Method for production of a high molecular weight polyester prepared from a prepolymer polyester having an optimal carboxyl content

Claim 3

A method according to claim 1, wherein said prepolymerization reaction comprises a dicarboxylic esterification stage, a partial polycondensation vacuum stage, and a particle preparation stage; and wherein said polymerization reaction comprises a drying stage and a solid state polymerization stage.

Claim 4

A method according to claim 2, wherein said dicarboxylic compound is a dicarboxylic acid, and said dicarboxylic esterification stage has a reaction temperature from about 240° C. to about 290° C., has a reaction pressure of at least atmospheric pressures, and has a termination when from about 90% to about 95% of said dicarboxylic acid has been esterified by said glycol; and wherein said partial polycondensation vacuum stage has a reaction temperature from about 260° C. to about 290° C., has a reaction pressure of at least sub-atmospheric pressures, and has a termination when said polyester prepolymer has an intrinsic viscosity from about 0.40 dl/g to about 0.62 dl/g; wherein said drying stage has a temperature from about 140° C. to about 180° C., has a duration from about 30 minutes to about 2 hours, and has a drying gas selected from the class consisting of air, argon, helium, nitrogen, and combinations thereof; and wherein said solid state polymerization has a temperature between about 200° C. and 240° C., has a duration until said polycondensed polyester intrinsic viscosity is at least 0.70 dl/g, and has a carrier gas at a flow rate of at least 1 ft. per minute, said carrier gas selected from the group consisting of argon, helium, nitrogen, and combinations thereof, so that a high molecular weight, high purity polycondensed polyester is formed at a 25% to 75% improved average reaction rate.

Claim 5

A method according to claim 3, wherein said subatmospheric pressures reach a pressure measuring less than 1.0 mm of mercury; wherein said partial polycondensation reaction temperature is from about 270° C. to about 285° C.; wherein said drying gas is nitrogen gas; and wherein said solid state polymerization stage temperature is from about 220° C. to about 230° C. and said carrier gas is nitrogen gas.

Claim 6

A method according to claim 2, wherein said particle preparation stage divides said prepolymer polyester into particles having between 1/8 inch cube diced and +20 Tyler mesh size.

Claim 7

A method according to claim 5, wherein said prepolymer particles have a -6 +12 Tyler mesh size.

Claim 8

A method according to claim 6, wherein said prepolymer particles have a -8 +10 Tyler mesh size.

Claim 9

A method according to claim 3, wherein said polyester prepolymer is formed by a two-stage reaction, said first stage reacting 1.0 moles of dicarboxylic acid and about 1.20 moles of glycol, said first reaction occurring during said dicarboxylic esterification stage and said second stage reacting make-up dicarboxylic acid, such that the overall glycol/dicarboxylic acid molar ratio is from about 1.02:1.0 to about 1.15:1.0, said second stage occurring during said dicarboxylic esterification stage.

Claim 10

A method according to claim 3, wherein said polyester prepolymer is formed by a two-stage reaction, said first stage reacting 1.0 moles of dicarboxylic acid and about 1.20 moles of glycol, said first reaction occurring during said dicarboxylic esterification stage and said second stage reacting make-up dicarboxylic acid, such that the overall glycol-dicarboxylic acid molar ratio is from about 1.02:1.0 to about 1.15:1.0, said second stage occurring after said dicarboxylic esterification stage and before said partial condensation vacuum stage.

Claim 12

A method according to claim 3 further comprising the step of forming a prepolymer heel by a reaction of 1.0 moles of dicarboxylic acid and greater than about 1.2 moles of glycol, said heel formation reaction occurring prior to said dicarboxylic esterification stage; and wherein sufficient dicarboxylic acid is added to said heel to change the overall glycol/dicarboxylic acid molar ratio from about 1.02:1.0 to about 1.15:1.0; and wherein said polyester prepolymer is formed in said prepolymerization reaction by reacting in the presence of said heel 1.0 moles of dicarboxylic compound and from about 1.02 to about 1.15 moles of said glycol, said reaction occurring during said dicarboxylic esterification stage.

Claim 13

A method according to claim 11, wherein said polyester prepolymer formed in the presence of said heel reacts 1.0 moles of dicarboxylic acid and from about 1.03 to about 1.10 moles of said glycol.

