Decoloration of polyolefins in the melt state

Patent metadata

Field	Value
Publication number	US-12540201-B2
Application number	US-202217942620-A
Country	US
Kind code	B2
Filing date	Sep 12, 2022
Priority date	Sep 23, 2021
Publication date	Feb 3, 2026
Grant date	Feb 3, 2026

Abstract

The present invention concerns a process for decolorizing a polyolefin composition, the process comprising the steps of a) providing a polyolefin composition comprising at least one polyolefin and at least one organic chromophore, b) mixing the polyolefin composition in a melt state at a temperature of 170 to 290° C. with an inorganic oxidizing agent, wherein the inorganic oxidizing agent is selected from the group of inorganic peroxides and hypochlorites, and c) obtaining a decolorized polyolefin composition.

First claim

The invention claimed is:

1 . A process for decolorizing a polyolefin composition, the process comprising the steps of
a) providing a polyolefin composition comprising at least one polyolefin and at least one organic chromophore, b) mixing the polyolefin composition in a melt state at a temperature of 170 to 290° C. with an inorganic oxidizing agent, wherein the inorganic oxidizing agent is selected from the group of hypochlorites, and c) obtaining a decolorized polyolefin composition.

2 . The process according to claim 1 , wherein the polyolefin has a density of 860 to 960 kg/m 3 measured according to ISO 1183 and/or a melting temperature Tm measured according to ISO 11357-3 of 60 to 170° C.

3 . The process according to claim 1 , wherein the polyolefin is selected from the group of ethylene homo- or copolymers having a density of 860 to 960 kg/m 3 , propylene homo- or copolymers having a density of 900 to 910 kg/m 3 , or mixtures thereof.

4 . The process according to claim 3 , wherein the ethylene homo- or copolymer is a HDPE having a density of 940 to 960 kg/m 3 , an LDPE having a density of 900 to less than 940 kg/m 3 , an LLDPE having a density of 900 to less than 940 kg/m 3 , a plastomer having a density of 860 to 890 kg/m 3 , or mixtures thereof.

5 . The process according to claim 3 , wherein the propylene homo- or copolymer is a propylene homopolymer, a random copolymer with ethylene and/or C4 to C10 alpha-olefins, heterophasic copolymer with ethylene and/or C4 to C10 alpha-olefins, random-heterophasic copolymer with ethylene and/or C4 to C10 alpha-olefins, or mixtures thereof.

6 . The process according to claim 1 , wherein the organic chromophore comprises one or more azo groups or wherein the organic chromophore comprises a substituted isoindoline group.

7 . The process according to claim 1 , wherein the organic chromophore comprises disodium 6-hydroxy-5-[(2-methoxy-5-methyl-4-sulfonatophenyl)diazenyl] naphthalene-2-sulfonate, trisodium (4E)-3-oxo-4-[(4-sulfonato-1-naphthyl)hydrazono]naphthalene-2,7-disulfonate, 4-[[2-methoxy-5-[(phenylamino)carbonyl]phenyl]azo]-; n-(2,3-dihydro-2-oxo-1h-benzimidazol-5-yl)-3-hydroxy-2-naphthalenecarboxamide, 4-[(2.5-dichlorophenyl)diazenyl]-N-[4-[[4-[(2.5-dichlorophenyl)diazenyl]-3-hydroxynaphthalene-2-carbonyl]amino]phenyl]-3-hydroxynaphthalene-2-carboxamide, trisodium 5-hydroxy-1-(4-sulfonatophenyl)-4-[(E)-(4-sulfonatophenyl)diazenyl]-1H-pyrazole-3-carboxylate, 5,5′-(1H-isoindole-1,3(2H)-diylidene)dibarbituric acid and mixtures thereof.

8 . The process according to claim 1 , wherein the organic chromophore is present in an amount of 1 to 100000 ppm by weight, preferably to 50000 ppm by weight, more preferably 10 to 25000 ppm by weight, based on the total polyolefin composition of step a).

9 . The process according to claim 1 , wherein the hypochlorite comprises Ca(OCl) 2 , NaOCl, KClO, LiClO or mixtures thereof.

10 . The process according to claim 1 , wherein the inorganic oxidizing agent in step b) is added in an amount of 0.1 to 10 wt.-% with respect to the total polyolefin composition of step a).

11 . The process according to claim 1 , wherein the ΔE measured according to ISO 11664-4 of the decolorized polyolefin composition is between 6.0 and 120.0.

12 . The process according to claim 1 , wherein the polyolefin composition of step a) has a first MFR2 measured according to ISO 1133 and the decolorized polyolefin composition obtained in step c) has a second MFR2 measured according to ISO 1133, wherein the second MFR2 is
1.5·(first MFR2)≥(second MFR2)≥0.9·(first MFR2).

13 . Decolorized polyolefin composition obtained by the process according to claim 1 wherein the difference between the oxidation induction time (OIT) of the decolorized polyolefin composition of (a) and the polyolefin composition of (a) expressed as percentage (ΔOIT %) is between −73% and −52% inclusive.

14 . A process for decolorizing a polyolefin composition comprising at least one polyolefin and at least one organic chromophore, comprising using an inorganic oxidizing agent selected from the group of hypochlorites to decolorize the polyolefin composition.

15 . Process for recycling a polyolefin composition comprising at least one polyolefin and at least one organic chromophore, the process for recycling comprising the process for decolorizing a polyolefin composition according to claim 1 .

Assignees

• Borealis Ag
• Borealis Gmbh

Inventors

• Koller Kerstin
• Burgstaller Christoph
• Braun Hermann
• Denifl Peter
• Gahleitner Markus

Classifications

• C08J2423/06

  Polyethene · CPC title

• C08K3/20

  Oxides; Hydroxides {(graphene oxides C08K3/042)} · CPC title

• C08J11/16

  by treatment with inorganic material (C08J11/14 takes precedence) · CPC title

• C08F10/02

  Ethene · CPC title

• C08F2/44 Primary

  Polymerisation in the presence of compounding ingredients, e.g. plasticisers, dyestuffs, fillers · CPC title