# Patent

## Title
Poly(butylene-co-adipate terephthalate), method of manufacture and uses thereof

## Abstract

A method for preparing poly(butylene terephthalate-co-adipate) copolymer by polymerizing 1,4-butane diol, an adipic acid component and an aromatic dicarboxy compound derived from polyethylene terephthalate, and a polyester component residue in the presence of a catalyst under conditions effective to form poly(butylene terephthalate-co-adipate) oligomers; adding a quencher; and reacting the quenched poly(butylene terephthalate-co-adipate) oligomers with a chain extender.

## Background
BACKGROUND OF THE INVENTION
This disclosure relates to biodegradable aliphatic-aromatic copolyester compositions, and methods of manufacture of the copolyesters and compositions. These copolyesters and compositions are useful as molded or extruded plastic objects, films, and fibers.
Aliphatic-aromatic copolyesters are often used for the manufacture of biodegradable disposable articles. For example, U.S. Pat. No. 6,020,393 discloses a branched, random aliphatic-aromatic copolyester suitable for forming into biodegradable disposable articles, including poly(butylene-co-adipate terephthalate) (PBAT). U.S. Pat. No. 6,201,034 discloses processes for preparing PBAT by reacting dimethyl terephthalate (DMT) or terephthalic acid (TPA) and adipic acid (AA) with butanediol (BDO). The biodegradability is induced by the incorporation of adipic acid in poly(butylene terephthalate) (PBT). The polymer thus made has a typical melting point (Tm) of about 109° C., and a glass transition temperature (Tg) between −25 to −30° C. The polymerization is conducted using a transesterification (TE) catalyst such as a titanium or tin compound.
The present inventors have observed that biodegradable aliphatic-aromatic copolyester product obtained in such a reaction was discolored, often ranging from pink to red in color. This presents a problem in that the aesthetic appearance of a non-white polymer product is an obstacle to employing the polymer in end-uses where the discoloration is apparent and cannot be readily overcome or masked with pigments, whitening agents or fillers. It has further been found that it is difficult to achieve a white color while at the same time maintaining or improving upon other desirable properties of biodegradable aliphatic-aromatic copolyesters such as PBAT. For at least the foregoing reasons, there remains a long unfelt need to develop processes that produce useful biodegradable aliphatic-aromatic copolyesters.
SUMMARY OF THE INVENTION
In an embodiment, a poly(butylene terephthalate-co-adipate) copolymer is provided having a melt temperature from 105 to 125° C., wherein the copolymer comprises a polyester component residue derived from a terephthalic-containing polyester homopolymer, a terephthalic-containing polyester copolymer, and combinations thereof, and further comprising a polyester residue component; a quencher residue; and from 0.05 to 5 weight % based on total weight of poly(butylene terephthalate-co-adipate) copolymer of a residue of an isocyanurate, polyisocyanate, isocyanate, and combinations thereof.
In another embodiment, a method is provided for the manufacture of a poly(butylene terephthalate-co-adipate) copolymer, the method comprising: (a) polymerizing 1,4-butane diol and an acid component comprising, based on the total weight of the acid component, 1) from 20 to 95 mol % of an adipic acid component selected from adipic acid, an ester-forming derivative of adipic acid, and combinations thereof, and 2) from 5 to 80 mol % of an aromatic dicarboxy compound selected from an aromatic dicarboxylic acid, aromatic dicarboxylic (C1-3)alkyl ester derived from polyethylene terephthalate, or a combination thereof, and a polyester component residue derived from a terephthalic-containing polyester homopolymer, a terephthalic-containing polyester copolymer, and combinations thereof; in the presence of a catalyst under conditions effective to form poly(butylene terephthalate-co-adipate) oligomers; (b) adding a quencher, selected from a phosphorus-containing compound, a nitrogen-containing compound, a boron-containing compound, and combination thereof; and (c) reacting the quenched poly(butylene terephthalate-co-adipate) oligomers with from 0.05 to 5 weight %, based on total weight of poly(butylene terephthalate-co-adipate) oligomer, of a chain extender selected from isocyanurate, polyisocyanate, isocyanate and combinations thereof, to form the poly(butylene terephthalate-co-adipate) copolymers, wherein the copolymer has a melt temperature of 100 to 125° C., and a number average molecular weight of at least 30,000 g/mole; an intrinsic viscosity of at least 1.0 deciliter per minute; a Tg of −30 to −10° C., and the copolymer comprises a residue derived from the polyester residue component.
In another embodiment, a composition is provided comprising the poly(butylene terephthalate-co-adipate) copolymer and at least one of an additive selected from nucleating agents, antioxidants, UV stabilizers, starch plasticizers, epoxy compounds, melt strength additives, alcohols, acetates, alcohol-acetate copolymers, crosslinkers, anti-aging agents, retrogradation agents, anti-blocking agents, water, odor-controlling agents, and combinations thereof; and an additional thermoplastic polymer.
An article is described, comprising the above-described compositions.
A method of forming an article comprising molding, coating, calendaring, shaping, or extruding the above-described compositions.
These and other features, aspects, and advantages will become better understood with reference to the following Figures, Description, Examples, and appended claims.



BRIEF DESCRIPTION OF THE FIGURE
The FIGURE shows the effect of the impurities on the melting temperature of the poly(butylene-co-adipate terephthalate) copolymer examples prepared in the presence of a chain extender as described herein.



