WO2014204296A1 - Semi-crystalline polyester - Google Patents

Semi-crystalline polyester Download PDF

Info

Publication number
WO2014204296A1
WO2014204296A1 PCT/NL2014/000019 NL2014000019W WO2014204296A1 WO 2014204296 A1 WO2014204296 A1 WO 2014204296A1 NL 2014000019 W NL2014000019 W NL 2014000019W WO 2014204296 A1 WO2014204296 A1 WO 2014204296A1
Authority
WO
WIPO (PCT)
Prior art keywords
residues
acid residues
semi
crystalline polyester
ester
Prior art date
Application number
PCT/NL2014/000019
Other languages
French (fr)
Inventor
Daniël STEPHAN VAN ES
Thiyagarajan SHANMUGAM
Johannes RUTGER IDSARD KNOOP
Original Assignee
Stichting Dutch Polymer Institute
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Stichting Dutch Polymer Institute filed Critical Stichting Dutch Polymer Institute
Publication of WO2014204296A1 publication Critical patent/WO2014204296A1/en

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08GMACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
    • C08G63/00Macromolecular compounds obtained by reactions forming a carboxylic ester link in the main chain of the macromolecule
    • C08G63/02Polyesters derived from hydroxycarboxylic acids or from polycarboxylic acids and polyhydroxy compounds
    • C08G63/12Polyesters derived from hydroxycarboxylic acids or from polycarboxylic acids and polyhydroxy compounds derived from polycarboxylic acids and polyhydroxy compounds
    • C08G63/16Dicarboxylic acids and dihydroxy compounds
    • C08G63/18Dicarboxylic acids and dihydroxy compounds the acids or hydroxy compounds containing carbocyclic rings
    • C08G63/181Acids containing aromatic rings
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08GMACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
    • C08G63/00Macromolecular compounds obtained by reactions forming a carboxylic ester link in the main chain of the macromolecule
    • C08G63/02Polyesters derived from hydroxycarboxylic acids or from polycarboxylic acids and polyhydroxy compounds
    • C08G63/60Polyesters derived from hydroxycarboxylic acids or from polycarboxylic acids and polyhydroxy compounds derived from the reaction of a mixture of hydroxy carboxylic acids, polycarboxylic acids and polyhydroxy compounds