Claim 14

A method according to claim 10, wherein said dicarboxylic acid is dimethylterephthalic acid and said glycol is 1,4 butane diol.

Claim 15

A method according to claim 10, wherein said dicarboxylic acid is terephthalic acid and said glycol is ethylene glycol.

Claim 16

A method according to claim 11, wherein said dicarboxylic acid is dimethylterephthalic acid and said glycol is 1,4 butane diol.

Claim 17

A method according to claim 2, wherein said dicarboxylic acid is terephthalic acid and said glycol is ethylene glycol.

Claim 18

A method according to claim 2, wherein said dicarboxylic compound is a dicarboxylic ester; wherein said dicarboxylic esterification stage has a reaction temperature from about 180° C. to about 250° C., has a reaction pressure at atmospheric pressures, and has a termination when from about 95% to about 100% of said dicarboxylic ester has been exchanged by said glycol; wherein said partial polycondensation vacuum stage has a reaction temperature from about 260° C. to about 290° C., has a reaction pressure of at least subatmospheric pressures, and has a termination when said polyester prepolymer has an intrinsic viscosity from about 0.40 dl/g to about 0.62 dl/g; wherein said drying stage has a temperature from about 140° C. to about 180° C., has a duration from about 30 minutes to about 2 hours, and has a drying gas selected from the class consisting of air, argon, helium, nitrogen, and combinations thereof, and wherein said solid state polymerization has a temperature between about 200° C. and 240° C., has a duration until said polycondensed polyester intrinsic viscosity is at least 0.70 dl/g, and has a carrier gas at a flow rate of at least 1 ft. per minute, said carrier gas selected from the group consisting of argon, helium, nitrogen and combinations thereof, so that a high molecular weight, high purity polycondensed polyester is formed at a 25% to 75% improved reaction rate.

Claim 19

A method according to claim 17, wherein said subatmospheric pressures reach a pressure measuring less than 1.0 mm of mercury; wherein said partial polycondensation reaction temperature is from about 270° C. to about 285° C.; wherein said drying gas is nitrogen gas; and wherein said solid state polymerization stage temperature is from about 220° C. to about 230° C. and said carrier gas is nitrogen gas.

Claim 20

A method according to claim 17, wherein said polyester prepolymer is formed by a two-stage process, said first stage reacting 1.0 moles of dicarboxylic ester and from about 1.70 to about 2.20 moles of glycol, said reaction occurring during said dicarboxylic esterification stage; said second stage reacting with said first stage product, sufficient dicarboxylic acid to form a dicarboxylic acid/dicarboxylic ester molar ratio between about 0.05:1.0 and 0.50:1.0, said second stage occurring during said dicarboxylic esterification stage.

Claim 21

A method according to claim 17, wherein said polyester prepolymer is formed by a two-stage process, said first stage reacting 1.0 moles of dicarboxylic ester and from about 1.70 to about 2.20 moles of glycol, said reaction occurring during said dicarboxylic esterification stage; said second stage reacting sufficient dicarboxylic acid to form a dicarboxylic acid/dicarboxylic ester molar ratio between about 0.05:1.0 and 0.50:1.0, said second stage occurring after said dicarboxylic esterification stage and before said partial polycondensation vacuum stage.

Claim 23

A method according to claim 21, wherein said dicarboxylic ester is dimethylterephthalate and said glycol is 1,4 butane diol.

Claim 24

A method according to claim 21, wherein said dicarboxylic ester is dimethylterephthalate and said glycol is ethylene glycol.

Claim 25

A method according to claim 21, wherein said dicarboxylic acid is terephthalic acid.

Claim 26

A polyester prepolymer having an optimal carboxyl content to maximize a subsequent solid state polymerization reaction rate, comprising: the reaction product of a glycol and a dicarboxylic compound selected from the group consisting of dicarboxylic acids and dicarboxylic esters, said reaction product having an intrinsic viscosity from about 0.40 dl/g to about 0.62 dl/g and having a carboxyl end group content from about 18% to about 40% of total end group, said dicarboxylic acids selected from the group consisting of alkyl dicarboxylic acids having a total of from 2 to 16 carbon atoms, and aryl dicarboxylic acids containing a total of from 8 to 16 carbon atoms, said dicarboxylic esters selected from the group consisting of alkyl esters having from 2 to 20 carbon atoms and an alkyl substituted aryl ester having from 10 to 20 carbon atoms, said glycol selected from the group consisting of glycols having 2 to 10 carbon atoms.