DETAILED DESCRIPTION OF THE INVENTION
The present inventors have surprisingly found that a poly(butylene-co-adipate terephthalate) copolymer prepared by reacting poly(butylene-co-adipate terephthalate) oligomers with a chain extender has an advantageous combination of properties. Advantageously, the oligomers are obtained from DMT monomers that are recovered from recycle polyethylene terephthalate. Surprisingly, the advantageous properties of the copolyesters are obtained even in the presence of a residue from the aromatic polyester if a quencher is added to the depolymerization mixture after the oligomers are formed.
The term “recycle” as used herein refers to any component that has been manufactured and either used or intended for scrap. Thus, a recycle polyester can be polyester that has been used, for example in a drinking bottle, or that is a byproduct of a manufacturing process, for example that does not meet a required specification and therefore would otherwise be discarded or scrapped. Recycle materials can therefore contain virgin materials that have not been utilized. Generally, in the case of PET, the PET includes recycle (scrap) PET in flake, powder/chip, film, or pellet form. Before use, the PET is generally processed to remove any impurities such as paper, adhesives, polyolefin, e.g., polypropylene, polyvinyl chloride (PVC), nylon, polylactic acid (an aliphatic polyester), and other contaminants.
The prefix “bio-” or “bio-derived” as used herein means that the compound or composition is ultimately derived from a biological source, e.g., “bio-1,3-propane diol” is derived from a biological (e.g., plant or microbial source) rather than a petroleum source. Similarly, the prefix “petroleum-” or “petroleum-derived” means that the compound or composition is ultimately derived from a petroleum source, e.g., a “petroleum-derived poly(ethylene terephthalate) is derived from reactants that are themselves derived from petroleum.
The singular forms “a,” “an,” and “the” include plural referents unless the context clearly dictates otherwise. “Or” means “and/or.” Further unless defined otherwise, technical, and scientific terms used herein have the same meaning as is commonly understood by one of skill in the art to which this invention belongs. Compounds are described using standard nomenclature. For example, any position not substituted by any indicated group is understood to have its valency filled by a bond as indicated, or a hydrogen atom. A dash (“—”) that is not between two letters or symbols is used to indicate a point of attachment for a substituent. For example, —CHO is attached through carbon of the carbonyl group.
The term “random copolymer,” as used in this application refers to a copolymer that includes macromolecules in which the probability of finding a given monomeric unit at any given site in the chain is independent of the nature of the adjacent units.
Other than in the operating examples or where otherwise indicated, all numbers or expressions referring to quantities of ingredients, reaction conditions, and the like, used in the specification and claims are to be understood as modified in all instances by the term “about.” Various numerical ranges are disclosed in this patent application. Because these ranges are continuous, they include every value between the minimum and maximum values. The endpoints of all ranges reciting the same characteristic or component are independently combinable and inclusive of the recited endpoint. Unless expressly indicated otherwise, the various numerical ranges specified in this application are approximations. The term “from more than 0 to” an amount means that the named component is present in some amount more than 0, and up to and including the higher named amount.
All ASTM tests and data are from the 2003 edition of the Annual Book of ASTM Standards unless otherwise indicated.
With respect to the terms “terephthalic acid group,” “isophthalic acid group,” “ethylene glycol group,” “butanediol group,” and “diethylene glycol group” being used to indicate, for example, the weight percent (wt. %) of the group in a molecule, the term “isophthalic acid group(s)” means the group or residue of isophthalic acid having the formula (—O(CO)C6H4(CO)—), the term “terephthalic acid group” means the group or residue of isophthalic acid having the formula (—O(CO)C6H4(CO)—), the term “diethylene glycol group” means the group or residue of diethylene glycol having the formula (—O(C2H4)O(C2H4)—), the term “butanediol group” means the group or residue of butanediol having the formula (—O(C4H8)—), and the term “ethylene glycol group” means the group or residue of ethylene glycol having the formula (—O(C2H4)—).
Any of the 1,4-butane diol, the adipic acid, or any other component of the copolyesters can be derived from a biological source. In an embodiment all or a portion of the 1,4-butane diol is derived from a biological source. “Bio-derived diols” as used herein refers to alcohols other than those named and derived from a biological source, e.g., various pentoses, hexoses, and the like.
The poly(butylene-co-adipate terephthalate) copolymers described herein comprise adipic acid groups, 1,4-butane diol groups, and aromatic dicarboxylic acid groups derived from DMT that is derived in turn from a poly(ethylene terephthalate) component, i.e., a poly(ethylene terephthalate) homopolymer, a poly(ethylene terephthalate) copolymer, or a combination thereof. Thus, the aromatic dicarboxylic ester groups comprise the polymerization product of dimethyl terephthalate derived from recycle PET and the dihydric alcohol (1,4-butanediol). The copolyester further comprises a dimethyl terephthalate residual composition. Processes for recovering dimethyl terephthalate, also referred to as DMT or the dimethyl ester of terephthalic acid from PET, are known in the art, for example as set forth in U.S. Pat. No. 6,472,557 and other patents disclosed therein. Typically, the polyethylene terephthalate is reacted at elevated temperature and suitable conditions with an alcohol, such as methanol, to break the ester linkages of the polyester and yield the corresponding diesters of the terephthalic acid, such as dimethyl terephthalate (DMT).
The copolyesters can further comprise other residues present in the poly(ethylene terephthalate) component, including catalyst residues from the manufacture of the poly(ethylene terephthalate) component, residues from additives in the poly(ethylene terephthalate) component, or residues arising from side reactions that occur during recovery of the DMT from the poly(ethylene terephthalate) component and/or the reaction of the first dihydric alcohol, the aliphatic diacid, and the DMT component. For example, in addition to butane diol groups, dihydric alcohol groups incorporated into the copolyester can be derived from any dihydric alcohol that reacts with the adipic acid and the DMT used to form the copolyester, such as groups derived from ethylene glycol, 1,2-propylene glycol, 1,3-propylene glycol, 1,2-butanediol, 2,3-butanediol, 1,4-butanediol, tetramethyl cyclobutanediol, isosorbide, cyclohexane dimethanol (including 1,2-, 1,3-, and 1,4-cyclohexane dimethanol), bio-derived diols, hexylene glycols, and a combination thereof. Such groups can arise, for example from a polyethylene terephthalate component containing polyethylene terephthalate copolymers.
Residues derived from the poly(ethylene terephthalate) component can be ethylene glycol groups, diethylene glycol groups, antimony-containing compounds, germanium-containing compounds, titanium-containing compounds, cobalt-containing compounds, tin-containing compounds, aluminum, aluminum salts, 1,3-cyclohexanedimethanol isomers, 1,4-cyclohexanedimethanol isomers, alkaline salts, alkaline earth metal salts, phosphorus-containing compounds and anions, sulfur-containing compounds and anions, naphthalene dicarboxylic acids, 1,3-propanediol groups, or combinations thereof. In an embodiment, the residue derived from the poly(ethylene terephthalate) component comprises ethylene glycol groups, diethylene glycol groups, and more particularly a combination of ethylene glycol groups, diethylene glycol groups.
