Claims Analysis
Total Claims: 14
Claim 1
Independent Claim
272 words
Process for the reduction of the free aldehyde content in a polyester melt during production of shaped polyester food packaging material which does not affect taste of the food, the steps of which are carried out as polyester in the melt phase flows directly from a poly-condensation reactor to a shaping apparatus, said polyester having at least 70 wt % ethylene glycol units based on the total diol units, said process comprising (a) providing a polyester melt which contains, in addition to conventional reaction catalysts, an added 5-120 ppm of a) cobalt or b) cobalt and manganese in a molar ratio of 1:1 to 3:1 and c) phosphorus in a molar amount equal to or twice the molar amount of cobalt, each in the form of their polyester-soluble compounds, (b) introducing an inert gas through a gas inlet and uniformly distributing said inert gas into said polyester melt immediately after leaving said polycondensation reactor in an amount, by weight, not in excess of the amount of polyester by weight to reduce the free aldehyde content of said polyester melt, (c) adding from 0.05 to 1.0 wt % of a low-volatility acetaldehyde-reducing amide, said amide being added to the polyester melt through an inlet next to said inert gas inlet, (d) vacuum degassing said polyester melt immediately before entering said shaping apparatus, (e) sending said degassed polyester melt to said shaping apparatus for processing into said shaped polyester food packaging, and (f) maintaining the temperature of said polyester melt at not more than 35° C. above the crystallite melting point for a maximum dwell time of 30 minutes between steps (b) to (e).
Claim 2
Dependent Claim
272 words
Process for the reduction of the free aldehyde content in a polyester melt during production of shaped polyester food packaging material which does not affect taste of the food, the steps of which are carried out as polyester in the melt phase flows directly from a poly-condensation reactor to a shaping apparatus, said polyester having at least 70 wt % ethylene glycol units based on the total diol units, said process comprising (a) providing a polyester melt which contains, in addition to conventional reaction catalysts, an added 5-120 ppm of a) cobalt or b) cobalt and manganese in a molar ratio of 1:1 to 3:1 and c) phosphorus in a molar amount equal to or twice the molar amount of cobalt, each in the form of their polyester-soluble compounds, (b) introducing an inert gas through a gas inlet and uniformly distributing said inert gas into said polyester melt immediately after leaving said polycondensation reactor in an amount, by weight, not in excess of the amount of polyester by weight to reduce the free aldehyde content of said polyester melt, (c) adding from 0.05 to 1.0 wt % of a low-volatility acetaldehyde-reducing amide, said amide being added to the polyester melt through an inlet next to said inert gas inlet, (d) vacuum degassing said polyester melt immediately before entering said shaping apparatus, (e) sending said degassed polyester melt to said shaping apparatus for processing into said shaped polyester food packaging, and (f) maintaining the temperature of said polyester melt at not more than 35° C. above the crystallite melting point for a maximum dwell time of 30 minutes between steps (b) to (e).
Claim 3
Dependent Claim
31 words
Process of claim 1 in which said polyester of step (a) has been produced by esterification and subsequent polycondensation and said added compounds are present in an amount of 5-60 ppm.
Claim 4
Dependent Claim
20 words
Process of claim 1 in which said polyester of step (a) has been produced by ester interchange and subsequent polycondensation.
Claim 5
Dependent Claim
30 words
Process of claim 1 in which the inert gasses added in step (b) are taken from the group consisting of nitrogen, helium, carbon dioxide, methane, ethane, butane and mixtures thereof.
Claim 6
Dependent Claim
22 words
Process of claim 1 in which said gas and said amide of steps (b) and (c) are uniformly distributed by static mixing.
Claim 7
Dependent Claim
19 words
Process of claim 1 in which step (d) is performed within a dwell time of less than 5 minutes.
Claim 8
Dependent Claim
18 words
Process of claim 6 in which step (d) is performed at a pressure of less than 20 mbar.
Claim 9
Dependent Claim
19 words
Process of claim 1 in which step (e) is performed with a dwell time of less than one minute.
Claim 10
Dependent Claim
22 words
Process of claim 1 in which said polyester melt in step (e) has a free acetaldehyde content of less than 5 ppm.
Claim 11
Dependent Claim
15 words
Process of claim 9 in which said free acetaldehyde content is less than 3 ppm.
Claim 12
Dependent Claim
29 words
Process of claim 1 in which the polyester melt in step (a) undergoes a change in intrinsic viscosity amounting to a maximum of ±5% between steps (b) to (e).
Claim 13
Dependent Claim
73 words
Process of claim 1 in which said polyester in step (a) is an ethylene dicarboxylate homopolyester or copolyester having an intrinsic viscosity of at least 0.50 dl/g, the dicarboxylic acid component of said polyester being taken from the group consisting of terephthalic acid, isophthalic acid, 2,6-naphthalene dicarboxylic acid and mixtures thereof, and the diol component, in addition to said ethylene glycol, being taken from the group consisting of 1,4-cyclohexane dimethanol and diethylene glycol.
Claim 14
Dependent Claim
32 words
The process of claim 7 in which during the vacuum degassing step the polyester melt is stirred creating a shearing force in the melt, said shearing force being as low as possible.