Recyclable extrusion blow molded articles from blends of copolyesters and recycled PET
AssigneeEastman Chemical Company
InventorsMark Allan Treece, Michael Gage Armstrong, Robert William Seymour
Life of this patent
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Abstract
The present disclosure relates to recyclable extrusion blow molded articles made from blends of recycled PET and copolyester compositions which comprise residues of terephthalic acid, neopentyl glycol (NPG), 1,4-cyclohexanedimethanol (CHDM), ethylene glycol (EG), and/or 2,2,4,4-tetramethyl-1,3-cyclobutanediol residues, in certain compositional ranges that are <4 mm thickness, have a high level of recycled PET content, have low haze and are recyclable in a PET stream.
Claims8
A method of making a recyclable, extrusion blow-molded article comprising:
- (A) compounding a rPET/copolyester blend which comprises:
- (1) 20-80 wt % of recycled polyethylene terephthalate (rPET);
- and
- (2) 20-80 wt % of at least one copolyester which comprises:
- (a) a dicarboxylic acid component comprising:
- i) 70 to 100 mole % of terephthalic acid residues, dimethyl terephthalic acid, and/or isophthalic acid;
- and
- ii) 0 to 30 mole % of aromatic and/or aliphatic dicarboxylic acid residues having up to 20 carbon atoms;
- and;
- iii) 0 to 5 mole % of a branching monomer;
- and
- (b) a glycol component comprising:
- i) 15 to 35 mole % of 2,2,4,4-tetramethyl-1,3-cyclobutanediol residues;
- and
- v) 65 to 85 mole % of ethylene glycol residues;
- and
- vi) 0 to 5 mole % of a branching monomer;
- and
- wherein the total mole % of the dicarboxylic acid component is 100 mole %, and the total mole % of the glycol component is 100 mole %;
- and
- (3) 0.05 to 5 weight % of a chain extending agent based on the weight of the blend;
- and
- wherein the blend has 1-15 wt % total comonomer content from glycols and acids other than ethylene glycol (EG), terephthalic acid (TPA), or dimethyl terephthalate (DMT), and wherein the blend is compounded at a temperature of 260-320° C., and wherein the method further comprises drying the rPET at temperature of up to 150° C. and the copolyester at temperature of up to 65° C. before compounding;
- (B) pelletizing the compounded blend;
- (C) drying the compounded blend at a temperature of 60-160° C., and optionally crystallizing the compounded blend at 120-180° C. before drying;
- (D) melting the compounded blend in an extruder and extruding the molten composition through a die to form a tube or parison of molten polymer;
- and
- (E) clamping a mold having the desired finished shape around the parison;
- (F) blowing air into the parison, causing it to stretch and expand to fill the mold;
- (G) cooling the molded article and ejecting the resulting article from the mold;
- and
- (H) removing excess plastic from the article;
- wherein the article is transparent and/or has a haze value of less than 20%;
- wherein the article has a melting temperature (Tm) of 230-250° C.;
- wherein the article has an enthalpy of melting (Hm) greater than 0.20 cal/g;
- wherein the inherent viscosity of the copolyester is 0.50 to 1.2 dL/g as determined in 60/40 (wt/wt) phenol/tetrachloroethane at a concentration of 0.5 g/100 ml at 25° C.;
- wherein the copolyester has a Tg of 70 to 115° C.;
- wherein the rPET/copolyester blend has a melt viscosity at 1 rad/s and 260° C. of 10,000 to 120,000 poise;
- and wherein the article has a thickness of less than 4 mm, and wherein the article is recyclable in a PET recycle stream.
A method of making a recyclable, extrusion blow-molded article comprising:
- (A) compounding a rPET/copolyester blend which comprises:
- (1) 20-80 wt % of recycled polyethylene terephthalate (rPET);
- and
- (2) 20-80 wt % of at least one copolyester which comprises:
- (a) a dicarboxylic acid component comprising:
- i) 70 to 100 mole % of terephthalic acid residues, dimethyl terephthalic acid, and/or isophthalic acid;
- and
- ii) 0 to 30 mole % of aromatic and/or aliphatic dicarboxylic acid residues having up to 20 carbon atoms;
- and;
- iii) 0 to 5 mole % of a branching monomer;
- and
- (b) a glycol component comprising:
- i) 30 to less than 50 mole % of 1,4-cyclohexanedimethanol residues;
- ii) 50 to 70 mole % of ethylene glycol residues;
- iii) 0 to 5 mole % of a branching monomer;
- and
- wherein the total mole % of the dicarboxylic acid component is 100 mole %, and the total mole % of the glycol component is 100 mole %;
- and
- (3) 0.05 to 5 weight % of a chain extending agent based on the weight of the blend;
- and
- wherein the blend has 1-15 wt % total comonomer content from glycols and acids other than ethylene glycol (EG), terephthalic acid (TPA), or dimethyl terephthalate (DMT), and wherein the blend is compounded at a temperature of 260-320° C., and wherein the method further comprises drying the rPET at temperature of up to 150° C. and the copolyester at temperature of up to 65° C. before compounding;
- (B) pelletizing the compounded blend;
- (C) drying the compounded blend at a temperature of 60-160° C., and optionally crystallizing the compounded blend at 120-180° C. before drying;
- (D) melting the compounded blend in an extruder and extruding the molten composition through a die to form a tube or parison of molten polymer;
- and
- (E) clamping a mold having the desired finished shape around the parison;
- (F) blowing air into the parison, causing it to stretch and expand to fill the mold;
- (G) cooling the molded article and ejecting the resulting article from the mold;
- and
- (H) removing excess plastic from the article;
- wherein the article is transparent and/or has a haze value of less than 20%;
- wherein the article has a melting temperature (Tm) of 230-250° C.;
- wherein the article has an enthalpy of melting (Hm) greater than 0.20 cal/g;
- wherein the inherent viscosity of the copolyester is 0.50 to 1.2 dL/g as determined in 60/40 (wt/wt) phenol/tetrachloroethane at a concentration of 0.5 g/100 ml at 25° C.;
- wherein the copolyester has a Tg of 70 to 115° C.;
- wherein the rPET/copolyester blend has a melt viscosity at 1 rad/s and 260° C. of 10,000 to 120,000 poise;
- and wherein the article has a thickness of less than 4 mm, and wherein the article is recyclable in a PET recycle stream.
Dependencies are inferred from the claim text.