Accordingly, our invention includes embodiments in which the residue derived from the poly(ethylene terephthalate) component includes individual elements and combinations of the foregoing materials. The residue derived from the poly(ethylene terephthalate) component, for instance, can comprise isophthalic acid groups, preferably in an amount of less than or equal to 2 mole %. In an embodiment, the residue derived from the poly(ethylene terephthalate) component further comprises the cis isomer of 1,3-cyclohexanedimethanol, cis isomer of 1,4-cyclohexanedimethanol, trans isomer of 1,3-cyclohexanedimethanol, trans isomer of 1,4-cyclohexanedimethanol and combinations thereof. In an embodiment, the residue derived from the poly(ethylene terephthalate) component includes a combination of ethylene glycol and diethylene glycol groups, optionally with isophthalic acid groups, and can further comprise the cis isomer of 1,3-cyclohexanedimethanol, the cis isomer of 1,4-cyclohexanedimethanol, the trans isomer of 1,3-cyclohexanedimethanol, trans isomer of 1,4-cyclohexanedimethanol, or combinations thereof. In an embodiment, the residue derived from the polyethylene terephthalate component comprises ethylene glycol groups, diethylene glycol groups, the cis isomer of cyclohexanedimethanol, the trans isomer of cyclohexanedimethanol, and combinations thereof. In an embodiment, the residue derived from the poly(ethylene terephthalate) component comprises ethylene glycol groups, diethylene glycol groups, and cobalt-containing compounds. The residues can be present in an amount from more than 0 to 10 wt. % of the copolymer, for example 0.01 to 8 wt. %, 0.05 to 6 wt. %, 0.1 to 5 wt. %, 0.1 to 2.5 wt. %, or 0.1 to 1.0 wt. % of the copolymer.
The preparation of copolyesters is well known in the art, such as disclosed in U.S. Pat. No. 2,012,267. Such reactions are typically operated at temperatures from 150 to 300° C. in the presence of polycondensation catalysts such as titanium isopropoxide, manganese diacetate, antimony oxide, dibutyl tin diacetate, zinc chloride, or combinations thereof. The amount of catalyst to obtain an acceptable depolymerization/oligomerization rate at the desired temperatures will vary, and can be determined by experimentation. The catalysts are typically employed in amounts from 10 to 5000, or 10 to 1000 parts per million (ppm), based on total weight of the reactants. In an embodiment, the catalyst is a tetraisopropyl titanate, available from DuPont under the tradename TYZOR.
The poly(butylene-co-adipate terephthalate) oligomers are treated with a quencher prior to reaction with the chain extender, or at the same time that the chain extender is added to the oligomers. The quencher may be a phosphorus-containing compound, a nitrogen-containing compound or a boron-containing compound, or a combination thereof.
Phosphorus-containing compounds include phosphoric acid, poly(phosphoric acid), phosphorous acid, monobutyl phosphate, dibutyl phosphate, monoalkyl phosphates, dialkyl phosphates, and combinations thereof.
Nitrogen-containing compounds include alkyl amines, aromatic amines, alkyl aromatic amines, alkanol amines, ammonium compounds, and combinations thereof.
Boron-containing compounds include boric acid, boron alkoxides, boric oxides, boron halides, metaborates, monoalkyl borates, dialkyl borates, trialkyl borates, borazines, and combinations thereof.
Generally, the quencher is selected from phosphoric acid, phosphorous acid, boric acid, and combinations thereof. In an embodiment of the method, the quencher is added at from 0.05 to 1 mole % based upon total moles of poly(butylene terephthalate-co-adipate) copolymer. In an embodiment, the copolymer contains 0.05 to 1 mol % of the quencher residue, based on poly(butylene terephthalate-co-adipate) copolymer.
The poly(butylene-co-adipate terephthalate) copolymer is produced by reacting poly(butylene-co-adipate terephthalate) oligomer with a chain extender. In an embodiment, the chain extender is selected from mononuclear isocyanate, binuclear isocyanate, trinuclear isocyanate, tetra or higher nuclear isocyanate and their mixtures, diisocyanate selected from the group consisting of tolylene 2,4-diisocyanate, tolylene 2,6-diisocyanate, 2,4′-diphenylmethane diisocyanate, naphthylene-1,5-diisocyanate, xylylene diisocyanate, hexamethylene diisocyanate, isophorone diisocyanate, and methylenebis (2-isocyanatocyclohexane).
In an embodiment, the chain extender is a combination comprising, based on the total weight of the combination, from 45 to 80 wt. % of a chain extender selected from a mononuclear isocyanurate, a chain extender containing two functional groups that react with an end group of the oligomer, or combinations thereof; from 13 to 25 wt. % of a chain extender selected from a binuclear isocyanurate, a chain extender containing three functional groups that react with an end group of the oligomer, and combinations thereof; from 5 to 12 wt. % of a chain extender selected from a trinuclear isocyanurate, a chain extender containing four functional groups that react with an end group of the oligomer, and combinations thereof; and from 2 to 18 wt. % a tetra- or higher-nuclear isocyanurate.
In an embodiment of the method, the chain extender can be present from 0.05 to 5 weight percent based upon the total weight of the poly(butylene terephthalate-co-adipate) oligomers. In an embodiment of the poly(butylene terephthalate-co-adipate) copolymer, the chain extender residue can be present from 0.05 to 5 weight % based on total weight of poly(butylene terephthalate-co-adipate) copolymer. In another embodiment the amount of chain extender can be present from 0.1 to 1 weight %.
Conditions for reacting the oligomers with the chain extender are known in the art, and will depend on the specific reactants, their amounts, and desired reaction time. For example, the chain extension can be conducted in the melt, for example at 100 to 125° C. at atmospheric or reduced pressure, optionally under an inert atmosphere.
The poly(butylene terephthalate-co-adipate) copolymers have an advantageous combination of properties. For example, the copolymers can have a melt temperature of 105 to 125° C., 110 to 125°, 100 to 120° C., 100 to 115° C., or 100 to 110° C. The copolymers can have a Tg of −30 to −10° C., −25 to −10° C., or −20 to −10° C.
The copolymers can further be manufactured to have a desired number average molecular weight, for example greater than 30,000 g/mole, 30,000 to 300,000 g/mole, 40,000 to 200,000 g/mole, or 45,000 to 150,000 g/mole.
In addition, the copolymers can have an I.V. of greater than 1.0, greater than 1.2, greater than 1.5 deciliter per minute (dL/minute) as measured in a 60:40 by weight phenol/1,1,2,2-tetrachloroethane mixture at 23° C.
The poly(butylene terephthalate-co-adipate) copolymers have an advantageous combination of properties. For example, the copolymers can have a melt temperature of 100 to 125° C., 110 to 125°, 100 to 120° C., 100 to 115° C., or 100 to 110° C. The copolymers can have a Tg of −30 to −10° C., −25 to −10° C., or −20 to −10° C.
Specifically the copolymer has a melt temperature of 100 to 125° C.; a number average molecular weight of at least 30,000 g/mole; an intrinsic of viscosity (I.V.) of at least 1.0 dL/minute; and a Tg of −30 to −10° C., and the copolymer comprises a residue derived from the polyester residue component. The manufacturing conditions can be adjusted to achieve the desired combination of properties. For example, the copolymers can have a melt temperature of 100 to 115° C.; a number average molecular weight of 40,000 to 200,000 g/mole; an intrinsic of viscosity (I.V.) of at least 1.2 dL/minute; and a Tg of −25 to −10° C. Other combinations of properties within these ranges are possible.