Definitions

  • the invention relates to a semi-crystalline polyester, to a process for preparing such polyester and to a semi-crystalline polyester obtained by such method.
  • Diacids that are conventionally used in these plastics are usually derived from fossil feedstocks, such as terephthalic acid for the production of
  • PET and PBT poly(ethylene-terephthalate) and poly(butylene-terephthalate), usually referred to as PET and PBT, respectively. It is contemplated that the high performance of such plastics as engineering plastics amongst other relies on the high rigidity of the terephthalate residues. In the production of polyesters, many efforts have therefore been made to substitute the conventional terephthalates with rigid bio-based alternatives, with the aim to obtain materials having properties that are similar or improved compared to those of the materials of fossil origin.
  • a well-known bio-based substitute for terephthalic acid (ester) is 2,5- furandicarboxylic acid (ester), as is described in e.g. J. Renew. Mater., Vol 1 , No. 1 , January 2013, 61-72.
  • Polyesters comprising 2,5-furandicarboxylic acid residues, such as poly(ethylene-2,5-furandicarboxylate) (known as 2,5-PEF) and poly(butylene-2,5-furandicarboxylate) (known as 2,5-PBF) have been shown to be useful alternatives for conventional terephthalate-based polyesters.
  • 2,5-PEF poly(ethylene-2,5-furandicarboxylate)
  • 2,5-PBF poly(butylene-2,5-furandicarboxylate)
  • bio-based polyester may serve as an alternative to known polyesters.
  • Such an alternative may for example comprise bio-based residues that have an improved availability via biological pathways and/or that have improved material properties.
  • bio-based polyester that has a high thermal stability, more in particular one that is higher than that of known polyesters.
  • bio-based polyester that has no or a low colour.
  • the invention relates to a polyester comprising dicarboxylic acid residues and diol residues, wherein the dicarboxylic acid residues comprise 2,4 furandicarboxylic acid residues and wherein the diol residues comprise aliphatic diol residues.
  • a polyester of the invention is preferably a semi-crystalline polyester.
  • a dicarboxylic acid residue is meant a residue derived from a dicarboxylic acid.
  • a diol residue is meant a residue derived from a diol, and so on.
  • the invention relates to a polyester comprising residues derived from a dicarboxylic acid and residues derived from a diol, wherein the residues derived from a dicarboxylic acid comprise residues derived from 2,4-furandicarboxylic acid and wherein the residues derived from a diol comprise residues derived from an aliphatic diol.
  • dicarboxylic acid residue and diol residue are used, respectively.
  • the polyester typically comprises a chain comprising at least one segment wherein a 2,4-furandicarboxylic acid residue is linked to an aliphatic diol residue via an ester linkage.
  • a chain may for example comprise 100 or more, 500 or more, or 1000 or more of such ester linkages.
  • a chain may in particular consist of a plurality of alternating 2,4- furandicarboxylic acid residues and aliphatic diol residues.
  • the degree of polymerization of a chain of a polymer of the invention may be 100 or more, 500 or more, or 1000 or more.
  • a polyester of the invention may comprise other dicarboxylic acid residues than 2,4-furandicarboxylic acid residues.
  • the amount of 2,4- furandicarboxylic acid residues in the polyester may be 99 mol% or more, 95 mol% or more, 90 mol% or more, 80 mol% or more, 70
  • the 2,4-furandicarboxylic acid residues constitute 50 mol% or more of the total amount of dicarboxylic acid residues.
  • the dicarboxylic acid residues may - in addition to the 2,4-furandicarboxylic acid residues - thus comprise one or more further residues, for example residues selected from the group of 2,5-furandicarboxylic acid residues, 3,4-furandicarboxylic acid residues, 2,3-furandicarboxylic acid residues, terephthalic acid residues, isophthalic acid residues, phthalic acid residues, succinic acid residues and adipic acid residues.
  • the amount of further dicarboxylic acid residues may be 1 mol% or more, 5 mol% or more, 10 mol% or more, 20 mol% or more, 30 mol% or more or 40 mol% more.
  • a polyester of the invention may comprise one type of aliphatic diol residue, but may also comprise two or more different types of diol residues, at least one of which is an aliphatic diol residue. It may for example also comprise aromatic diol residues.
  • the amount of aliphatic diol residues may be at least 60 mol%, at least 70 mol%, at least 80 mol%, at least 90 mol% or at least 95 mol% of the total amount of diol residues.
  • the aliphatic diol residues constitute 50 mol% or more of the total amount of diol residues.
  • An aliphatic diol residue may in particular be selected from the group of ethylene glycol, 1 ,2-propandiol, 1 ,3-propanediol, 1 ,2-butanediol, 1 ,3- butanediol, 1 ,4-butanediol, 2,3-butanediol, 1 ,5-pentanediol, 1 ,4-pentanediol, 2,4-pentanediol 1 ,6-hexanediol, 1 ,5-hexanediol, 1 ,4-hexanediol, 2,5- hexanediol,3,4-hexanediol, cyclobutane-1 ,2-dimethanol, cyclobutane-1 ,3- dimethanol, cyclopentane- ,2-dimethanol, cyclopentane-1 ,3-
  • a polyester of the invention may further comprise monohydroxy monocarboxylic acid residues, such as alpha, beta or gamma hydroxy acids, more in particular monohydroxy monocarboxylic acid residues selected from the group of hydrobenzoic acids (including the ortho-, meta- and para- isomers), lactic acid, glycolic acid and gamma-hydroxybutyric acid.
  • the amount of monohydroxy monocarboxylic acid residues may be 1 mol% or more, 2 mol% or more, 5 mol% or more, 20 mol% or more or 35 mol% or more, relative to the total amount of residues in the polyester. Usually, up to 50 mol% of the total amount of residues are monohydroxy monocarboxylic acid residues.
