Propylene polymer with improved processability in thermoforming

1. A propylene polymer comprising at least one comonomer and at least two propylene polymer fractions of different melt flow index, said propylene polymer being characterized by

a melt flow index ranging from 0.5 dg/min to 8.0 dg/min, determined according to ISO 1133, condition L at 230° C. and 2.16 kg,

a xylene solubles content ranging from 1.0 wt % to 4.0 wt %, relative to a total weight of the propylene polymer, and

a total comonomer content of from 0.1 wt % to 1.0 wt %, relative to the total weight of the propylene polymer,

wherein the fraction with the lowest melt flow index has a melt flow index ranging from 0.2 dg/min to 1.0 dg/min, determined according to ISO 1133, condition L at 230° C. and 2.16 kg;

wherein each of the at least two propylene polymer fractions has substantially the same comonomer content and, relative to the comonomer content of the propylene polymer fraction with the lowest melt flow index, the comonomer content of the other propylene polymer fraction is from 70% to 130%, under the provision that each of the at least two propylene polymer fractions comprises comonomer.

2. The propylene polymer according to claim 1 , wherein the melt flow index ranges from 1.0 dg/min to 5.0 dg/min, determined according to ISO 1133, condition L, at 230° C. and 2.16 kg.

3. The propylene polymer according to claim 1 , wherein the total comonomer content ranges from 0.2 wt % to 0.8 wt %, relative to the total weight of the propylene polymer.

4. The propylene polymer according to claim 1 , wherein the xylene solubles content is ranges from 1.3 wt % to 3.5 wt %, relative to the total weight of the propylene polymer.

5. The propylene polymer according to claim 1 , wherein the fraction with the lowest melt flow index has a melt flow index ranging from 0.3 dg/min to 0.9 dg/min, determined according to ISO 1133, condition L, at 230° C. and 2.16 kg.

6. The propylene polymer according to claim 1 , wherein the propylene polymer comprises from 50 wt % to 70 wt %, relative to the total weight of the propylene polymer, of the propylene polymer fraction with the lowest melt flow index.

7. The propylene polymer according to claim 1 , wherein each of the at least two propylene polymer fractions has the same comonomer content.

8. The propylene polymer according to claim 1 , wherein at least 60 mol % of the total amount of comonomer is present as single comonomer units.

9. A thermoformed article comprising the propylene polymer of claim 1 .

10. A process for the production of the propylene polymer of claim 1 in presence of

(i) at least two Ziegler-Natta polymerization catalysts having different internal donors, each Ziegler-Natta polymerization catalyst having a different hydrogen response, each of said Ziegler-Natta catalysts comprising a titanium compound, which has at least one titanium-halogen bond, and an internal donor, both supported on magnesium halide in active form,

(ii) an organo aluminium compound (Al),

(iii) an external electron donor (ED), and

(iv) hydrogen,

said process comprising the step of polymerizing propylene and at least one comonomer in a single polymerization reactor, so as to produce the propylene polymer of claim 1 .

11. A process for the production of the propylene polymer of claim 1 in at least two sequential polymerization reactors in presence of

(i) a Ziegler-Natta polymerization catalyst, said Ziegler-Natta catalyst comprising a titanium compound, which has at least one titanium-halogen bond, and an internal donor, both supported on magnesium halide in active form,

(ii) an organo aluminium compound (Al),

(iii) an external electron donor (ED), and

(iv) hydrogen,

said process comprising the steps of

(a) polymerizing propylene or polymerizing propylene and at least one comonomer in a first polymerization reactor to produce a first propylene polymer fraction;

(b) transferring said first propylene polymer fraction to a second polymerization reactor; and

(c) polymerizing propylene or polymerizing propylene and at least one comonomer in said second polymerization reactor to produce a second propylene polymer fraction,

(f) recovering said propylene polymer after the last of the polymerization reactors;

wherein the hydrogen concentration in at least one of the sequential polymerization reactors is different from the hydrogen concentration in the remaining polymerization reactors, and wherein the hydrogen concentration in at least one of the polymerization reactors is controlled such as to produce therein the propylene polymer fraction with the lowest melt flow index as defined above, so as to produce the propylene polymer of claim 1 .