Claim 27

A polyester prepolymer having an optimal carboxyl content to maximize a subsequent solid state polymerization reaction rate, comprising: the reaction product of a glycol and a dicarboxylic compound selected from the group consisting of dicarboxylic acids and dicarboxylic esters, said reaction product having an intrinsic viscosity from about 0.40 dl/g to about 0.62 dl/g and having a carboxyl end group content from about 18% to about 40% of total end group, said dicarboxylic acids selected from the group consisting of alkyl dicarboxylic acids having a total of from 2 to 16 carbon atoms, and aryl dicarboxylic acids containing a total of from 8 to 16 carbon atoms, said dicarboxylic esters selected from the group consisting of alkyl esters having from 2 to 20 carbon atoms and an alkyl substituted aryl ester having from 10 to 20 carbon atoms, said glycol selected from the group consisting of glycols having 2 to 10 carbon atoms.

Claim 28

A polyester prepolymer as in claim 25, wherein said reaction product is formed by a prepolymerization reaction process, said process comprising a dicarboxylic esterification stage, a partial polycondensation vacuum stage, and a particle preparation stage.

Claim 29

A prepolymer polyester produced according to claim 26, wherein said dicarboxylic compound is a dicarboxylic acid, and said dicarboxylic esterification stage has a reaction temperature from about 240° C. to about 290° C., has a reaction pressure of at least atmospheric pressures, and has a termination when from about 90% to about 95% of said dicarboxylic acid has been esterified by said glycol; and wherein said partial polycondensation vacuum stage has a reaction temperature from about 260° C. to about 290° C., has a reaction pressure of at least subatmospheric pressures, and has a termination when said polyester prepolymer has an intrinsic viscosity from about 0.40 dl/g to about 0.62 dl/g.

Claim 30

A prepolymer polyester produced according to claim 27, wherein said subatmospheric pressures reach a pressure measuring less than 1.0 mm of mercury; wherein said partial polycondensation reaction temperature is from about 270° C. to about 285° C.; wherein said drying gas is nitrogen gas; and wherein said solid state polymerization stage temperature is from about 220° C. to about 230° C. and said carrier gas is nitrogen gas.

Claim 31

A prepolymer polyester produced according to claim 27, wherein said polyester prepolymer is formed by a two-stage reaction, said first stage reacting 1.0 moles of dicarboxylic acid and about 1.20 moles of glycol, said first reaction occurring during said dicarboxylic esterification stage and said second stage reacting make-up dicarboxylic acid, such that the overall glycol/dicarboxylic acid molar ratio is from about 1.02:1.0 to about 1.15:1.0, said second stage occurring during said dicarboxylic esterification stage.

Claim 32

A prepolymer polyester produced according to claim 27, wherein said polyester prepolymer is formed by a two-stage reaction, said first stage reacting 1.0 moles of dicarboxylic acid and greater than about 1.20 moles of dicarboxylic acid and greater than about 1.20 moles of glycol, said first reaction occurring during said dicarboxylic esterification stage and said second stage reacting make-up dicarboxylic acid, such that the overall glycol/dicarboxylic acid molar ratio is from about 1.02:1.0 to about 1.15:1.0, said second stage occurring after said dicarboxylic esterification stage and before said partial condensation vacuum stage.

Claim 33

A prepolymer polyester produced according to claims 29 or 30, wherein said second stage adds sufficient make-up dicarboxylic acid, such that the overall glycol/dicarboxylic acid molar ratio is from about 1.03:1.0 to about 1.10:1.0.

Claim 34

A prepolymer polyester produced according to claim 27 further comprising the step of forming a prepolymer heel by a reaction of 1.0 moles of dicarboxylic acid and about 1.2 moles of glycol, said heel formation reaction occurring prior to said dicarboxylic esterification stage; and wherein sufficient dicarboxylic acid is added to said heel to change the overall glycol/dicarboxylic acid molar ratio from about 1.02:1.0 to about 1.15:1.0; and wherein said polyester prepolymer is formed in said prepolymerization reaction by reacting in the presence of said heel 1.0 moles of dicarboxylic compound and from about 1.02 to about 1.15 moles of said glycol, said reaction occurring during said dicarboxylic esterification stage.