  • An end-group of a chain of a polyester of the invention may be a carboxy group (connected to the furan moiety), a hydroxyl group, or an alkyl ester of a carboxy group (which carboxy group is connected to the furan ring).
  • the type of end-group depends on the applied stoichiometry of the
  • the average molar mass Mn of a polymer of the invention is usually 4.000 g/mol or more, 8.000 g/mol or more or 16.000 g/mol or more.
  • it is 20.000 g/mol or more.
  • micro-crystalline is meant a material which has a mixture of crystalline domains and amorphous domains.
  • the degree of crystallinity is usually between 1 % and 95% or between 2 and 90%.
  • the aliphatic diol residue is meant that the diol residue does not contain aromatic groups.
  • the aliphatic diol residue is in particular a residue wherein the two oxygen atoms (i.e. those originating from the diol hydroxyl groups but in the polyester being part of an ester group) are for example separated by a -(CH2)n- group, where n is 2 or more. They may also be separated by a -(CHR)2- group, where is R is a hydrocarbyl group, e.g. a methyl group or an ethyl group.
  • R 1 and R 2 may be different hydrocarbyl groups that are chosen independently from each other.
  • the link between the two oxygen atoms in the aliphatic diol residue is in particular selected from the group of -(CH2)2- (i.e. ethylene), -(CH2)3- (i.e. ,3-propylene), -(CH2>4- ⁇ i.e. ,4-butylene) and -(CHCH3HCH3CH)- (i.e. 2,3-butylene).
  • the diol from which the residue is derived is in these cases ethylene glycol, ,3-propylene glycol, 1 ,4-butylene glycol and 2,3- butylene glycol.
  • the melting point of a polyester according to the invention usually depends on the average molar mass Mn. Thus, by varying the Mn of polyesters of the invention, the melting point can be influenced. Usually, polyesters of the invention have a melting temperature of 160°or lower, 150°or lower, 140°or lower or 130°or lower.
  • a polyester according to the invention is usually opaque in its solid state.
  • the melting points of the polyesters of the invention are much lower than those of the 2,5-furandicarboxylic acid analogues.
  • the polyesters of the invention have a higher thermal stability than the corresponding polyesters derived from 2,5-furandicarboxylic acid (see Table 2).
  • the invention further relates to a process for preparing a polymer of the invention, comprising forming a mixture comprising
  • the mixture is exposed to elevated
  • temperatures e.g. up to 150 °C, up to 175 °C, up to 200 °C, up to 215 °C or up to 225 °C.
  • the best results are obtained when the temperature of the mixture is increased step-wise to up to 215 °C.
  • the molar ratio of 2,4-furandicarboxylic acid and/or an ester- forming derivative thereof to aliphatic diol and/or an ester-forming derivative thereof is in the range of 1 :1.5 to 1 :2.5.
  • the diol relative to the diacid.
  • the amount of 2,4-furandicarboxylic acid and/or an ester-forming derivative thereof and aliphatic diol and/or an ester-forming derivative thereof in the mixture may be at least 60 mol%, at least 70 mol%, at least 80 mol%, at least 90 mol% or at least 95 mol% of the monomers present in the mixture.
  • the 2,4-furandicarboxylic acid (ester) monomers and the aliphatic diol (ester) monomers together constitute 50 mol% or more of the total amount of monomers in the mixture.
  • the polyester obtained with a process of the invention is usually colourless. In the event that it is coloured, for example slightly yellow, it may easily be obtained as a colourless solid after purification. Purification may for example be performed by dissolving the polyester in a chlorinated solvent such as chloroform followed by precipitation in an alcohol such as methanol.
  • 2,4-furandicarboxylic acid monomer more susceptible to degradation and accompanying colouration, especially when it is exposed to elevated temperatures above 200 °C.
  • the polyester product appears to be colourless or almost colourless, which is an advantage for the application the polyester in bottles for e.g. soda.
  • the catalyst may be selected from the group of titanium
  • tetraalkoxides e.g. Ti(/-OPr) 4 , Ti(OEt) 4 , or Ti(OMe) 4 , Ti(/-OBu)4)
  • DBTO dibutyltinoxide
  • DBTL dibutyltinlaurate
  • stannous oxide stannous oxide
  • an ester-forming derivative of a diol or a carboxylic acid is meant a derivative that is capable of being transformed into an ester. This is also meant to include a monomeric ester from which a polyester is formed. In the latter case, a transesterification reaction takes place.
  • An ester-forming derivative of a diol may be an ester, for example an acetate ester.
  • An ester-forming derivative of a carboxylic acid may be its diacid chloride or its diester such as a dimethyl ester or a diethyl ester.
  • the invention further relates to a polymer obtainable by the process of the invention.
  • the polymerization method involves two stages. During the first stage, the reaction was carried out under nitrogen gas to form oligomers. The reaction mixture was heated in the silicone-oil bath at 115 °C for 15 min. After observing the complete melt of the mixtures, the catalyst Ti(OiPr) 4 (0.10 mmol) in 1 ml_ of toluene was added into the flask under the continuous flow of nitrogen gas. The temperature was now increased to 160 °C and stirred for 12 h, and finally to 200 - 215 °C for 1 -2 h to complete the first stage of pre- polymerisation reaction. The methanol and toluene were collected in the cooling flask.
  • the molar masses of the polymers were determined by GPC, using HFIP as solvent.
  • TGA samples were heated from 30 °C to 600 °C at a heating rate of 10 °C/min under a nitrogen flow of 60 mL/min.
  • the DSC measurement followed the standard heating and cooling rate of 10 °C/min. Not observed up to 230 °C.

