Production of non-solid-stated polyester particles having solid-stated properties
DC CAFCFirst Claim
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1. A polyester polymer production process comprising:
- (a) forming polyester polymer particles from a polyester polymer melt in a particle forming zone;
(b) subsequent to step (a), quenching at least a portion of said particles via contact with a quench liquid in a quenching zone;
(c) subsequent to step (b), drying at least a portion of said particles in a drying zone;
(d) subsequent to step (c), crystallizing at least a portion of said particles in a crystallizing zone; and
(e) subsequent to step (d), annealing at least a portion of said particles in an annealing zone wherein said particles have a residence time in said annealing zone of between 1 hour and 24 hours,wherein at all points during and between steps (b) through (e) the average bulk temperature of said particles is maintained above 165°
C., wherein the It.V. of said particles produced from said particle forming zone is within about 5 percent of the It.V. of said particles produced from said annealing zone, and wherein said polyester polymer melt comprises a carboxylic acid component and a hydroxyl component, wherein said carboxylic acid component comprises at least 80 mole percent of the residues of terephthalic acid and/or derivatives thereof, wherein said hydroxyl component comprises at least 80 mole percent of residues of ethylene glycol.
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Abstract
A process for producing non-solid-stated polyester polymer particles having one or more properties similar to polyester polymer particles that have undergone solid-state processing. In one embodiment, the process comprises (a) forming polyester polymer particles from a polyester polymer melt; (b) quenching at least a portion of the particles, (c) drying at least a portion of the particles, (d) crystallizing at least a portion of the particles, (e) annealing at least a portion of the particles. At all points during and between steps (b) through (e), the average bulk temperature of the particles is maintained above 165° C.
35 Citations
26 Claims
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1. A polyester polymer production process comprising:
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(a) forming polyester polymer particles from a polyester polymer melt in a particle forming zone; (b) subsequent to step (a), quenching at least a portion of said particles via contact with a quench liquid in a quenching zone; (c) subsequent to step (b), drying at least a portion of said particles in a drying zone; (d) subsequent to step (c), crystallizing at least a portion of said particles in a crystallizing zone; and (e) subsequent to step (d), annealing at least a portion of said particles in an annealing zone wherein said particles have a residence time in said annealing zone of between 1 hour and 24 hours, wherein at all points during and between steps (b) through (e) the average bulk temperature of said particles is maintained above 165°
C., wherein the It.V. of said particles produced from said particle forming zone is within about 5 percent of the It.V. of said particles produced from said annealing zone, and wherein said polyester polymer melt comprises a carboxylic acid component and a hydroxyl component, wherein said carboxylic acid component comprises at least 80 mole percent of the residues of terephthalic acid and/or derivatives thereof, wherein said hydroxyl component comprises at least 80 mole percent of residues of ethylene glycol. - View Dependent Claims (2, 3, 4, 5, 6, 7, 8, 9, 10, 11, 12, 13, 14, 15, 16)
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17. A polyester polymer production process comprising:
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(a) forming initial polyester polymer particles from a polymer melt having an intrinsic viscosity (It.V.) in the range of 0.70 dL/g to 1.2 dL/g when measured at 25°
C. in a 60/40 wt/wt phenol/tetrachloroethane solvent at a polymer concentration of 0.50 g/100 ml, wherein said initial particles comprise a shell and a core, wherein said shell is cooler and more crystalline than said core, wherein at least a portion of said shell exhibits strain-induced crystallinity;(b) drying at least a portion of said initial particles to thereby provide dried particles; (c) crystallizing at least a portion of said dried particles to thereby provide crystallized particles exhibiting both strain-induced crystallinity and spherulitic crystallinity; and (d) annealing at least a portion of said crystallized particles to thereby provide annealed particles, wherein said annealing occurs in an annealing zone, wherein the average bulk temperature of said annealed particles exiting said annealing zone is in the range of 170°
C. to 205°
C., and wherein an average particle residence time in said annealing zone is in the range of 1 hour to 24 hours,wherein the average bulk temperature of said initial particles and said dried particles is maintained above the onset-of-melting temperature (Tom) of said core, and wherein said polymer melt comprises a carboxylic acid component and a hydroxyl component, wherein said carboxylic acid component comprises at least 80 mole percent of the residues of terephthalic acid and/or derivatives thereof, wherein said hydroxyl component comprises at least 80 mole percent of residues of ethylene glycol, and wherein the It.V. of said initial particles is within about 5 percent of the It.V. of said annealed particles. - View Dependent Claims (18, 19, 20, 21, 22, 23, 24, 25, 26)
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Specification