Polypropylene with extreme broad molecular weight distribution

1. Polypropylene having:

(a) a melt flow rate MFR 2 (230° C.) measured according to ISO 1133 of at least 20 g/10min; and

(b) a complex viscosity ratio eta*(0.05 rad/sec)/eta*(300 rad/sec) of at least 20.0 measured by dynamic rheology according to ISO 6271-10 at 200° C.;

wherein said polypropylene has a first polypropylene fraction (PP1), a second polypropylene fraction (PP2), and a third polypropylene fraction (PP3), said first polypropylene fraction(PP1) , second polypropylene fraction (PP2), and third polyproplene fraction (PP3)differ in the melt flow rate MFR 2 (230° C. by at least 30 g/10min.

2. Polypropylene according to claim 1 , wherein said polypropylene has:

a ratio of weight average molecular weight (Mw) to number average molecular weight (Mn) [Mw/Mn] of at least 15.0 determined by Gel Permeation Chromatography (GPC).

3. Polypropylene according to claim 1 , wherein said polypropylene has

(a) a xylene cold soluble content (XCS) determined according ISO 16152 (25° C.) of at least 2.8 wt. %; and/or

(b) a melting temperature Tm of more than 161° C.

4. Polypropylene according to claim 1 , wherein said polypropylene has:

(a) 2,1 erythro regio-defects of equal or below 0.4 mol.-% determined by 13 C-NMR spectroscopy; and/or

(b) a pentad isotacticity (mmmm) of more than 95.0 mol. %.

5. Polypropylene according to claim 1 , wherein said polypropylene has:

(a) a ratio of z-average molecular weight (Mz) to weight average molecular weight (Mw) [Mz/Mw] of at least 9.0; and/or

(b) a ratio of z-average molecular weight (Mz) to number average molecular weight (Mn) [Mz/Mn] of at least 150.

6. Polypropylene according to claim 1 , wherein said polypropylene is α-nucleated.

7. Polypropylene according to claim 1 , wherein said polypropylene has:

(a) a weight ratio of the crystalline fractions melting in the temperature range of above 160 to 180° C. to the crystalline fractions melting in the temperature range of 90 to 160 of at least 3.20, wherein said fractions are determined by the stepwise isothermal segregation technique (SIST); and/or

(b) a crystallization temperature of at least 125° C.; and/or

(c) a tensile modulus measured according to ISO 527-2 of at least 2250 MPa.

8. Polypropylene according to claim 1 , wherein said polypropylene has a first polypropylene fraction (PP1), a second polypropylene fraction (PP2) and a third polypropylene fraction (PP3), and the amount:

(a) of the first polypropylene fraction (PP1) is in the range of 40 to 60 wt. %,

(b) of the second polypropylene fraction (PP2) is in the range of 20 to 59.0 wt. %, and

(c) of the third polypropylene fraction (PP3) is in the range of 1.0 to 15.0 wt. %,

based on the total amount of the polypropylene.

9. Polypropylene according to claim 1 , wherein:

(a) the melt flow rate MFR 2 (230° C.) of the first polypropylene fraction (PP1) is at least 5 times higher than the melt flow rate MFR 2 (230° C.) of the second polypropylene fraction (PP2); and/or

(b) the melt flow rate MFR 2 (230° C.) of the second polypropylene fraction (PP2) is at least 5,000 times higher than the melt flow rate MFR 2 (230° C.) of the third polypropylene fraction (PP3).

10. Polypropylene according to claim 1 , wherein:

(a) the melt flow rate MFR 2 (230° C.) of the first polypropylene fraction (PP1) is at least 200 g/10min; and/or

(b) the melt flow rate MFR 2 (230° C.) of the second polypropylene fraction (PP2) is in the range of 10 to below 200 g/10min; and/or

(c) the melt flow rate MFR 2 (230° C.) of the third polypropylene fraction (PP3) is below 0.1 g/10min.

11. Process for the manufacture of the polypropylene according to claim 1 , in a sequential polymerization system comprising a pre-polymerization reactor (PR) and at least three polymerization reactors (R1), (R2) and (R3) connected in series, feeding propylene (C3) and optionally hydrogen (H2) to said pre-polymerization reactor (PR) in a H2/C3 feed ratio of 0.00 to 0.10 mol/kmol to form a pre-polypropylene (Pre-PP) and polymerizing the pre-polypropylene (Pre-PP) in the at least three polymerization reactors (R1), (R2), and (R3), wherein the polymerization in the at least three polymerization reactors (R1), (R2) and (R3) takes place in the presence of a Ziegler-Natta catalyst (ZN-C), said Ziegler-Natta catalyst (ZN-C) comprises

(a) a pro-catalyst (PC) comprising a titanium compound (TC) having at least one titanium-halogen bond and an internal donor (ID), both supported on a magnesium halide;

(b) a co-catalyst (Co); and

(c) an external donor (ED);

wherein:

the internal donor (ID) comprises at least 80 wt.-% of a compound selected from the group consisting of succinate, citraconate, di-ketone, enaminoimine, and mixtures thereof;

the mol-ratio of co-catalyst (Co) to external donor (ED) [Co/ED] of said Ziegler-Natta catalyst (ZN-C) is below 20.0; and

said Ziegler-Natta catalyst (ZN-C) is present in the pre-polymerization reactor (PR).

12. Process according to claim 11 , wherein:

(a) the mol-ratio of co-catalyst (Co) to titanium compound (TC) (TC) [Co/TC] is at most 130; and/or

(b) the mol-ratio of external donor (ED) to titanium compound (TC)) [Co/TC] is below 50.

13. Process according to claim 11 , wherein:

(a) the operating temperature in the pre-polymerization reactor (PR) is in the range of more than 20° C. to 80° C.; and/or

(b) the average residance time of the Ziegler-Natta catalyst (ZN-C) in the pre-polymerization reactor (PR) is in the range of more than 3 to 20 min.

14. Process according to claim 11 , wherein:

(a) the average residence time in the first polymerization reactor (R1) is at least 20 min; and/or

(b) the average residence time in the second polymerization reactor (R2) is at least 30 min; and/or

(c) the average residence time in the third polymerization reactor (R3) is at least 80 min; and/or

(d) the total residence time in the three polymerization reactors (R1), (R2), and (R3) together is at most 700 min.

15. Process according to claim 11 , wherein:

(a) the feed ratio of hydrogen (H 2 ) to propylene (C 3 ) [H 2 /C 3 ] in the first polymerization reactor (R1) is in the range of 10 to 60 mol/kmol; and/or

(b) the feed ratio of hydrogen (H 2 ) to propylene (C 3 ) [H 2 /C 3 ] in the second polymerization reactor (R2) is in the range of 10 to 260 mol/kmol; and/or

(c) the feed ratio of hydrogen (H 2 ) to propylene (C 3 ) [H 2 /C 3 ] in the third polymerization reactor (R3) is in the range of 0 to 20 mol/kmol.

16. Polypropylene according to claim 1 , wherein said polypropylene has a polydispersity index (PI) of at least 10.0.