The composition of the invention includes, in addition to the copolyester, other components combined with the copolyester, for example other polymers and additives, used in the formulation of molding compositions. Examples of the polymers include aliphatic polyesters, aromatic polycarbonates, aliphatic polycarbonates, starches, aromatic polyesters, cycloaliphatic polyesters, polyesteramides, combinations thereof and the like. The polymers can be wholly or partially bio-derived, including petroleum-derived aromatic polyesters and bio-derived aromatic polyesters. In the art, chain extenders such as epoxides, bisoxazolines, biscaprolactams, dianhydrides, and the like have been reported for use in polyesters. Among these, epoxides are most widely used on a commercial scale due to their relatively low cost and availability of a variety of structures.
In a specific embodiment the copolyester is combined with an aliphatic polyester, for example poly(lactic acid), poly(hydroxyalkanoate), poly(butylene succinate), poly(butylene adipate), poly(butylene succinate adipate) and poly(caprolactone), or a combination thereof. Polyhydroxyalkanoates (PHAs) are linear polyesters produced in nature by bacterial fermentation of sugar or lipids, and include, for example, poly(R-3-hydroxybutyrate) (PHB or poly(3HB)).
In another specific embodiment the copolyester is combined with an aromatic polyester, for example a poly(trimethylene terephthalate) derived from petroleum-derived 1,3-propanediol, poly(trimethylene terephthalate) derived from bio-derived 1,3-propanediol, poly(butylene terephthalate) derived from petroleum-derived 1,4-butanediol, poly(butylene terephthalate) derived from bio-derived 1,4-butanediol, poly(trimethylene terephthalate) derived from post-consumer poly(ethylene terephthalate), poly(butylene terephthalate) derived from post-consumer poly(ethylene terephthalate), virgin poly(ethylene terephthalate), recycled poly(ethylene terephthalate), post-consumer poly(ethylene terephthalate), recycled poly(trimethylene terephthalate), recycled copolyesters of terephthalic acid with ethylene glycol and cyclohexane dimethanol, or a combination thereof.
The amounts of the copolyesters and the additives can vary depending on the desired properties of the biodegradable composition. In an embodiment the additives are present in an amount from 2 to 90 wt. %, for example from 2 to 40 wt. % or from 40 to 90 wt. %, based on the total weight of the composition. When the copolyester is used with starch, the amount of starch can range from 40 to 90 wt. %, and the amount of polyester can range from 10 to 60%, based on the total weight of the total composition. When the copolyester is used in conjunction with polylactic acid, the amount of the copolyester can range from 40 to 90 wt. % and the amount of polylactic acid can range from 10 to 60 wt. %, specifically 40 to 60%, based on the total weight of the composition.
The composition can also contain from 0.01 to 45 wt. %, based on the total weight of the composition, of an additive selected from alcohols, acetates, alcohol-acetate copolymers, and combinations thereof. Additionally, the composition can contain from 0.01 to 2 wt. %, based on the weight of the composition, of an additive selected from crosslinkers, anti-aging agents, retrogradation agents, anti-blocking agents, water, odor-controlling agents, and combinations thereof.
Additives ordinarily incorporated into polymer compositions can be used, with the proviso that the additives are selected so as to not significantly adversely affect the desired properties of the composition, for example, biodegradability, impact, flexural strength, color, and the like. Such additives can be mixed at a suitable time during the mixing of the components for forming the composition. Possible additives include impact modifiers, fillers, reinforcing agents, anti-oxidants, heat stabilizers, light stabilizers, ultraviolet light (UV) absorbers, plasticizers, lubricants, mold release agents, antistatic agents, colorants, blowing agents, flame retardants, anti-drip agents, and radiation stabilizers. Combinations of additives can be used, for example an antioxidant, a UV absorber, and a mold release agent. The total amount of additives (other than any impact modifier, filler, or reinforcing agents) is generally 0.01 to 5 wt. %, based on the total weight of the composition. In a specific embodiment, from 0.01 to 5.00 wt. % of a nucleating agent, antioxidant, UV stabilizer, plasticizers, epoxy compound, melt strength additive, or a combination thereof is used.
Advantageously, the copolyester and compositions containing the copolyester can be biodegradable. This means that the copolyester and compositions containing the copolyester exhibit aerobic biodegradability, as determined by ISO 14855-1:2005. ISO 14855-1:2005, as is known, specifies a method for the determination of the ultimate aerobic biodegradability of plastics, based on organic compounds, under controlled composting conditions by measurement of the amount of carbon dioxide evolved and the degree of disintegration of the plastic at the end of the test. This method is designed to simulate typical aerobic composting conditions for the organic fraction of solid mixed municipal waste. The test material is exposed to an inoculum, which is derived from compost. The composting takes place in an environment wherein temperature, aeration and humidity are closely monitored and controlled. The test method is designed to yield the percentage conversion of the carbon in the test material to evolved carbon dioxide as well as the rate of conversion. Also specified is a variant of the method, using a mineral bed (vermiculite) inoculated with thermophilic microorganisms obtained from compost with a specific activation phase, instead of mature compost. This variant is designed to yield the percentage of carbon in the test substance converted to carbon dioxide and the rate of conversion. Generally, our copolyesters (and compositions containing copolyesters) exhibit a biodegradation (measured in % of solid carbon of the test item that is converted into gaseous, mineral C in the form of CO2), which is at least 30% after 75 days. In an embodiment, the copolyesters (and compositions containing copolyesters) exhibit a biodegradation, which is at least 40% or 50% after 75 days. The biodegradation of the copolyesters (and compositions containing copolyesters) can range from at least 30% to 50%, or at least 30% to 60%, or at least 30% to 70%.
Advantageously, useful articles can be made from the copolyester and compositions containing the copolyester. In a specific embodiment, an article is extruded, calendared, extrusion molded, blow molded, solvent cast or injection molded from the copolymer or the composition containing the copolymer. The article can be a film or a sheet. When the article is a film, the article can be formed by extrusion molding or calendaring the copolyester or composition containing the copolyester. The copolyesters and compositions containing the copolyesters are useful for films, for example film packaging applications, among other applications.
As stated above, various combinations of the foregoing embodiments can be used. The invention is further described in the following illustrative examples in which all parts and percentages are by weight unless otherwise indicated.
EXAMPLES
Materials
Following is a list of materials, acronyms, and selected sources used in the examples.

