Soft heterophasic random propylene copolymer with improved clarity

1. A heterophasic propylene copolymer (RAHECO) having

(a) a xylene cold soluble content (XCS) determined according ISO 16152 (25° C.) in the range of 25.0 to 35.0 wt.-%, and

(b) a comonomer content in the range of more than 4.5 to 10.0 wt.-%,

wherein further

(c) the comonomer content of xylene cold soluble (XCS) fraction of the propylene copolymer is in the range of 12.0 to 22.0 wt.-%,

(d) the intrinsic viscosity (IV) determined according to DIN ISO 1628/1 (in decalin at 135° C.) of the xylene cold soluble (XCS) fraction of the propylene copolymer is in the range of more than 1.5 to below 3.0 dl/g, and

(e) the relative content of isolated to block ethylene sequences (I(E)) of the XCS fraction fulfilling the inequation (I)

I ( E )<78 1.97× C 2+0.015×( C 2) 2   (I)

wherein C2 is the comonomer content [wt %] of the XCS fraction and

wherein the I(E) content is defined by equation (II)

I ( E )= f PEP/(( f EEE+ f PEE+ f PEP))×100  (II)

wherein

I(E) is the relative content of isolated to block ethylene sequences [in %];

fPEP is the mol fraction of propylene/ethylene/propylene sequences (PEP) in the sample;

fPEE is the mol fraction of propylene/ethylene/ethylene sequences (PEE) and of ethylene/ethylene/propylene sequences (EEP) in the sample;

fEEE is the mol fraction of ethylene/ethylene/ethylene sequences (EEE) in the sample wherein all sequence concentrations are based on a statistical triad analysis of 13C-NMR data.

2. The heterophasic propylene copolymer (RAHECO) according to claim 1 , wherein the xylene cold insoluble (XCI) fraction of the propylene copolymer has one or more of:

(a) a polydispersity (Mw/Mn) of more than 4.9 to 10.0,

or

(b) a comonomer content in the range of 3.0 to 7.0.

3. The heterophasic propylene copolymer (RAHECO) according to claim 1 , wherein the total melt flow rate MFR 2 (230° C.) of the heterophasic propylene copolymer (RAHECO) measured according to ISO 1133 is in the range of more than 0.8 to below 2.5 g/10 min.

4. The heterophasic propylene copolymer (RAHECO) according to claim 1 , wherein the heterophasic propylene copolymer (RAHECO) comprises one or more of:

(a) an α-nucleating agent,

or

(b) a hexane soluble content of below 5.5 wt.-%.

5. The heterophasic propylene copolymer (RAHECO) according to claim 1 , wherein the heterophasic propylene copolymer (RAHECO) has a melting temperature Tm determined by differential scanning calorimetry (DSC) of not lower than 140° C.

6. The heterophasic propylene copolymer (RAHECO) according to claim 1 , wherein the heterophasic propylene copolymer (RAHECO) comprises a matrix (M) and an elastomeric propylene copolymer (E) dispersed in said matrix (M), wherein

(a) said matrix (M) is a random propylene copolymer (R-PP), and

(b) the weight ratio between the matrix (M) and the elastomeric propylene copolymer (E) is 60/40 to 95/5.

7. The heterophasic propylene copolymer (RAHECO) according to claim 6 , wherein the random propylene copolymer (R-PP) comprises one or more of:

(a) a comonomer content in the range of 1.5 to 7.0 wt.-%,

or

(b) fulfills inequation (III)

Co (total)/ Co ( RPP )≥1.3  (III)

wherein

Co (total) is the comonomer content [wt.-%] of the heterophasic propylene copolymer (RAHECO),

Co (RPP) is the comonomer content [wt.-%] of the random propylene copolymer (R-PP),

or

(c) has a xylene cold soluble (XCS) fraction in the range of 8.0 to below 20.0 wt.-%.

8. The heterophasic propylene copolymer (RAHECO) according to claim 6 , wherein the elastomeric propylene copolymer (E) has a comonomer content of not higher than 30.0 wt.-%.

9. The heterophasic propylene copolymer (RAHECO) according to claim 1 , wherein an extrusion blow molded bottle with wall thickness of 0.3 mm comprising the said heterophasic propylene copolymer (RAHECO) has a clarity determined according to ASTM D1003 of higher than 70.0%.

10. A polymerization process for producing a heterophasic propylene copolymer (RAHECO), comprising the steps of

(a) polymerizing in a first reactor (R1) propylene and one or more of ethylene or a C4 to C12 α-olefin,

obtaining a first random propylene copolymer fraction (R-PP1),

(b) transferring the first random propylene copolymer fraction (R-PP1), into a second reactor (R2),

(c) polymerizing in said second reactor (R2) in the presence of the first random propylene copolymer fraction (R-PP1),

propylene and one or more of ethylene or a C4 to C12 α-olefin,

obtaining a second random propylene copolymer fraction (R-PP2), the first and second polymer fraction form the random propylene copolymer (R-PP),

(d) transferring said random propylene copolymer (R-PP), into a third reactor (R3),