Landscapes

  • Chemical & Material Sciences (AREA)
  • Health & Medical Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Medicinal Chemistry (AREA)
  • Polymers & Plastics (AREA)
  • Organic Chemistry (AREA)
  • Polyesters Or Polycarbonates (AREA)

Abstract

The invention relates to a semi-crystalline polyester comprising dicarboxyiic acid residues and diol residues, wherein the dicarboxyiic acid residues comprise 2,4-furandicarboxylic acid residues and wherein the diol residues comprise aliphatic diol residues. Such polyester may be prepared by polymerizing in the melt a mixture comprising (1) 2,4-furandicarboxylic acid and/or an ester-forming derivative thereof, (2) an aliphatic diol and/or an ester-forming derivative thereof, and (3) a catalyst.

Description

Semi-crystalline polyester
The invention relates to a semi-crystalline polyester, to a process for preparing such polyester and to a semi-crystalline polyester obtained by such method.
Now that raw materials of fossil origin become increasingly scarce and expensive, there is a strong desire for a structural transition from fossil- based feedstocks to sustainable, bio-based raw materials. An example is the use of bio-based monomers in engineering plastics such as polyesters.
Diacids that are conventionally used in these plastics are usually derived from fossil feedstocks, such as terephthalic acid for the production of
poly(ethylene-terephthalate) and poly(butylene-terephthalate), usually referred to as PET and PBT, respectively. It is contemplated that the high performance of such plastics as engineering plastics amongst other relies on the high rigidity of the terephthalate residues. In the production of polyesters, many efforts have therefore been made to substitute the conventional terephthalates with rigid bio-based alternatives, with the aim to obtain materials having properties that are similar or improved compared to those of the materials of fossil origin.
A well-known bio-based substitute for terephthalic acid (ester) is 2,5- furandicarboxylic acid (ester), as is described in e.g. J. Renew. Mater., Vol 1 , No. 1 , January 2013, 61-72. Polyesters comprising 2,5-furandicarboxylic acid residues, such as poly(ethylene-2,5-furandicarboxylate) (known as 2,5-PEF) and poly(butylene-2,5-furandicarboxylate) (known as 2,5-PBF) have been shown to be useful alternatives for conventional terephthalate-based polyesters. There remains however an increasing need for more bio-based diacids, which would enable the development of a greater variety of bio-based engineering plastics.
It is therefore an object of the present invention to provide a bio- based polyester that may serve as an alternative to known polyesters. Such an alternative may for example comprise bio-based residues that have an improved availability via biological pathways and/or that have improved material properties. It is in particular an object to provide a bio-based polyester that has a high thermal stability, more in particular one that is higher than that of known polyesters. It is a further object to provide a bio-based polyester that has no or a low colour.
It is also an object of the present invention to provide a process for preparing a bio-based polyester that is faster, less complicated and/or more energy-efficient than processes for bio-based polyesters known in the art.
Therefore, the invention relates to a polyester comprising dicarboxylic acid residues and diol residues, wherein the dicarboxylic acid residues comprise 2,4 furandicarboxylic acid residues and wherein the diol residues comprise aliphatic diol residues. A polyester of the invention is preferably a semi-crystalline polyester.
For the purpose of the invention, by a dicarboxylic acid residue is meant a residue derived from a dicarboxylic acid. Analogously, by a diol residue is meant a residue derived from a diol, and so on. Thus, in an alternative wording, the invention relates to a polyester comprising residues derived from a dicarboxylic acid and residues derived from a diol, wherein the residues derived from a dicarboxylic acid comprise residues derived from 2,4-furandicarboxylic acid and wherein the residues derived from a diol comprise residues derived from an aliphatic diol. For the sake of clarity and for the purpose of the present invention, however, the more concise wordings of dicarboxylic acid residue and diol residue are used, respectively.
The polyester typically comprises a chain comprising at least one segment wherein a 2,4-furandicarboxylic acid residue is linked to an aliphatic diol residue via an ester linkage. Usually, however, does such chain comprise a much higher amount of such ester linkages. A chain may for example comprise 100 or more, 500 or more, or 1000 or more of such ester linkages. A chain may in particular consist of a plurality of alternating 2,4- furandicarboxylic acid residues and aliphatic diol residues. The degree of polymerization of a chain of a polymer of the invention may be 100 or more, 500 or more, or 1000 or more.
A polyester of the invention may comprise other dicarboxylic acid residues than 2,4-furandicarboxylic acid residues. The amount of 2,4- furandicarboxylic acid residues in the polyester may be 99 mol% or more, 95 mol% or more, 90 mol% or more, 80 mol% or more, 70