    ADA: Adipic Acid (from INVISTA)
    BDO: 1,4-Butanediol (from BASF, with a purity specification of 99.5 wt. %)
    DMI: Dimethyl Isophthalate
    DSC: Differential Scanning calorimetry
    EI: Ester Interchange
    Hexamethylene diisocyanate (from Acros, grade/purity 99%)
    Phosphoric Acid: Phosphoric Acid (from Acros, grade/purity 98%)
    TPT: Tetraisopropyl titanate (from DuPont, commercial Tyzor grade)
    PBAT: Poly(butylene terephthalate-co-adipate)
    Recycle DMT: Dimethyl terephthalate obtained via methanolysis of post-consumer PET
    Post consumer PET: Polyethylene terephthalate obtained from Futura.

Methods and Procedures



The reported L*, a*, b* values were obtained through the diffuse reflectance method acquired on a Gretag Macbeth Color-Eye 7000A with D65 illumination. The term “white,” as used in this application, means that the material being described as white exhibits an L* value that is at least 75, or at least 80, or at least 85 with a corresponding set of “a” and “b” values that are substantially close to 0, (less than 5 units on the CIE color scale), where the “a” represents red and green hues and “b” represents blue and yellow hues of the white material on the CIE LAB color scale. The L* value can range from 75, or 80, or 85 to 100. The “L*, a, b” method for describing colors is well known and developed by the CIE (Commission Internationale de l'Eclairage). The CIE provides recommendations for colorimetry by specifying the illuminants, the observer, and the methodology used to derive values for describing color. In this system, 3 coordinates are utilized to locate a color in a color space which is represented by L*, a* and b*. When a color is expressed in CIELAB, L* defines lightness, if a value is closer to 0 it means total absorption or how dark a color is. If the L* value is closer to 100 it means total reflection or how light a color is. The a* value denotes how green or red a color is, whereas the b* value represents how blue or yellow a color is.
IV: Intrinsic Viscosity, (IV) of the polymer was measured using an automatic Viscotek Microlab® 500 series Relative Viscometer Y501. In a typical procedure, 0.5000 g of polymer sample was fully dissolved in a 60/40 mixture (by vol) of % phenol/1,1,2,2-tetrachloroethane solution (Harrell Industries). Two measurements were taken for each sample, and the result reported was the average of the two measurements.
Dynamic scanning calorimetry (DSC), Perkin Elmer DSC 7 equipped with Pyris DSC 7 software, was used to determine melting characteristics of the polymers synthesized as well as the thermal properties of the corresponding monomers. In a typical procedure, a polymer sample (10-20 mg) was heated from −50° C. to 200° C. (20° C./min), held at 200° C. for 1 min, cooled back to −50° C. (20° C./min), then held at −50° C. for 1 min, and the above heating/cooling cycle was repeated. The second heating cycle is usually used to obtain the Tg and Tm data.
Example 1
The purpose of Example 1 was to prepare the copolyester PBAT by reacting recycle DMT with adipic acid (ADA), and 1,4-butanediol (BDO) using phosphoric acid as a catalyst quencher and hexamethylene diisocyanate as a chain extender. The materials, amounts, and reaction conditions are shown in Table 1.







TABLE 1







Materials and Conditions for Example 1.

















Scale of
Recycled

Phosphoric
Catalyst
EI
EI
Poly
Poly


Ex.
Reaction
DMT:BDO
ADA:BDO
Acid
Amount
Temp.
Time
Temp.
Time


No.
(g)
(mol/mol)
(mol/mol)
(ppm)
(ppm)
(° C.)
(min)
(° C.)
(min)





1
143
0.39
0.39
250
250
220
120
240
15









Techniques and Procedures

First, 50 grams of BDO and 36.5 grams of ADA were introduced into a three neck round bottom flask. The reactor was placed in an oil bath the temperature of which was adjusted to 175° C. Then, 250 ppm of TPT was added to the reactor under inert atmosphere. The ester interchange temperature was increased to 220° C. at a rate of 2° C./min while stirring at 260 rpm under nitrogen. After the evolution of water ceased, excess butanediol was distilled out under reduced pressure. Then, 48.6 grams of recycled DMT obtained through the methanolysis of post consumer PET and 50 grams of BDO were introduced into the reactor while stirring at 220° C. The mixture was heated over the course of 2 hours. Then, 0.5 ml of phosphoric acid solution in water (0.1 g/ml) was added. The temperature of the reaction mixture was increased to 240° C. The vacuum was reduced to below 1 torr. After achieving the desired oligomers, the vacuum was stopped and 0.7 ml of hexamethylene diisocyanate was added into the reactor. The melt was mixed with hexamethylene diisocyanate for 15 minutes under nitrogen atmosphere. After achieving the desired intrinsic viscosity, the reaction was stopped.
Results
Table 2 shows the glass transition temperature (Tg), melting temperature (Tm) (obtained from DSC), molecular weight data (obtained from gel permeation chromatography (GPC) using polystyrene standards), intrinsic viscosity (I.V.), and color obtained from visual observation of Example 1.







TABLE 2







Results for Example 1

















IV










Ex.
(dL/
Tm
Tg








No.
min)
(° C.)
(° C.)
PDI
Mn
Mw
L*
a*
b*





1
1.89
98
−23
7.0
40000
280000
79.0
0.5
8.2









Table 3 describes the compositional analysis of Example 1 obtained through proton NMR. The number reported therefore reflects the degree of incorporation of the named unit in the polymer.







