is replaced with an identical or different circular arc, having a centre located on the long diagonal, a radius of length (r) such that the ratio (2r/d) is chosen within a range from 0.1/1 to 0.8/1, and two ends contiguous with the two respective sides of the acute angle; or
a third shape comprising a rhombus identical to that of the second shape, except that only the acute angle located at the end of the long diagonal and facing in the opposite direction to the rotation of the central shaft is replaced with the circular arc.
22. Apparatus according to claim 21 , wherein the stirring member or members are chosen from members generating radial flow.
23. Apparatus according to claim 21 , wherein the stirring member or members are chosen from dual-flow screw impellers, screw impellers with thin-profile blades or profiled blades, turbine impellers with inclined blades, single-spiral or double-spiral Archimedian screws and single-, double-, triple- or quadruple-helical ribbon stirrers.
24. Apparatus according to claim 21 , wherein the stirring member or members are chosen from single-, double-, triple- or quadruple-helical ribbon stirrers, combined with a bottom stirring member.
25. Apparatus according to claim 21 , wherein the ratio (d/D) is chosen within a range from 0.2/1 to 0.8/1.
26. Apparatus according to claim 21 , wherein the ratio (2r/d) is chosen within a range from 0.2/1 to 0.7/1.
27. Apparatus according to claim 21 , wherein, in the second or third shape of the cross section of the baffle, each end of the circular arc is joined to the respective side of the acute angle to which the arc is joined, along a tangent to the circular arc which, at the joining point, is coincident with the direction of the said side.
28. Apparatus according to claim 21 , wherein the stirring member or members are chosen from members generating axial or essentially axial flow.
29. Apparatus according to claim 23 , wherein the stirring member or members are combined with an Archimedian screw.
30. Apparatus according to claim 24 , wherein the bottom stirring member has the shape of an anchor.
31. Apparatus according to claim 25 , wherein the ratio (d/D) is chosen within a range from 0.25/1 to 0.65/1.
32. Apparatus according to claim 26 , wherein the ratio (2r/d) is chosen within a range from 0.35/1 to 0.65/1.