mol% or more or 60 mol% or more of the total amount of dicarboxylic acid residues. Usually, the 2,4-furandicarboxylic acid residues constitute 50 mol% or more of the total amount of dicarboxylic acid residues. The dicarboxylic acid residues may - in addition to the 2,4-furandicarboxylic acid residues - thus comprise one or more further residues, for example residues selected from the group of 2,5-furandicarboxylic acid residues, 3,4-furandicarboxylic acid residues, 2,3-furandicarboxylic acid residues, terephthalic acid residues, isophthalic acid residues, phthalic acid residues, succinic acid residues and adipic acid residues. The amount of further dicarboxylic acid residues may be 1 mol% or more, 5 mol% or more, 10 mol% or more, 20 mol% or more, 30 mol% or more or 40 mol% more.
A polyester of the invention may comprise one type of aliphatic diol residue, but may also comprise two or more different types of diol residues, at least one of which is an aliphatic diol residue. It may for example also comprise aromatic diol residues. The amount of aliphatic diol residues may be at least 60 mol%, at least 70 mol%, at least 80 mol%, at least 90 mol% or at least 95 mol% of the total amount of diol residues. Usually, the aliphatic diol residues constitute 50 mol% or more of the total amount of diol residues.
An aliphatic diol residue may in particular be selected from the group of ethylene glycol, 1 ,2-propandiol, 1 ,3-propanediol, 1 ,2-butanediol, 1 ,3- butanediol, 1 ,4-butanediol, 2,3-butanediol, 1 ,5-pentanediol, 1 ,4-pentanediol, 2,4-pentanediol 1 ,6-hexanediol, 1 ,5-hexanediol, 1 ,4-hexanediol, 2,5- hexanediol,3,4-hexanediol, cyclobutane-1 ,2-dimethanol, cyclobutane-1 ,3- dimethanol, cyclopentane- ,2-dimethanol, cyclopentane-1 ,3-dimethanol, cyclohexane-1 ,2-dimethanol, cyclohexane-1 ,3-dimethanol, cyclohexane-1 ,4- dimethanol and 2,2 bis(4-hydroxycyclohexyl)propane.
A polyester of the invention may further comprise monohydroxy monocarboxylic acid residues, such as alpha, beta or gamma hydroxy acids, more in particular monohydroxy monocarboxylic acid residues selected from the group of hydrobenzoic acids (including the ortho-, meta- and para- isomers), lactic acid, glycolic acid and gamma-hydroxybutyric acid. The amount of monohydroxy monocarboxylic acid residues may be 1 mol% or more, 2 mol% or more, 5 mol% or more, 20 mol% or more or 35 mol% or more, relative to the total amount of residues in the polyester. Usually, up to 50 mol% of the total amount of residues are monohydroxy monocarboxylic acid residues.
An end-group of a chain of a polyester of the invention may be a carboxy group (connected to the furan moiety), a hydroxyl group, or an alkyl ester of a carboxy group (which carboxy group is connected to the furan ring). The type of end-group depends on the applied stoichiometry of the
polymerization reaction and on the functionalization of the terminal carboxy group of a terminal 2,4-furandicarboxylic acid residue.
The average molar mass Mn of a polymer of the invention is usually 4.000 g/mol or more, 8.000 g/mol or more or 16.000 g/mol or more.
Preferably, it is 20.000 g/mol or more.
By "semi-crystalline" is meant a material which has a mixture of crystalline domains and amorphous domains. The degree of crystallinity is usually between 1 % and 95% or between 2 and 90%.
With an aliphatic diol residue is meant that the diol residue does not contain aromatic groups. The aliphatic diol residue is in particular a residue wherein the two oxygen atoms (i.e. those originating from the diol hydroxyl groups but in the polyester being part of an ester group) are for example separated by a -(CH2)n- group, where n is 2 or more. They may also be separated by a -(CHR)2- group, where is R is a hydrocarbyl group, e.g. a methyl group or an ethyl group. They may also be separated by a -(CHR1)- (CH2)n-(CHR2)- group, where n is 1 one or more and R1 and R2 are a hydrocarbyl group, e.g. a methyl group or an ethyl group. R and R2 may be different hydrocarbyl groups that are chosen independently from each other.
The link between the two oxygen atoms in the aliphatic diol residue is in particular selected from the group of -(CH2)2- (i.e. ethylene), -(CH2)3- (i.e. ,3-propylene), -(CH2>4- {i.e. ,4-butylene) and -(CHCH3HCH3CH)- (i.e. 2,3-butylene). Thus, the diol from which the residue is derived is in these cases ethylene glycol, ,3-propylene glycol, 1 ,4-butylene glycol and 2,3- butylene glycol. The melting point of a polyester according to the invention usually depends on the average molar mass Mn. Thus, by varying the Mn of polyesters of the invention, the melting point can be influenced. Usually, polyesters of the invention have a melting temperature of 160°or lower, 150°or lower, 140°or lower or 130°or lower.
A polyester according to the invention is usually opaque in its solid state.
It was surprisingly found that the melting points of the polyesters of the invention are much lower than those of the 2,5-furandicarboxylic acid analogues. In addition, the polyesters of the invention have a higher thermal stability than the corresponding polyesters derived from 2,5-furandicarboxylic acid (see Table 2).
The invention further relates to a process for preparing a polymer of the invention, comprising forming a mixture comprising
- 2,4-furandicarboxylic acid and/or an ester-forming derivative thereof;
- an aliphatic diol and/or an ester-forming derivative thereof; and
- a catalyst,
followed by performing a melt polymerization by exposing the mixture to a temperature of at least 100 °C, yielding a semi-crystalline polyester.
Usually, once formed, the mixture is exposed to elevated
temperatures, e.g. up to 150 °C, up to 175 °C, up to 200 °C, up to 215 °C or up to 225 °C. The best results are obtained when the temperature of the mixture is increased step-wise to up to 215 °C.
