METHOD FOR THE DIRECT PRODUCTION OF POLYESTER ARTICLES FOR PACKAGING PURPOSES AND ARTICLES OBTAINED THEREFROM

• US 20090270564A1
• Filed: 03/29/2007
• Published: 10/29/2009
• Est. Priority Date: 03/29/2006
• Status: Abandoned Application

• Current Assignee: Nestle Waters Management & Technology S.A.S. (Nestle SA)
• Original Assignee: Nestle Waters Management & Technology S.A.S. (Nestle SA)
• Inventors: Hartwig, Klaus, Gorlier, Eric Marie, Thiele, Ulrich Karl
• Application Number:
  US12/293,447
• Publication Number:
  US 20090270564A1
• Time in Patent Office: Days
• US Class Current: 525/439
• CPC Class Codes: C08G 63/78 Preparation processes
• CPC Class Codes: C08G 63/88 Post-polymerisation treatment
• CPC Class Codes: C08G 63/916 Dicarboxylic acids and dihydroxy compounds
• CPC Class Codes: C08J 2367/02 Polyesters derived from dicarboxylic acids and dihydroxy compounds; C08J2367/06 takes precedence
• CPC Class Codes: C08J 5/18 Manufacture of films or sheets

Abstract

The present invention is related to a method for the direct production of polyester articles for packaging purposes, in particular for the production of hollow bodies, thermoformed sheets and films, said articles containing an amount of acetaldehyde less than 10 ppm. This method is characterised in that it essentially comprises a step in which the initial level SE₀ of the sum of end groups in the polymer melt is increased by adding a mixture of at least one inert and at least one reactive substance to said polymer melt to a second level SE₁ and a degassing step consisting in essentially applying a vacuum to the previously obtained polymer melt to cause a removal of low molecular weight substances present and formed, of non reacted reactive substance(s) and inert substance(s) added during previous step before the so obtained polymer melt is directly converted into the desired articles.

Claims

1. Method for the production of polyester articles for packaging purposes, containing an amount less than 10 ppm of acetaldehyde, consisting of essentially the following steps:

a) providing a polyethylene terephthalate based polymer melt which is directly produced by conversion of more than 90 weight % of terephthalic acid or dimethyl terephthalate and ethylene glycol, the polymer melt having an intrinsic viscosity (IV₀) at an outlet of a polycondensation reactor in a range of 0.5 dl/g to 0.90 dl/g;

b) adding to sad the polymer melt, a mixture of at least one inert and at least one reactive substances which reacts with at least one of the groups selected from the group consisting of the —

COOH, —

OH, —

COO—

CH═

CH₂ end groups of the polyester and the ester bonds of the polyester chain in order to cause an increase of the sum of end groups from an initial level SE₀ at the end of step a) to a first level SE₁ at the end of his step b); and

c) removing low molecular weight monomer substances having a molecular weight of not greater than 500 g/mol present and formed, the non-reacted reactive substance(s) and the inert substance(s) added during step b) after a reaction time of greater than 1 second and less than 3600 seconds by subjecting the polymer melt to a degassing step comprising applying a vacuum of 0.05-800 mbar causing a partial polycondensation, which thereby causes a decrease of the sum of end groups from said first level SE₁ to a second sum of end group level SE₂ at the end of this step; and

d) converting directly the obtained polymer melt into desired articles.

2. Method according to claim 1, wherein the polyester melt comprises up to 10 weight % of one or a mixture of co-monomers selected from the group consisting of:

diethylene glycol, triethylene glycol, isophthalic acid, naphthalene dicarboxylic acid, adipic acid, cyclohexane dimethanol, pyromellitic acid, trimellitic acid, pentaerythrol, neopentylglycol, triethylene glycol tetraethylene glycol, pentaethylene glycol, polyethylenglycol and polypropylenglycol.

3. Method according to claim 1, wherein the amount of acetaldehyde contained in the polymer melt at the outlet of the polycondensation reactor is between 1 and 150 ppm.

4. Method according to claim 1, wherein the added amount of reactive substance(s) during step b) is sufficient to reach a first level of the sum of end groups SE₁ after step b, which is increased by ≧

1% and ≦

30% compared to the sum of end group level SE₀ of the polymer melt at the end of step a).

5. Method according to claim 1, wherein the step of adding of a reactive substance or substance mixture to the polymer melt after the polycondensation reactor during step b) is carried out continuously.

6. Method according to claim 1, wherein the added reactive substance or substance mixture is applied during step b) with an inert gaseous carrier.

7. Method according to claim 1, wherein the reactive substance or substance mixture added during step b) is selected from the group consisting of:

water for hydrolysis,

at least one monofunctional or polyfunctional alcohol,

at least one monofunctional or polyfunctional carbonic acid

at least one hydroxycarbonic acid,

at least one primary, secondary or tertiary amines or mixtures of these,

hydrazine and/or its derivatives,

substances which, under the conditions existing in the polyester melt, decay into the described reactive substances, and

at least one anhydride of monocarbonic acids,

and wherein the condition of aggregation of the above described reactive substance or substance mixture is selected from the group consisting of liquid gaseous and supercritical.

