Granted Patent B2

US 12,577,372 · App. 18/231,814 · Granted Mar 17, 2026

Inventors: Andreas Fuchs (Linz, AT); Luca Boragno (Linz, AT); Girish Suresh Galgali (Linz, AT); Markus Gahleitner (Linz, AT); Jurgen Huber (Linz, AT); Stefanie Engleder (Linz, AT)

Assignee: BOREALIS AG

C08K5/20C08K3/34C08K3/40C08L23/12C08L2205/025

Abstract

Claims (50)

1 . A process for providing a polypropylene composition comprising:

semi-volatile organic condensable oligomers FOG in an amount of 50 μg/g to 400 μg/g of the total polypropylene composition determined according to VDA 278 October 2011, and

volatile organic compounds VOC in an amount of less than 80 μg/g of the total polypropylene composition determined according to VDA 278 October 2011,

wherein the weight ratio of said semi-volatile organic condensable oligomers versus said volatile organic compounds is more than 5.0,

wherein the polypropylene composition has an MFR 2 of 10 g/10 min or higher determined according to ISO 1133 at 230° C. and a load of 2.16 kg,

wherein the polypropylene composition has a flexural modulus, determined according to ISO 178 on injection molded specimens of 80×10×4 mm prepared in accordance with ISO 294-1:1996, of from 1000 to 6000 MPa, and

wherein the total quantity of slip agent is at least 500 ppm,

the process comprising:

blending

polypropylene,

filler,

slip agent,

optional HDPE,

optional plastomer, and

optional pigment in the presence of additives providing to obtain a blend,

and further subjecting the blend to a process comprising the steps of:

a) providing an aeration vessel having,

at least one inlet for aeration gas,

at least one outlet for exhaust gas,

an inlet for a raw polypropylene composition at the top of the aeration vessel,

an outlet for the polypropylene composition at the bottom of the aeration vessel,

wherein the polypropylene composition is present as a packed bed;

b) initiating a counter-current flow of the polypropylene composition and aeration gas,

c) by

feeding the raw polypropylene composition having

a volatile organic compound content VOC of greater than 150 μg/g determined according to VDA 278 October 2011; and

a semi-volatile organic condensable content FOG of greater than 350 μg/g determined according to VDA 278 October 2011, into said aeration vessel from the top,

feeding the aeration gas into said aeration vessel via the at least one inlet at the bottom;

withdrawing the exhaust gas via the outlet for exhaust gas;

withdrawing the aerated polypropylene composition via the outlet at the bottom of the aeration vessel,

d) maintaining said aeration gas flow for an aeration time of from 3 to 96 hours,

wherein the temperature of the gas is from 100° C. to 140° C., and wherein, the Reynolds number of the gas flow is from 5 to 150, whereby the Reynolds number for the flow of aeration gas through the packed bed is defined by formula (I)

Re=(ρ v s D )/μ  (I)

where:

ρ is the density of the aeration gas at the temperature used in kg/m 3 ,

μ is the kinematic viscosity of the aeration gas at the temperature used in kg/m s,

v s is the superficial velocity, defined as Q/A where Q is the volume flow rate of the aeration gas in m 3 /s and A is the cross sectional area in m 2 ,

D is the diameter in m of the particles; and

wherein no further slip agent is added to the composition after step d), the aeration step.

2 . The process according to claim 1 , wherein the slip agent is a fatty acid amide.

3 . The process according to claim 2 , wherein the fatty acid amide is erucamide or oleamide.

4 . The process according to claim 1 , wherein the odor rating according to VDA 277 is less than 1.

5 . The process according to claim 1 , wherein the fogging gravimetric is less than 1.1,

and/or wherein the total emissions according to VDA 270 are 3 μg carbon per g sample or less.

6 . The process according to claim 1 , wherein the polypropylene composition has an MFR 2 of from 10 to 25 g/10 min determined according to ISO 1133 at 230° C. and a load of 2.16 kg.

7 . The process according to claim 1 , wherein the polypropylene composition has a flexural modulus, determined according to ISO 178 on injection molded specimens of 80×10×4 mm prepared in accordance with ISO 294-1:1996, of from 1300 to 5000 MPa.

8 . The process according to claim 1 , wherein the blending step involves blending a heterophasic polypropylene with a further polypropylene homo- and/or copolymer.

9 . The process according to claim 1 , wherein the polypropylene composition has a flexural modulus, determined according to ISO 178 on injection molded specimens of 80×10×4 mm prepared in accordance with ISO 294-1:1996, of from 1200 to 5500 MPa.

10 . The process according to claim 1 , wherein the polypropylene composition has a puncture energy of from 20 to 60 J.

11 . The process according to claim 1 , wherein the filler is selected from the group consisting of talc, glass, and mixtures thereof.

Priority Claims (1)

Continuity (2)

References Cited (37)