Usually, the molar ratio of 2,4-furandicarboxylic acid and/or an ester- forming derivative thereof to aliphatic diol and/or an ester-forming derivative thereof is in the range of 1 :1.5 to 1 :2.5. Thus there is usually an excess of the diol relative to the diacid.
The amount of 2,4-furandicarboxylic acid and/or an ester-forming derivative thereof and aliphatic diol and/or an ester-forming derivative thereof in the mixture may be at least 60 mol%, at least 70 mol%, at least 80 mol%, at least 90 mol% or at least 95 mol% of the monomers present in the mixture.
Usually, the 2,4-furandicarboxylic acid (ester) monomers and the aliphatic diol (ester) monomers together constitute 50 mol% or more of the total amount of monomers in the mixture.
The polyester obtained with a process of the invention is usually colourless. In the event that it is coloured, for example slightly yellow, it may easily be obtained as a colourless solid after purification. Purification may for example be performed by dissolving the polyester in a chlorinated solvent such as chloroform followed by precipitation in an alcohol such as methanol.
It is surprising that with 2,4-furandicarboxylic acid colourless polyesters can be obtained, in particular when during the synthesis
temperatures of up to 200 °C or 215 °C are applied. This is because - in contrast to the 2,5-furandicarboxylic acid isomer - there is an alpha-hydrogen atom on the 5-position of the furan ring (i.e. at the carbon next to the oxygen). Such hydrogen atom is much more reactive than the other hydrogens on the furan ring (on the 3- and 4-positions), and is known to make the
2,4-furandicarboxylic acid monomer more susceptible to degradation and accompanying colouration, especially when it is exposed to elevated temperatures above 200 °C. In a method of the present invention, however, the polyester product appears to be colourless or almost colourless, which is an advantage for the application the polyester in bottles for e.g. soda.
The catalyst may be selected from the group of titanium
tetraalkoxides (e.g. Ti(/-OPr)4, Ti(OEt)4, or Ti(OMe)4, Ti(/-OBu)4))',
dibutyltinoxide (DBTO), dibutyltinlaurate (DBTL), stannous oxide and tinoctanoate.
By an ester-forming derivative of a diol or a carboxylic acid is meant a derivative that is capable of being transformed into an ester. This is also meant to include a monomeric ester from which a polyester is formed. In the latter case, a transesterification reaction takes place.
An ester-forming derivative of a diol may be an ester, for example an acetate ester. An ester-forming derivative of a carboxylic acid may be its diacid chloride or its diester such as a dimethyl ester or a diethyl ester.
The invention further relates to a polymer obtainable by the process of the invention. EXAMPLES
Synthesis: In a typical experiment, polymerizations were conducted in 100 ml_ three-neck round-bottom flasks equipped with a mechanical overhead stirrer, nitrogen inlet and water-condenser. 2,4-furandicarboxylic acid dimethylester (1.5 g, 8.14 mmol) and diol (16.2 mmol) were charged into the reaction flask. The set-up was placed under vacuum and purged with nitrogen gas, and this cycle was repeated for three times.
The polymerization method involves two stages. During the first stage, the reaction was carried out under nitrogen gas to form oligomers. The reaction mixture was heated in the silicone-oil bath at 115 °C for 15 min. After observing the complete melt of the mixtures, the catalyst Ti(OiPr)4 (0.10 mmol) in 1 ml_ of toluene was added into the flask under the continuous flow of nitrogen gas. The temperature was now increased to 160 °C and stirred for 12 h, and finally to 200 - 215 °C for 1 -2 h to complete the first stage of pre- polymerisation reaction. The methanol and toluene were collected in the cooling flask.
During the second stage of the polymerization to obtain high molar mass polyesters, high vacuum of 0.02 mbar was applied gradually to the polymerisation set-up at 210 - 215 °C for 2 h. After completion of the reaction, the reaction mixture was cooled down to room temperature under nitrogen atmosphere. The polymer was purified by dissolving in 10 mL of chloroform/TFA mixture (6:1 ) and precipitated in 100 mL of methanol to yield a white powder. The yields were in the range of 80 - 90 %. The structural and thermal properties of the obtained polyesters were measured and are given in the tables below (Table 1 & 2).
Table 1. Molar masses of polyesters based on 2,4-furandicarboxylic acid dimethyl ester (2,4-FDCA-Me, white rows) and 2,5-furandicarboxylic acid dimethyl ester (2,5-FDCA-Me, grey rows) with the diols ,2-ethanediol (1 ,2- EDO), 1 ,3-propanediol (1 ,3-PDO), 1 ,4-butanediol (1 ,4-BDO) and 2,3- butanediol (2,3-BDO).
Figure imgf000009_0001
The molar masses of the polymers were determined by GPC, using HFIP as solvent.
Table 2. Thermal properties of polyesters based on
2.4- furandicarboxylic acid dimethyl ester (2,4-FDCA-Me, white rows) and
2.5- furandicarboxylic acid dimethyl ester (2,5-FDCA-Me, grey rows) with the diols 1 ,2-ethanediol (1 ,2-EDO), 1 ,3-propanediol (1 ,3-PDO), 1 ,4-butanediol
(1 ,4-BDO) and 2,3- butanediol (2,3-BDO).
Figure imgf000009_0002
TGA samples were heated from 30 °C to 600 °C at a heating rate of 10 °C/min under a nitrogen flow of 60 mL/min.
The DSC measurement followed the standard heating and cooling rate of 10 °C/min. Not observed up to 230 °C.