TABLE 3







Compositional analysis result of Example 1












Ex.
Isophthalic
Terephthalic
ADA
BDO
EG


No.
Acid (mol %)
acid (mol %)
(mol %)
(mol %)
(mol %)





1
0.6
25.0
24.6
42.1
7.8









Discussion

A novel approach was used to prepare PBAT copolyesters from recycle DMT obtained through the methanolysis of the post-consumer PET. This approach includes first the preparation of the oligomers of PBAT made through the melt condensation of ADA, BDO, and recycle DMT in the presence of phosphoric acid catalyst quencher. The resulting oligomers exhibited white color due to lower reaction temperature and successful quenching of catalyst. Then the oligomers were chain extended using hexamethylene diisocyanate at the same temperature and atmospheric pressure. A sharp viscosity increase was observed within 15 minutes indicating that chain extension through hexamethylene diisocyanate is rapid and quantitative.
The results shown in Table 2 demonstrate that the current process enabled the co-polyester to obtain a very high IV. The melting temperature of Example 1 is 17° C. lower compared to a commercial PBT-co-adipate (Tm=117° C.) obtained from printed BASF data sheet.
The resulting copolyester includes isophthalic acid and EG in its backbone, which stems from the post consumer PET. The mole percent of EG in the backbone is high compared to previous processes due to lack of vacuum during the chain extension process.
Examples 2-8
The purpose of Examples 2-5 was to determine the effect of ethylene glycol (EG) and isophthalic impurities on the final melting temperature of the PBAT prepared by isocyanate chain extension. The materials, amounts, and reaction conditions are shown in Table 4.







TABLE 4







Materials and Conditions for Examples 2-5.















BDO:(PET +
Phosphoric
Catalyst
EI
EI
Poly
Poly


Ex.
ADA)
Acid:TPT
Amount
Temp.
Time
Temp.
Time


No.
(mol:mol)
(mol/mol)
(ppm)
(° C.)
(min)
(° C.)
(min)





2
0
1:1
250
220
200
250
80


3
1.1:1  
1:1
250
220
236
250
86


4
3:1
1:1
250
220
251
250
90


5
6:1
1:1
250
220
251
250
94









The purpose of Examples 6-8 was to determine the effect of isophthalic impurities on the final melting temperature of PBAT by isocyanate chain extension. The materials, amounts, and reaction conditions are shown in Table 5.







TABLE 5







Materials and Conditions for Examples 6-8.






















Phosphoric
Catalyst


Poly
Poly


Ex.
DMT
ADA
DMI
BDO
Acid:TPT
Amount
EI Temp.
EI Time
Temp.
Time


No.
(mol)
(mol)
(mol)
(mol)
(mol/mol)
(ppm)
(° C.)
(min)
(° C.)
(min)




















