Process for preparing polypropylene composition

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

a) polymerizing in a first reactor monomers consisting of propylene and a comonomer selected from C 4 -C 10 alpha-olefins, to obtain a first propylene polymer fraction having a comonomer content in a range of from 2.0 to 8.0 mol %,

b) polymerizing in a second reactor monomers consisting of propylene, ethylene, and a comonomer selected from C 4 -C 10 alpha-olefins, in the presence of the first propylene polymer fraction, to obtain a second propylene polymer fraction, and

c) polymerizing in a third reactor monomers consisting of propylene, ethylene, and optionally one or more C 4 -C 10 alpha-olefins, in the presence of the second propylene polymer fraction, to obtain a polypropylene composition having an ethylene comonomer content in a range of from 0.5 to 5.0 mol % and a C 4 -C 10 alpha-olefin comonomer content in a range of from 3.0 to 10.0 mol %, relative to a total amount of monomers present in the polypropylene composition, and

wherein the process is operated in the presence of a Ziegler-Natta catalyst comprising a transition metal of group 4 to 6 of the periodic table, and an internal donor, optionally a co-catalyst and optionally an external donor, wherein the internal donor is a non-phthalic internal donor.

2. The process according to claim 1 , wherein the second propylene polymer fraction has an ethylene comonomer content in a range of from 0.5 to 5.0 mol % and a C 4 -C 10 alpha olefins comonomer content in a range of from 3.0 to 9.0 mol %, relative to the total amount of monomers present in the second propylene polymer fraction.

3. The process according to claim 1 , wherein polymerization in the first reactor is carried out at a temperature in a range of from 62 to 85° C.

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

5. The process according to claim 1 , wherein the polypropylene composition has an MFR 2 in a range of from 3 to 12 g/10 min, as measured at 230° C. under a load of 2.16 kg according to ISO 1133.

6. The process according to claim 1 , wherein the process is carried out in the absence of an anti-fouling agent.

7. A polypropylene composition obtained by the process of claim 1 , wherein the polypropylene composition has an ethylene comonomer content in a range of from 0.5 to 5.0 mol % and a C 4 -C 10 alpha olefins comonomer content in a range of from 3.0 to 10.0 mol %, relative to the total amount of monomers present in the polypropylene composition and, wherein the polypropylene composition has an MFR 2 in a range of from 3 to 12 g/10 min, as measured at 230° C. under a load of 2.16 kg according to ISO 1133, and wherein the polypropylene composition has a melting temperature in a range of from 135 to 160° C. and

wherein the polypropylene composition has trimodal comonomer composition with respect to the comonomer content of each of the propylene polymers comprised in said polypropylene composition.

8. The polypropylene composition according to claim 7 , wherein the polypropylene composition satisfies the equation:

Delta=Tm−SIT

wherein Delta is a temperature in a range of from 30 to 45° C.,

Tm is the melting temperature, in ° C., of the polypropylene composition,

SIT is the sealing initiation temperature, in ° C., of the polypropylene composition.

9. The polypropylene composition according to claim 7 , wherein the polypropylene composition has one or more comonomers selected from ethylene and 1-butene.

10. An article comprising the polypropylene composition according to claim 7 .

11. The article according to claim 10 , wherein said article is a film or a multilayer film.