Process for preparing a polypropylene composition

1. A process for producing a polypropylene composition by sequential polymerization comprising the steps:

a) polymerizing in a first reactor monomers comprising propylene and optionally one or more comonomers selected from ethylene and C 4 -C 10 alpha-olefins, to obtain a first propylene polymer fraction having a comonomer content in the range of 0.0 to 1.0 wt %;

b) polymerizing in a second reactor monomers comprising propylene and one or more comonomers selected from ethylene and C 4 -C 10 alpha-olefins, in the presence of the first propylene polymer fraction, to obtain a second propylene polymer fraction having a comonomer content in the range of 0.3 to 2.0 wt %;

c) polymerizing in a third reactor monomers comprising propylene and one or more comonomers selected from ethylene and C 4 -C 10 alpha-olefins, wherein the ratio of the one or more comonomers to propylene is in the range of 45.0 to 170.0 mol/kmol, in the presence of the second propylene polymer fraction to obtain a third propylene polymer fraction having a comonomer content in the range of from 1.5 to 5.0 wt %; and

d) extruding the third propylene polymer fraction in the presence of at least one alpha-nucleating agent;

wherein the polypropylene composition has an MFR 2 in the range of from 12.0 to 60.0 g/10 min, as measured according to ISO 1133 at 230° C. under a load of 2.16 kg.

2. The process according to claim 1 , wherein the polymerization in steps a), b), and c) is carried out in the presence of a Ziegler-Natta catalyst.

3. The process according to claim 2 , wherein the Ziegler-Natta catalyst is free of a phthalic compound.

4. The process according to claim 1 , wherein the process is operated in the presence of a Ziegler-Natta catalyst with a transition metal of group 4 to 6 of the periodic table, the catalyst comprising an internal donor, wherein the internal donor is a non-phthalic internal donor.

5. The process according to claim 4 , wherein the non-phthalic internal donor is selected from (di)esters of non-phthalic carboxylic (di)acids, wherein the (di)ester belongs to the group consisting of malonates, maleates, succinates, citraconates, glutarates, cyclohexene-1,2-dicarboxylates, benzoates, derivatives thereof, and mixtures thereof.

6. The process according to claim 4 , wherein the catalyst further comprises a co-catalyst, an external donor, or a combination thereof.

7. The process according to claim 1 , wherein the comonomers in step a), step b), step c), or a combination thereof are selected from one or more comonomers comprising ethylene.

8. The process according to claim 1 , wherein:

a) the hydrogen/propylene (H 2 /C 3 ) ratio in the first reactor is in the range of 1.5 to 6.0 mol/kmol;

b) the hydrogen/propylene (H 2 /C 3 ) ratio in the second reactor is in the range of 12.0 to 70.0 mol/kmol; and

c) the hydrogen/propylene (H 2 /C 3 ) ratio in the third reactor is in the range of 15.0 to 80.0 mol/kmol.

9. The process according to claim 1 , wherein the third propylene polymer fraction is extruded in the presence of an amount of the at least one alpha-nucleating agent in the range of from 0.01 to 1.0 wt %, relative to the total amount of polypropylene composition.

10. The process according to claim 1 , wherein the polypropylene composition has a haze value <20%, as measured according to ASTM D1003 on injection molded plaques having 1 mm thickness produced as described in EN ISO 1873-2.

11. The process according to claim 1 , wherein the first reactor comprises a slurry reactor.

12. The process according to claim 1 , wherein the second reactor comprises a gas phase reactor.

13. The process according to claim 1 , wherein the third reactor comprises a gas phase reactor.