Process for preparing polypropylene composition

Patent metadata

Field	Value
Publication number	US-12378330-B2
Application number	US-202217751995-A
Country	US
Kind code	B2
Filing date	May 24, 2022
Priority date	Dec 29, 2016
Publication date	Aug 5, 2025
Grant date	Aug 5, 2025

Abstract

The invention relates to a process for producing a polypropylene composition by sequential polymerization said polypropylene composition having low sealing initiation temperature (SIT) and high melting point (Tm), presenting thus a broad sealing window.

First claim

The invention claimed is:

1. An article comprising a polypropylene composition produced by a sequential polymerization process wherein the polypropylene composition is a binary blend comprising two propylene polymer fractions PPF1 and PPF2, wherein the propylene polymer fraction PPF1 is present in an amount of 30 to 50 wt % relative to the sum of the propylene polymer fractions PPF1 and PPF2 and is a propylene copolymer comprising 1.50 to 7.00 mol % of 1-butene (C 4 ) relative to the total amount of monomers in the propylene copolymer (PPF1) and the propylene polymer fraction PPF2 is present in an amount of 50 to 70 wt % relative to the sum of the propylene polymer fractions PPF1 and PPF2 and is a propylene terpolymer comprising 0.30 to 12.00 mol % of ethylene comonomer and 1.50 to 17.00 mol % of 1-butene (C 4 ), the amount of ethylene and 1-butene (C 4 ) comonomers relative to the total amount of monomers in the propylene terpolymer (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 1-butene (C 4 ) to obtain the 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 1-butene (C 4 ) in the presence of the propylene polymer fraction (PPF1) to obtain 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 1-butene (C 4 ) content in the propylene copolymer fraction PPF1 (C 4 -PPF1)/1-butene (C 4 ) content in the polypropylene composition, (C 4 -T), [(C 4 -PPF1)/(C 4 -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 143 to 160° C. as determined by DSC according to ISO 11357, a xylene soluble fraction (XS) determined at 25° C. according to ISO 16152, 5 th edition, 2005 Jul. 1 in the range of 4 to 30 wt %, and a melt flow rate (MFR2) determined according to ISO 1133 at a temperature of 230° C. under a load of 2.16 kg in the range of 3 to 20.0 g/10 min,
wherein the polymerization process is carried out in the presence of a Ziegler-Natta catalyst that is free of phthalic compound, a co-catalyst being triethylaluminum (TEAL), and an external donor being dicyclo pentyl dimethoxy silane, wherein the Ziegler-Natta catalyst comprises a transition metal of Group 4 to 6 (TM) and a non-phthalic internal donor (ID) being bis(2-ethylhexyl) citraconate, and
wherein the polypropylene composition satisfies the equation
Delta= Tm −SIT

wherein Delta is in the range of 41 to 50° C., and wherein
Tm is the melting temperature of the polypropylene composition, and
SIT is the sealing initiation temperature, in ° C., of the polypropylene composition.

2. A film comprising a polypropylene composition produced by a sequential polymerization process wherein the polypropylene composition is a binary blend comprising two propylene polymer fractions PPF1 and PPF2, wherein the propylene polymer fraction PPF1 is present in an amount of 30 to 50 wt % relative to the sum of the propylene polymer fractions PPF1 and PPF2 and is a propylene copolymer comprising 1.50 to 7.00 mol % of 1-butene (C 4 ) relative to the total amount of monomers in the propylene copolymer (PPF1) and the propylene polymer fraction PPF2 is present in an amount of 50 to 70 wt % relative to the sum of the propylene polymer fractions PPF1 and PPF2 and is a propylene terpolymer comprising 0.30 to 12.00 mol % of ethylene comonomer and 1.50 to 17.00 mol % of 1-butene (C 4 ), the amount of ethylene and 1-butene (C 4 ) comonomers relative to the total amount of monomers in the propylene terpolymer (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 1-butene (C 4 ) to obtain the 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 1-butene (C 4 ) in the presence of the propylene polymer fraction (PPF1) to obtain 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 1-butene (C 4 ) content in the propylene copolymer fraction PPF1 (C 4 -PPF1)/1-butene (C 4 ) content in the polypropylene composition, (C 4 -T), [(C 4 -PPF1)/(C 4 -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 143 to 160° C. as determined by DSC according to ISO 11357, a xylene soluble fraction (XS) determined at 25° C. according to ISO 16152, 5 th edition, 2005 Jul. 1 in the range of 4 to 30 wt %, and a melt flow rate (MFR2) determined according to ISO 1133 at a temperature of 230° C. under a load of 2.16 kg in the range of 3 to 20.0 g/10 min,
wherein the polymerization process is carried out in the presence of a Ziegler-Natta catalyst that is free of phthalic compound, a co-catalyst (Co) being triethylaluminum (TEAL), and an external donor being dicyclo pentyl dimethoxy silane, wherein the Ziegler-Natta catalyst comprises a transition metal of Group 4 to 6 (TM) and a non-phthalic internal donor (ID) being bis(2-ethylhexyl) citraconate, and
wherein the polypropylene composition satisfies the equation
Delta= Tm −SIT

wherein Delta is in the range of 41 to 50° C., and wherein
Tm is the melting temperature of the polypropylene composition, and
SIT is the sealing initiation temperature, in ° C., of the polypropylene composition.

3. The film according to claim 2 wherein said film is a blown film or a cast film.

4. The film according to claim 2 , wherein said film is a multilayer film.

Assignees

• Borealis Ag

Inventors

• Leskinen Pauli
• Boragno Luca

Classifications

• C08J2323/14

  Copolymers of propene (C08J2323/16 takes precedence) · CPC title

• C08J5/18

  Manufacture of films or sheets · CPC title

• C08F2500/26

  Use as polymer for film forming · CPC title

• C08F2500/12

  Melt flow index or melt flow ratio · CPC title

• C08F210/16

  Copolymers of ethene with alpha-alkenes, e.g. EP rubbers · CPC title