Claims

Claims
1. Semi-crystalline polyester comprising dicarboxylic acid residues and diol
residues, wherein the dicarboxylic acid residues comprise
2,4-furandicarboxylic acid residues and wherein the diol residues comprise aliphatic diol residues.
2. Semi-crystalline polyester according to claim 1 , wherein the 2,4- furandicarboxylic acid residues constitute 50 mol% or more of the total amount of dicarboxylic acid residues.
3. Semi-crystalline polyester according to claim 1 or 2, wherein the aliphatic diol residues constitute 50 mol% or more of the total amount of diol residues.
4. Semi-crystalline polyester according to any one of claims 1-3, wherein the dicarboxylic acid residues further comprise one or more residues selected from the group of 2,5-furandicarboxylic acid residues, 3,4-furandicarboxylic acid residues, 2,3-furandicarboxylic acid residues, terephthalic acid residues, isophthalic acid residues, phthalic acid residues, succinic acid residues and adipic acid residues.
5. Semi-crystalline polyester according to any one of claims 1-4, wherein the diol residues comprise two or more different types of aliphatic diol residues.
6. Semi-crystalline polyester according to any one of claims 1-5, further
comprising monohydroxy monocarboxylic acid residues.
7. Semi-crystalline polyester according to any one of claims 1-6, wherein up to 50 mol% of the total amount of residues are monohydroxy monocarboxylic acid residues.
8. Semi-crystalline polyester according to claim 7, wherein the monohydroxy
monocarboxylic acid residue is selected from the group of ortho- hydroxybenzoic acid, meta-hydroxybenzoic acid, para-hydroxybenzoic acid, lactic acid, glycolic acid and gamma-hydroxybutyric acid.
9. Semi-crystalline polyester according to any one of claims 1-8, wherein the aliphatic diol residue is selected from the group of ethylene glycol, 1 ,2- propanediol, 1 ,3-propanediol, ,2-butanediol, ,3-butanediol, 1 ,4-butanediol, 2,3-butanediol, 1 ,5-pentanediol, 1 ,4-pentanediol, 2,4-pentanediol 1 ,6- hexanediol, 1 ,5-hexanediol, 1 ,4-hexanediol, 2,5-hexanediol, 3,4-hexanediol, cyciobutane-1 ,2-dimethanol, cyclobutane-1 ,3-dimethanol, cyclopentane-1 ,2- dimethanol, cyclopentane-1 ,3-dimethanol, cyclohexane-1 ,2-dimethanol, cyclohexane-1 ,3-dimethanol, cyclohexane-1 , 4-dimethanol and
2,2-bis(4-hydroxycyclohexyl)propane.
0. Semi-crystalline polyester according to any one of claims 1-9, having a melting temperature of 160°or lower.
1 . Process for preparing a polyester according to any one of claims 1-10,
comprising forming a mixture comprising
- 2,4-furandicarboxylic acid and/or an ester-forming derivative thereof;
- an aliphatic diol and/or an ester-forming derivative thereof; and
- a catalyst,
followed by performing a melt polymerization by exposing the mixture to a temperature of at least 00 °C, yielding a semi-crystalline polyester, and thereafter optionally followed by performing a solid state post condensation.
12. Process according to claim 11 , wherein the molar ratio of 2,4-furandicarboxylic acid and/or an ester-forming derivative thereof to aliphatic diol and/or an ester- forming derivative thereof is in the range of 1 :1.5 to 1 :2.5.
13. Process according to claim 1 or 12, wherein the amount of 2,4- furandicarboxylic acid and/or an ester-forming derivative thereof and aliphatic diol and/or an ester-forming derivative thereof in the mixture is at least 95 mol% of the monomers present in the mixture.
14. Process according to any one of claims 1-13, wherein the catalyst is
selected from the group of titanium tetraalkoxides, dibutyltinoxide (DBTO), dibutyltinlaurate (DBTL), stannous oxide and tinoctanoate.
15. Semi-crystalline polyester obtainable by the process of any of claims 1 1-14.
PCT/NL2014/000019 2013-06-21 2014-06-23 Semi-crystalline polyester WO2014204296A1 (en)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
NL1040265 2013-06-21
NL1040265A NL1040265C2 (en) 2013-06-21 2013-06-21 SEMI-CRYSTALLINE POLYESTER.

Publications (1)

Publication Number Publication Date
WO2014204296A1 true WO2014204296A1 (en) 2014-12-24

Family

ID=49585558

Family Applications (1)

Application Number Title Priority Date Filing Date
PCT/NL2014/000019 WO2014204296A1 (en) 2013-06-21 2014-06-23 Semi-crystalline polyester

Country Status (2)

Country Link
NL (1) NL1040265C2 (en)
WO (1) WO2014204296A1 (en)

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2017023173A1 (en) * 2015-08-04 2017-02-09 Furanix Technologies B.V. Masterbatch polyester composition
WO2017048119A1 (en) * 2015-09-14 2017-03-23 Furanix Technologies B.V. Process for the preparation of a polyester
EP3235848A1 (en) * 2016-04-18 2017-10-25 Stichting Wageningen Research Furan dicarboxylate copolyesters
WO2018067007A1 (en) * 2016-10-05 2018-04-12 Furanix Technologies B.V. Process for the production of a solid-state polymerized poly (tetramethylene-2, 5-furan dicarboxylate) polymer and polymer thus produce
US10208006B2 (en) 2016-01-13 2019-02-19 Stora Enso Oyj Processes for the preparation of 2,5-furandicarboxylic acid and intermediates and derivatives thereof
US11192872B2 (en) 2017-07-12 2021-12-07 Stora Enso Oyj Purified 2,5-furandicarboxylic acid pathway products

Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2009227717A (en) * 2008-03-19 2009-10-08 Nec Corp Polylactic acid-based copolymer
JP2010280767A (en) * 2009-06-02 2010-12-16 Canon Inc Polyester resin, method for producing the same and molded article
BRPI1005070A2 (en) * 2010-12-30 2013-04-16 Univ Fed Do Rio Grande Do Sul renewable thermoplastic elastomer, and, use thereof
WO2013120989A2 (en) * 2012-02-17 2013-08-22 Uhde Inventa-Fischer Gmbh Process for preparing a high molecular weight heteroaromatic polyester or copolyester