6
0.248
0.25
0.002
0.50
1:1
250
220
200
250
80


7
0.245
0.25
0.005
0.50
1:1
250
220
236
250
86


8
0.24
0.25
0.01
0.50
1:1
250
220
251
250
90









Techniques and Procedures
Example 2
First, 50 grams of BDO and 36.5 grams of ADA were introduced into a three neck round bottom flask. The reactor was placed in an oil bath the temperature of which was adjusted to 175° C. Then, 250 ppm of TPT was added to the reactor under inert atmosphere. The ester interchange temperature was increased to 220° C. at a rate of 2° C./min while stirring at 260 rpm under nitrogen. After the evolution of water ceased, excess butanediol was distilled out under reduced pressure. Then, 48.5 grams of DMT and 65 grams of BDO were introduced into the reactor while stirring at 220° C. The mixture was heated over the course of 2 hours. Then, 0.5 ml of phosphoric acid solution in water (0.1 g/ml) was added. The temperature of the reaction mixture was increased to 240° C. The vacuum was reduced to below 1 torr. After achieving the desired oligomers, as indicated by time (30 minutes), the vacuum was stopped and 0.7 ml of hexamethylene diisocyanate was added into the reactor. The melt was mixed with hexamethylene diisocyanate for 15 minutes under nitrogen atmosphere. After achieving the desired intrinsic viscosity, the reaction was stopped.
Example 3
First, 50 grams of BDO and 36.5 grams of ADA were introduced into a three neck round bottom flask. The reactor was placed in an oil bath the temperature of which was adjusted to 175° C. Then, 250 ppm of TPT was added to the reactor under inert atmosphere. The ester interchange temperature was increased to 220° C. at a rate of 2° C./min while stirring at 260 rpm under nitrogen. After the evolution of water ceased, excess butanediol was distilled out under reduced pressure. Then, 48 grams of post consumer PET and 50 grams of BDO were introduced into the reactor while stirring at 220° C. The mixture was heated over the course of 2 hours. Then, 0.5 ml of phosphoric acid solution in water (0.1 g/ml) was added. The temperature of the reaction mixture was increased to 240° C. The vacuum was reduced to below 1 torr. After achieving desired oligomers, as indicated by time (30 minutes), the vacuum was stopped and 0.7 ml of hexamethylene diisocyanate was added into the reactor. The melt was mixed with hexamethylene diisocyanate for 15 minutes under nitrogen atmosphere. After achieving the desired intrinsic viscosity as indicated by the torque of the stirrer, the reaction was stopped.
Example 4
First, 50 grams of BDO and 36.5 grams of ADA were introduced into a three neck round bottom flask. The reactor was placed in an oil bath the temperature of which was adjusted to 175° C. Then, 250 ppm of TPT was added to the reactor under inert atmosphere. The ester interchange temperature was increased to 220° C. at a rate of 2° C./min while stirring at 260 rpm under nitrogen. After the evolution of water ceased, excess butanediol was distilled out under reduced pressure. Then, 48 grams of post consumer PET and 135 grams of BDO were introduced into the reactor while stirring at 220° C. The mixture was heated over the course of 2 hours. Then, 0.5 ml of phosphoric acid solution in water (0.1 g/ml) was added. The temperature of the reaction mixture was increased to 240° C. The vacuum was reduced to below 1 torr. After achieving desired oligomers, as indicated by time (30 minutes) the vacuum was stopped and 0.7 ml of hexamethylene diisocyanate was added into the reactor. The melt was mixed with hexamethylene diisocyanate for 15 minutes under nitrogen atmosphere. After achieving the desired intrinsic viscosity, as indicated by the torque of the stirrer, the reaction was stopped.
Example 5
First, 50 grams of BDO and 36.5 grams of ADA were introduced into a three neck round bottom flask. The reactor was placed in an oil bath the temperature of which was adjusted to 175° C. 250 ppm of TPT was added to the reactor under inert atmosphere. The ester interchange temperature was increased to 220° C. at a rate of 2° C./min while stirring at 260 rpm under nitrogen. After the evolution of water ceased, excess butanediol was distilled out under reduced pressure. Then, 48 grams of post consumer PET and 270 grams of BDO were introduced into the reactor while stirring at 220° C. The mixture was heated over the course of 2 hours. Then, 0.5 ml of phosphoric acid solution in water (0.1 g/ml) was added. The temperature of the reaction mixture was increased to 240° C. The vacuum was reduced to below 1 torr. After achieving desired oligomers, the vacuum was stopped and 0.7 ml of hexamethylene diisocyanate was added into the reactor. The melt was mixed with hexamethylene diisocyanate for 15 minutes under nitrogen atmosphere. After achieving the desired intrinsic viscosity, the reaction was stopped.
Example 6
First, 50 grams of BDO and 36.5 grams of ADA were introduced into a three neck round bottom flask. The reactor was placed in an oil bath the temperature of which was adjusted to 175° C. Then, 250 ppm of TPT was added to the reactor under inert atmosphere. The ester interchange temperature was increased to 220° C. at a rate of 2° C./min while stirring at 260 rpm under nitrogen. After the evolution of water ceased, excess butanediol was distilled out under reduced pressure. Then, 48.1 grams of DMT, 0.39 grams of DMI and 65 grams of BDO were introduced into the reactor while stirring at 220° C. The mixture was heated over the course of 2 hours. Then, 0.5 ml of phosphoric acid solution in water (0.1 g/ml) was added. The temperature of the reaction mixture was increased to 240° C. The vacuum was reduced to below 1 torr. After achieving desired oligomers, the vacuum was stopped and 0.7 ml of hexamethylene diisocyanate was added into the reactor. The melt was mixed with hexamethylene diisocyanate for 15 minutes under nitrogen atmosphere. After achieving the desired intrinsic viscosity, the reaction was stopped.
Example 7
First, 50 grams of BDO and 36.5 grams of ADA were introduced into a three neck round bottom flask. The reactor was placed in an oil bath the temperature of which was adjusted to 175° C. Then, 250 ppm of TPT was added to the reactor under inert atmosphere. The ester interchange temperature was increased to 220° C. at a rate of 2° C./min while stirring at 260 rpm under nitrogen. After the evolution of water ceased, excess butanediol was distilled out under reduced pressure. Then, 47.53 grams of DMT, 0. ° C. The mixture was heated over the course of 2 hours. Then, 0.5 ml of phosphoric acid solution in water (0.1 g/ml) was added. The temperature of the reaction mixture was increased to 240° C. The vacuum was reduced to below 1 torr. After achieving desired oligomers, the vacuum was stopped and 0.7 ml of hexamethylene diisocyanate was added into the reactor. The melt was mixed with hexamethylene diisocyanate for 15 minutes under nitrogen atmosphere. After achieving the desired intrinsic viscosity, the reaction was stopped.
Examples 8
First, 50 grams of BDO and 36.5 grams of ADA were introduced into a three neck round bottom flask. The reactor was placed in an oil bath the temperature of which was adjusted to 175° C. Then, 250 ppm of TPT was added to the reactor under inert atmosphere. The ester interchange temperature was increased to 220° C. at a rate of 2° C./min while stirring at 260 rpm under nitrogen. After the evolution of water ceased, excess butanediol was distilled out under reduced pressure. Then, 46.56 grams of DMT, 1.94 grams of DMI and 65 grams of BDO were introduced into the reactor while stirring at 220° C. The mixture was heated over the course of 2 hours. Then, 0.5 ml of phosphoric acid solution in water (0.1 g/ml) was added. The temperature of the reaction mixture was increased to 240° C. The vacuum was reduced to below 1 torr. After achieving desired oligomers, the vacuum was stopped and 0.7 ml of hexamethylene diisocyanate was added into the reactor. The melt was mixed with hexamethylene diisocyanate for 15 minutes under nitrogen atmosphere. After achieving the desired intrinsic viscosity, the reaction was stopped.
Results
Table 6 shows the melting temperature (Tm) (obtained from DSC), and chemical compositions of Examples 2-5.







TABLE 6







Impurity content and melting temperature for Examples 2-5.













Ex.
Terephthalic
Isophthalic
ADA
EG
BDO
Tm


No.
(%)
(%)
(%)
(%)
(%)
(° C.)
















2
25.0
0
25.0
0
50.0
125


3
25.4
0.6
24.5
4.6
44.9
110


4
24.9
0.7
24.9
7.6
41.9
101


5
25.0
0.6
24.8
14.8
34.8
75









Table 7 shows the melting temperature (Tm) (obtained from DSC), and chemical compositions of Examples 6-8.







TABLE 7







Impurity content and melting temperature for Examples 6-8.












Ex.
Terephthalic
Isophthalic
ADA
BDO
Tm


No.
(%)
(%)
(%)
(%)
(° C.)















6
25.8
0.2
25.0
49.0
123


7
25.7
0.5
246
49.3
121


8
25.7
1.1
25.0
49.5
119









FIG. 1 shows the effect of the impurities on the melting temperature of the examples prepared in the presence of the chain extender. The red circles show the effect of DMI incorporation in the backbone of the polymer chain on the melting temperature of the polymer in examples 6, 7 and 8. The black line shows the transfer function, which explains the linear correlation of DMI impurities with the melting temperature of the polymer. The blue triangles show that the melting temperature of the polymer decreases in the presence of increased combined amounts of DMI and EG impurities in examples 2, 3, 4, and 5. The good fit of these data points to the blue straight line graph indicates strong linear correlation of this inverse relationship between the melting temperature and total mol percent of EG and DMI impurities to the graphed function, with an R square value of 0.9942. The thermal properties of the polymers prepared from recycled DMT (pink triangle) and recycled PET (green circle) with a given impurity level fit very well to the transfer function given as a blue line.
Discussion
Examples 2-8 show the effect of the impurities on the final melting temperature of PBAT prepared through a chain extension process. The melting temperature of PBAT decreases in a linear fashion as the content of indicated comonomer impurities within the backbone increases (FIG. 1, Table 4 and 5). Samples prepared from recycle DMT correlates with the blue curve (FIG. 1). The PBAT prepared with this process and including total impurities level less than 2 mol % shows similar thermal properties compared to a commercial PBAT (Trade name Ecoflex, BASF).
All references cited herein are incorporated by reference in their entirety. While typical embodiments have been set forth for the purpose of illustration, the foregoing descriptions should not be deemed to be a limitation on the scope herein. Accordingly, various modifications, adaptations, and alternatives can occur to one skilled in the art without departing from the spirit and scope herein.