8. Method according to claim 1, wherein the degassing step carried out in step c) is carried out in an atmosphere of 0.1 to 10 mbar.

9. Method according to claim 1, wherein the levels of sum of end groups in the polymer melt satisfies:

SE₀<

SE₁ and SE₀<

SE₂ and SE₂<

1,3SE₀

wherein

SE₂=level of the sum of end groups at the end of step a),

SE₁=level of the sum of end groups at the end of step b), and

SE₂=level of the sum of end groups at the end of step c).

12. Method according to claim 1, wherein the added amount of reactive substance(s) during step b) is sufficient to reach a first level of the sum of end groups SE₁ after this step, which is increased by between 4% and 8% compared to the sum of end group level SE₀ of the polymer melt at the end of step a).

13. Method according to claim 1, wherein the added reactive substance or substance mixture is applied during step b) with an inert gaseous selected from the group consisting of:

nitrogen, hydrogen, helium, argon, carbon dioxide, ethane, propane, butane, n-hexane, cyclohexane or mixtures out of these substances.

14. Method according to claim 1, wherein the reactive substance or substance mixture added during step b) is selected in the group consisting of:

water for hydrolysis;

at least one monofunctional or polyfunctional alcohol, selected from the group consisting of;

methanol, ethanol, butanol, propanol, isopropanol, isobutanol, ethylene glycol, diethylene glycol, polyethylene glycol and polypropylene glycol, for alcoholysis;

at least one monofunctional or polyfunctional carbonic acid selected from the group consisting of formic acid, acetic acid and propionic acid;

at least one hydroxycarbonic acid;

at least one primary, secondary or tertiary amines or mixtures;

hydrazine and/or its derivatives;

substances which, under the conditions existing in the polyester melt, decay into the described reactive substances selected from the group consisting of ethylene carbonate, propylene carbonate and methylacetate; and

at least one anhydride of monocarbonic acids, selected from the group consisting of acetic acid anhydride, isobutyric anhydride and butyric anhydride.

10. Polyester articles for packaging purposes comprising an acetaldehyde content of less than 10 ppm, provided by a method consisting of essentially the following steps:

a) providing a polyethylene terephthalate based polymer melt which is directly produced by conversion of more than 90 weight % of terephthalic acid or dimethyl terephthalate and ethylene glycol, the polymer melt having an intrinsic viscosity (IV₀) at an outlet of a polycondensation reactor in a range of 0.5 dl/g to 0.90 dl/g;

b) adding to the polymer melt, a mixture of at least one inert and at least one reactive substances which reacts with at least one of the groups selected from the group consisting of the —

COOH, —

OH, —

COO—

CH═

CH₂ end groups of the polyester and the ester bonds of the polyester chain in order to cause an increase of the sum of end groups from an initial level SE₀ at the end of step a) to a first level SE₁ at the end of step b);

c) removing low molecular weight monomer substances having a molecular weight ≦

500 g/mol present and formed, the non-reacted reactive substance(s) and the inert substance(s) added during step b) after a reaction time of >

1 second and <

3600 seconds by subjecting the polymer melt to a degassing step comprising applying a vacuum of 0.05-800 mbar causing a partial polycondensation, which thereby causes a decrease of the sum of end groups from said first level SE₁ to a second sum of end group level SE₂ at the end of this step; and

d) converting directly the obtained polymer melt into desired articles.

11. Method for the production of polyester articles comprising less than 10 ppm acetaldehyde, comprising the steps:

a) providing a polyethylene terephthalate based polymer melt which is produced by conversion of more than 90 weight % of terephthalic acid or dimethyl terephthalate and ethylene glycol, the polymer melt having an intrinsic viscosity (IV₀) at the outlet of the polycondensation reactor in a range of 0.5 dl/g to 0.90 dl/g;

b) adding to the polymer melt, a mixture of at least one inert and at least one reactive substances which reacts with the —

COOH, —

OH, or —

COO—

CH═

CH₂ end groups of the polyester and/or with the ester bonds of the polyester chain thereby causing an increase of the sum of end groups from an initial level SE₀ at the end of step a) to a first level SE₁ at the end of step b),

c) removing low molecular weight monomer substances that are formed and have a molecular weight of not greater than 500 g/mol, the non-reacted reactive substance(s) and the inert substance(s) added during step b) after a reaction time of less than 3600 seconds by subjecting the polymer melt to a degassing step causing a decrease of the sum of end groups from the first level SE₁ to a second sum of end group level SE₂ at the end of step c); and

d) converting directly the polymer melt into the desired articles.