초록 ▼

A compound plant for processing elastomeric compounds for tires with both a high quality and a high throughput includes at least one batch mixing device in combination with at least one multi-shaft continuous mixing device having a high number of shafts. For example, the multi-shaft continuous mixin

A compound plant for processing elastomeric compounds for tires with both a high quality and a high throughput includes at least one batch mixing device in combination with at least one multi-shaft continuous mixing device having a high number of shafts. For example, the multi-shaft continuous mixing device could be a ring extruder having a plurality of co-rotating screws disposed to form a ring. In operation, a first elastomeric compound is discharged from the at least one batch mixing device and processed with the at least one multi-shaft continuous mixing device to obtain a second elastomeric compound.

대표청구항 ▼

1. A process for manufacturing a tyre comprising: providing at least one crosslinkable elastomeric compound;manufacturing a plurality of structural elements of said tyre, wherein at least one structural element of said plurality of structural elements comprises said at least one crosslinkable elasto

1. A process for manufacturing a tyre comprising: providing at least one crosslinkable elastomeric compound;manufacturing a plurality of structural elements of said tyre, wherein at least one structural element of said plurality of structural elements comprises said at least one crosslinkable elastomeric compound;manufacturing a green tyre using said plurality of structural elements; andsubjecting the green tyre to moulding and crosslinking to obtain a finished tyre,wherein providing of said at least one crosslinkable elastomeric compound comprises:feeding at least one elastomeric polymer and at least one reinforcing filler to a mixing apparatus comprising at least one batch mixing device;mixing and dispersing, in said mixing apparatus, said at least one reinforcing filler in said at least one elastomeric polymer, so as to obtain a first elastomeric compound;discharging said first elastomeric compound from said mixing apparatus;feeding said first elastomeric compound to at least one multi-shaft continuous mixing device, said at least one multi-shaft continuous mixing device being a ring extruder comprising an inner core, an outer housing defining with said inner core an annular chamber, and at least six rotating screws, wherein said ring extruder comprises at least one gas outlet opening provided in said outer housing;mixing said first elastomeric compound in said at least one multi-shaft continuous mixing device, so as to obtain a second elastomeric compound; andapplying vacuum to said at least one gas outlet opening during mixing of said first elastomeric compound in said ring extruder. 2. The process according to claim 1, wherein said at least one batch mixing device is selected from internal mixers and open mixers. 3. The process according to claim 1, wherein mixing in said at least one batch mixing device is carried out at a rotor speed of about 20 rpm to about 60 rpm. 4. The process according to claim 3, wherein mixing in said at least one batch mixing device is carried out at a rotor speed of about 30 rpm to about 50 rpm. 5. The process according to claim 1, wherein mixing in said at least one batch mixing device is carried out using a fill factor of the mixing chamber not higher than about 80%. 6. The process according to claim 5, wherein mixing in said at least one batch mixing device is carried out using a fill factor of the mixing chamber from about 55% to about 70%. 7. The process according to claim 1, wherein said at least one multi-shaft continuous mixing device comprises at least six co-rotating screws. 8. The process according to claim 1, wherein said at least one multi-shaft continuous mixing device comprises at least twelve rotating screws. 9. The process according to claim 1, wherein said rotating screws have a diameter of at least 30 mm. 10. The process according to claim 9, wherein said rotating screws have a diameter of at least 60 mm. 11. The process according to claim 1, wherein mixing in said at least one multi-shaft continuous mixing device is carried out at a screw rotation speed between about 10 rpm and about 600 rpm. 12. The process according to claim 11, wherein mixing in said at least one multi-shaft continuous mixing device is carried out at a screw rotation speed between about 40 rpm and about 400 rpm. 13. The process according to claim 1, wherein the first elastomeric compound is fed to at least one conveying extruder before being fed to said at least one multi-shaft continuous mixing device. 14. The process according to claim 1, wherein providing said at least one crosslinkable elastomeric compound comprises feeding said second elastomeric compound to at least one further batch mixing device. 15. The process according to claim 1, further comprising discharging said second elastomeric compound from said multi-shaft continuous mixing device at an average throughput of at least 500 kg/h.