## Claims

1. A method for the manufacture of a poly(butylene terephthalate-co-adipate) copolymer, the method comprising:
(a) polymerizing 1,4-butanediol and an acid component comprising, based on the total acid component,
(1) from 20 to 95 mol % of an adipic acid component selected from the group consisting of adipic acid, an ester-forming derivative of adipic acid, and combinations thereof, and
(2) from 5 to 80 mol % of an aromatic dicarboxy compound, derived from a terephthalic-containing polymer, selected from the group consisting of an aromatic dicarboxylic acid, an aromatic dicarboxylic (C1-3)alkyl ester, and a combination thereof; and

wherein polymerization occurs in the presence of a catalyst under conditions effective to form poly(butylene terephthalate-co-adipate) oligomers;
(b) adding a catalyst quencher selected from the group consisting of a phosphorus-containing compound, a nitrogen containing compound, a boron-containing compound, and combination thereof; and
(c) reacting the quenched poly(butylene terephthalate-co-adipate) oligomers with from 0.05 to 5 weight %, based on total weight of poly(butylene terephthalate-co-adipate) oligomer, of a chain extender selected from the group consisting of isocyanurate, polyisocyanate, isocyanate and combinations thereof, to form the poly(butylene terephthalate-co-adipate) copolymer, wherein the copolymer has:
a melt temperature of 100 to 125° C.,
a number average molecular weight of at least 40,000 to 200,000 g/mole,
an intrinsic viscosity of at least 1.2 deciliter per minute, and
a Tg of −25 to −10° C.;
wherein the poly(butylene terephthalate-co-adipate) copolymer exhibits an L* value of at least 75.

2. The method of claim 1, comprising adding from 0.05 to 1 mole % of the catalyst quencher, based on total moles of poly(butylene terephthalate-co-adipate) copolymer.

3. The method of claim 1, wherein the catalyst quencher is selected from phosphoric acid, phosphorous acid, boric acid, nitrogen containing compound, and combinations thereof.

4. The method of claim 1, wherein the copolymer comprises less than 10 mole % of a combination of ethylene glycol groups and isophthalate groups, based upon poly(butylene terephthalate-co-adipate) copolymer.

5. The method of claim 1, wherein the chain extender is selected from the group consisting of mononuclear isocyanate, binuclear isocyanate, trinuclear isocyanate, tetra or higher nuclear isocyanate and their mixtures, diisocyanate selected from the group consisting of tolylene 2,4-diisocyanate, tolylene 2,6-diisocyanate, 2,4′-diphenylmethane diisocyanate, naphthylene-1,5-diisocyanate, xylylene diisocyanate, hexamethylene diisocyanate, isophorone diisocyanate, and methylenebis (2-isocyanatocyclohexane), and combinations thereof.

6. The method of claim 1, wherein the chain extender is a combination comprising, based on the total weight of the combination,
from 45 to 80 wt. % of a chain extender selected from the group consisting of a mononuclear isocyanurate, a chain extender containing two functional groups that react with an end group of the oligomer, and combinations thereof;
from 13 to 25 wt. % of a chain extender selected from the group consisting of a binuclear isocyanurate, a chain extender containing three functional groups that react with an end group of the oligomer, and combinations thereof;
from 5 to 12 wt. % of a chain extender selected from the group consisting of a trinuclear isocyanurate, a chain extender containing four functional groups that react with an end group of the oligomer, and combinations thereof; and
from 2 to 18 wt. % a tetra- or higher-nuclear isocyanurate.

7. A method for the manufacture of a poly(butylene terephthalate-co-adipate) copolymer, the method comprising:
(a) polymerizing 1,4-butanediol and an acid component comprising, based on the total acid component,
(1) from 20 to 95 mol % of an adipic acid component selected from the group consisting of adipic acid, an ester-forming derivative of adipic acid, and combinations thereof, and
(2) from 5 to 80 mol % of an aromatic dicarboxy compound derived from polyethylene terephthalate selected from the group consisting of an aromatic dicarboxylic acid, an aromatic dicarboxylic (C1-3)alkyl ester, and a combination thereof;
wherein a polyester component residue is present that is derived from the polyethylene terephthalate; and
wherein polymerization occurs in the presence of a titanium catalyst under conditions effective to form poly(butylene terephthalate-co-adipate) oligomers;

(b) adding a catalyst quencher selected from the group consisting of a phosphorus-containing compound, a nitrogen containing compound, a boron-containing compound, and combination thereof; and
(c) reacting the quenched poly(butylene terephthalate-co-adipate) oligomers with from 0.05 to 5 weight %, based on total weight of poly(butylene terephthalate-co-adipate) oligomer, of a chain extender selected from the group consisting of isocyanurate, polyisocyanate, isocyanate and combinations thereof, to form the poly(butylene terephthalate-co-adipate) copolymer, wherein the copolymer has:
a melt temperature of 100 to 125° C.,
a number average molecular weight of at least 40,000 to 200,000 g/mole;
an intrinsic viscosity of at least 1.2 deciliter per minute, and
a Tg of −25 to −10° C.;
wherein the poly(butylene terephthalate-co-adipate) copolymer exhibits an L* value of at least 75.

8. The method of claim 7, wherein the quencher is selected from phosphoric acid or phosphorous acid.

9. The method of claim 7, wherein the quencher is boric acid.

10. The method of claim 8, wherein the residue is selected from the group consisting of ethylene glycol groups, diethylene glycol groups, cobalt-containing compounds, antimony-containing compounds, germanium-containing compounds, tin-containing compounds, aluminum, aluminum salts, and combinations thereof.