Process for preparing polypropylene composition

1. Process for producing a polypropylene composition by a sequential polymerization process wherein the polypropylene composition is a binary blend comprising two propylene polymer fractions PPF1 and PPF2 and wherein the process comprises at least two reactors connected in series, said process comprising the steps:

a) polymerizing in a first reactor (R-1), propylene and one comonomer selected from C 4 -C 10 alpha-olefin to obtain a propylene polymer fraction (PPF1), the first reactor (R-1) being a slurry reactor and the propylene polymer fraction (PPF1) being a propylene copolymer,

b) transferring the propylene polymer fraction (PPF1) and unreacted comonomers of the reactor (R-1) into a second reactor (R-2), the second reactor (R-2) being a first gas-phase reactor-1 (GPR-1),

c) polymerizing in the gas-phase reactor-1 (GPR-1) propylene, ethylene and one comonomer selected from C 4 -C 10 alpha-olefin in the presence of the propylene polymer fraction (PPF1), to obtain a propylene polymer fraction (PPF2), the propylene polymer fraction (PPF2) being a polypropylene terpolymer,

d) forming the polypropylene composition from the propylene polymer fraction (PPF2) and the propylene polymer fraction (PPF1), and

e) recovering the polypropylene composition wherein the mol ratio of C 4 -C 10 alpha-olefin content in the propylene copolymer fraction PPF1 (C 4 -C 10 -PPF1)/C 4 -C 10 alpha-olefin content in the polypropylene composition (C 4 -C 10 -T) [(C 4 -C 10 -PPF1) /(C 4 -C 10 -T)] is in the range of 0.10 to 0.95,

and wherein the polypropylene composition has a melting temperature (Tm) in the range of 135 to 160° C. as determined by DSC according to ISO 11357,

wherein the polymerization process is carried out in the presence of a Ziegler-Natta catalyst that is free of phthalic compound, wherein the Ziegler-Natta catalyst comprises a transition metal of Group 4 to 6 (TM) and a non-phthalic internal donor (ID).

2. The process according to claim 1 , wherein:

a) the propylene copolymer fraction (PPF1) obtained in the first reactor (R-1) is produced in an amount of less than or equal to 50 wt %,

b) the propylene terpolymer fraction (PPF2) obtained in the second reactor (R-2) is produced in an amount of more than or equal to 50 wt %,

the amount of PPF1 and PPF2 being relative to the total sum of the propylene polymer fractions PPF1 and PPF2.

3. The process according to claim 1 , wherein:

a) the propylene polymer fraction PPF1 comprises 1.50 to 7.00 mol % of one comonomer selected from C 4 -C 10 alpha-olefin, the amount of C 4 -C 10 alpha-olefin comonomer relative to the total amount of monomers in the propylene copolymer (PPF1), and

b) the propylene polymer fraction PPF2 comprises 0.30 to 12.00 mol % of ethylene comonomer and 1.50 to 17.00 mol % of one comonomer selected from C 4 -C 10 alpha-olefin, the amount of ethylene and C 4 -C 10 alpha-olefin comonomers relative to the total amount of monomers in the propylene terpolymer (PPF2).

4. The process according to claim 1 , wherein the operating temperature in the first reactor (R-1) is in the range of 62 to 85° C.

5. The process according to claim 1 , wherein the following components are present in said process:

a co-catalyst (Co), and

optionally an external donor (ED)

and wherein if present, the co-catalyst (Co) to external donor (ED) molar ratio [Co/ED] is in the range of 2.5 to 50.0 mol/mol and wherein the co-catalyst (Co) to transition metal of Group 4 to 6 (TM) molar ratio [Co/TM] is in the range of 20.0 to 500.0 mol/mol.

6. The process according to claim 1 , wherein the non-phthalic internal donor (ID) 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, benzoates, derivatives of any of them, and mixtures of any of the preceding compounds.

7. The process according to claim 1 , wherein the propylene polymer fraction PPF1 is a propylene copolymer comprising 1-butene (C 4 ) and the propylene polymer fraction PPF2 is a propylene terpolymer comprising ethylene comonomer and 1-butene (C 4 ).

8. The process according to claim 1 , wherein the polypropylene composition satisfies the equation:

Delta=Tm −SIT

wherein Delta is in the range of 30 to 50° C., and wherein

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

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

9. The process according to claim 1 , wherein the polypropylene composition has an MFR 2 in the range of 1.0 to 50.0 g/10 min, as measured at 230° C. under a load of 2.16 kg according to ISO 1133.

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