Claim 35

A polyester prepolymer produced according to claim 32, wherein said polyester prepolymer formed in the presence of said heel reacts 1.0 moles of dicarboxylic acid and from about 1.03 to about 1.10 moles of said glycol.

Claim 36

A polyester prepolymer produced according to claim 31, wherein said dicarboxylic acid is dimethylterephthalic acid and said glycol is 1,4 butane diol.

Claim 37

A polyester prepolymer produced according to claim 31, wherein said dicarboxylic acid is terephthalic acid and said glycol is ethylene glycol.

Claim 38

A polyester prepolymer produced according to claim 32, wherein said dicarboxylic acid is dimethylterephthalic acid and said glycol is 1,4 butane diol.

Claim 39

A polyester prepolymer produced according to claim 33, wherein said dicarboxylic acid is terephthalic acid and said glycol is ethylene glycol.

Claim 40

A polyester prepolymer produced according to claim 26, wherein said dicarboxylic compound is a dicarboxylic ester; wherein said dicarboxylic esterification stage has a reaction temperature from about 180° C. to about 250° C., has a reaction pressure at atmospheric pressures, and has a termination when from about 95% to about 100% of said dicarboxylic ester has been exchanged by said glycol; wherein said partial polycondensation vacuum stage has a reaction temperature from about 260° C. to about 290° C., has a reaction pressure of at least subatmospheric pressures, and has a termination when said polyester prepolymer has an intrinsic viscosity from about 0.40 dl/g to about 0.62 dl/g; wherein said drying stage has a temperature from about 140° C. to about 180° C., has a duration from about 30 minutes to about 2 hours, and has a drying gas selected from the class consisting of air, argon, helium, nitrogen, and combinations thereof; and wherein said solid state polymerization has a temperature between about 200° C. and 240° C., has a duration until said polycondensed polyester intrinsic viscosity is at least 0.70 dl/g, and has a carrier gas at a flow rate of at least 1 ft. per minute, said carrier gas selected from the group consisting of argon, helium, nitrogen and combinations thereof.

Claim 41

A prepolymer polyester produced according to claim 38, wherein said subatmospheric pressures reach a pressure measuring less than 1.0 mm of mercury; wherein said partial polycondensation reaction temperature is from about 270° C. to about 285° C.; wherein said drying gas is nitrogen gas; and wherein said solid state polymerization stage temperature is from about 220° C. to about 230° C. and said carrier gas is nitrogen gas.

Claim 42

A polyester prepolymer produced according to claim 38, wherein said polyester prepolymer is formed by a two-stage process, said first stage reacting 1.0 moles of dicarboxylic ester and from about 1.70 to about 2.20 moles of glycol, said reaction occurring during said dicarboxylic esterification stage; said second stage reacting with said first stage product, sufficient dicarboxylic acid to form a dicarboxylic ester molar ratio between about 0.05:1.0 and 0.50:1.0, said second stage occurring during said dicarboxylic esterification stage.

Claim 43

A polyester prepolymer produced according to claim 38, wherein said polyester prepolymer is formed by a two-stage process, said first stage reacting 1.0 moles of dicarboxylic ester and from about 1.70 to about 2.20 moles of glycol, said reaction occurring during said dicarboxylic esterification stage; said second stage reacting sufficient dicarboxylic acid to form a dicarboxylic acid/dicarboxylic ester molar ratio between about 0.05:1.0 and 0.50:1.0, said second stage occurring after said dicarboxylic esterification stage and before said partial polycondensation vacuum stage.

Claim 44

A polyester prepolymer produced according to claims 37 or 38, wherein said dicarboxylic acid/dicarboxylic ester molar ratio is between about 0.10:1.0 and 0.30:1.0.

Claim 45

A polyester prepolymer produced according to claim 42, wherein said dicarboxylic ester is dimethylterephthalate and said glycol is 1,4 butane diol.

Claim 46

A polyester prepolymer produced according to claim 42, wherein said dicarboxylic ester is dimethylterephthalate and said glycol is ethylene glycol.

Claim 47

A polyester prepolymer produced according to claim 42, wherein said dicarboxylic acid is terephthalic acid.