(e) polymerizing in said third reactor (R3) in the presence of the random propylene copolymer (R-PP),

propylene and one or more of ethylene or a C4 to C12 α-olefin,

obtaining a third polymer fraction, said third polymer fraction is the elastomeric propylene copolymer (E); the third polymer fraction and the random propylene copolymer (R-PP) form the heterophasic propylene copolymer (RAHECO), and

(f) removing the propylene copolymer from the third reactor (R3),

wherein the heterophasic propylene copolymer (RAHECO) comprises:

(a) a xylene cold soluble content (XCS) determined according ISO 16152 (25° C.) in the range of 25.0 to 35.0 wt.-%, and

(b) a comonomer content in the range of more than 4.5 to 10.0 wt.-%,

wherein further

(c) the comonomer content of xylene cold soluble (XCS) fraction of the propylene copolymer is in the range of 12.0 to 22.0 wt.-%,

(d) the intrinsic viscosity (IV) determined according to DIN ISO 1628/1 (in decalin at 135° C.) of the xylene cold soluble (XCS) fraction of the propylene copolymer is in the range of more than 1.5 to below 3.0 dl/g, and

(e) the relative content of isolated to block ethylene sequences (I(E)) of the XCS fraction fulfilling the inequation (I)

I ( E )<78−1.97× C 2+0.015×( C 2) 2   (I)

wherein C2 is the comonomer content [wt %] of the XCS fraction and

wherein the I(E) content is defined by equation (II)

I ( E )= f PEP/(( f EEE+ f PEE+ f PEP))×100  (II)

wherein

I(E) is the relative content of isolated to block ethylene sequences [in %];

fPEP is the mol fraction of propylene/ethylene/propylene sequences (PEP) in the sample;

fPEE is the mol fraction of propylene/ethylene/ethylene sequences (PEE) and of ethylene/ethylene/propylene sequences (EEP) in the sample;

fEEE is the mol fraction of ethylene/ethylene/ethylene sequences (EEE) in the sample wherein all sequence concentrations are based on a statistical triad analysis of 13C-NMR data.

11. The polymerization process according to claim 10 , wherein steps a), c), and e) of claim 10 are carried out in the presence of

a) a Ziegler-Natta catalyst (ZN-C) comprising compounds (TC) of a transition metal of Group 4 to 6 of IUPAC, a Group 2 metal compound (MC) and an internal donor (ID), wherein said internal donor (ID) is a non-phthalic compound,

b) a co-catalyst (Co), and

c) optionally an external donor (ED).

12. The polymerization process according to claim 11 , wherein the internal donor (ID) is selected from the group consisting of malonates, maleates, succinates, glutarates, cyclohexene-1,2-dicarboxylates, benzoates, derivatives and mixtures thereof.

13. A molded article comprising a heterophasic propylene copolymer (RAHECO), wherein the heterophasic propylene copolymer (RAHECO) comprises:

(a) a xylene cold soluble content (XCS) determined according ISO 16152 (25° C.) in the range of 25.0 to 35.0 wt.-%, and

(b) a comonomer content in the range of more than 4.5 to 10.0 wt.-%,

wherein further

(c) the comonomer content of xylene cold soluble (XCS) fraction of the propylene copolymer is in the range of 12.0 to 22.0 wt.-%,

(d) the intrinsic viscosity (IV) determined according to DIN ISO 1628/1 (in decalin at 135° C.) of the xylene cold soluble (XCS) fraction of the propylene copolymer is in the range of more than 1.5 to below 3.0 dl/g, and

(e) the relative content of isolated to block ethylene sequences (I(E)) of the XCS fraction fulfilling the inequation (I)

I ( E )<78−1.97× C 2+0.015×( C 2) 2   (I)

wherein C2 is the comonomer content [wt %] of the XCS fraction and

wherein the I(E) content is defined by equation (II)

I ( E )= f PEP/(( f EEE+ f PEE+ f PEP))×100  (II)

wherein

I(E) is the relative content of isolated to block ethylene sequences [in %];

fPEP is the mol fraction of propylene/ethylene/propylene sequences (PEP) in the sample;

fPEE is the mol fraction of propylene/ethylene/ethylene sequences (PEE) and of ethylene/ethylene/propylene sequences (EEP) in the sample;

fEEE is the mol fraction of ethylene/ethylene/ethylene sequences (EEE) in the sample wherein all sequence concentrations are based on a statistical triad analysis of 13C-NMR data.

14. The molded article according to claim 13 , wherein the article is a bottle.

15. The polymerization process according to claim 11 , wherein the non-phthalic compound comprises a non-phthalic acid ester.

16. The polymerization process according to claim 12 , wherein the internal donor (ID) is a citraconate.

17. The molded article according to claim 13 , wherein the molded article is an extrusion blow molded article.

18. The molded article according to claim 14 , wherein the molded article is an extrusion blow molded article.

19. The polymerization process according to claim 15 , wherein the internal donor (ID) is selected from the group consisting of malonates, maleates, succinates, glutarates, cyclohexene-1,2-dicarboxylates, benzoates, derivatives and mixtures thereof.

20. The polymerization process according to claim 19 , wherein the internal donor (ID) is a citraconate.