Patent Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2009227717A (en) * 2008-03-19 2009-10-08 Nec Corp Polylactic acid-based copolymer
JP2010280767A (en) * 2009-06-02 2010-12-16 Canon Inc Polyester resin, method for producing the same and molded article
BRPI1005070A2 (en) * 2010-12-30 2013-04-16 Univ Fed Do Rio Grande Do Sul renewable thermoplastic elastomer, and, use thereof
WO2013120989A2 (en) * 2012-02-17 2013-08-22 Uhde Inventa-Fischer Gmbh Process for preparing a high molecular weight heteroaromatic polyester or copolyester

Non-Patent Citations (2)

* Cited by examiner, † Cited by third party
Title
J. RENEW. MATER., vol. 1, no. 1, January 2013 (2013-01-01), pages 61 - 72
MOORE J A ET AL: "POLYESTERS AND POLYAMIDES CONTAINING ISOMERIC FURAN DICARBOXYLIC ACIDS", POLYMER SCIENCE AND TECHNOLOGY, PLENUM PRESS, US, vol. 31, 1 January 1985 (1985-01-01), pages 51 - 91, XP009116061, ISSN: 0093-6286, ISBN: 978-0-306-42467-0 *

Cited By (18)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
NL2015264B1 (en) * 2015-08-04 2017-02-21 Furanix Technologies Bv Masterbatch polyester composition.
WO2017023173A1 (en) * 2015-08-04 2017-02-09 Furanix Technologies B.V. Masterbatch polyester composition
WO2017048119A1 (en) * 2015-09-14 2017-03-23 Furanix Technologies B.V. Process for the preparation of a polyester
JP2018526521A (en) * 2015-09-14 2018-09-13 センヴィナ・セー・フェー Polyester manufacturing method
US10590235B2 (en) 2015-09-14 2020-03-17 Synvina C.V. Process for the preparation of a polyester
US11613523B2 (en) 2016-01-13 2023-03-28 Stora Enso Oyj Processes for the preparation of 2,5-furandicarboxylic acid and intermediates and derivatives thereof
US10208006B2 (en) 2016-01-13 2019-02-19 Stora Enso Oyj Processes for the preparation of 2,5-furandicarboxylic acid and intermediates and derivatives thereof
US11891370B2 (en) 2016-01-13 2024-02-06 Stora Enso Ojy Processes for the preparation of 2,5-furandicarboxylic acid and intermediates and derivatives thereof
US10442780B2 (en) 2016-01-13 2019-10-15 Stora Enso Oyj Processes for the preparation of 2,5-furandicarboxylic acid and intermediates and derivatives thereof
US10654819B2 (en) 2016-01-13 2020-05-19 Stora Enso Oyj Processes for the preparation of 2,5-furandicarboxylic acid and intermediates and derivatives thereof
US10851074B2 (en) 2016-01-13 2020-12-01 Stora Enso Oyj Processes for the preparation of 2,5-furandicarboxylic acid and intermediates and derivatives thereof
EP3235848A1 (en) * 2016-04-18 2017-10-25 Stichting Wageningen Research Furan dicarboxylate copolyesters
WO2018067007A1 (en) * 2016-10-05 2018-04-12 Furanix Technologies B.V. Process for the production of a solid-state polymerized poly (tetramethylene-2, 5-furan dicarboxylate) polymer and polymer thus produce
KR102453497B1 (en) 2016-10-05 2022-10-11 퓨라닉스 테크놀러지스 비.브이. Process for the production of solid-phase polymerized poly(tetramethylene-2,5-furan dicarboxylate) polymers and polymers produced therefrom
US11174344B2 (en) 2016-10-05 2021-11-16 Furanix Technologies B.V. Process for the production of a solid-state polymerized poly (tetramethylene-2, 5-furan dicarboxylate) polymer and polymer thus produced
KR20190065369A (en) * 2016-10-05 2019-06-11 퓨라닉스 테크놀러지스 비.브이. The production process of the solid-phase polymerized poly (tetramethylene-2,5-furan dicarboxylate) polymer and the resulting polymer
US11192872B2 (en) 2017-07-12 2021-12-07 Stora Enso Oyj Purified 2,5-furandicarboxylic acid pathway products
US12049456B2 (en) 2017-07-12 2024-07-30 Stora Enso Oyj Purified 2,5-furandicarboxylic acid pathway products

Also Published As

Publication number Publication date
NL1040265C2 (en) 2014-12-24

Similar Documents

Publication Publication Date Title
NL1040265C2 (en) SEMI-CRYSTALLINE POLYESTER.
JP5517494B2 (en) Polyester, production method thereof, and molded product
TWI385194B (en) Aromatic polyester and its manufacturing method
JP6371278B2 (en) Production method of polyester resin
JP2003501532A (en) Amorphous copolyester with high glass transition temperature and low melt viscosity
JP2015518915A (en) Polyester resin and method for producing the same
JP2015518916A (en) Polyester resin and method for producing the same
JP7159213B2 (en) polyester copolymer
KR101372581B1 (en) Hydrolysis resistant and biodegradable aliphatic/aromatic copolyester resin composition
CN104371094B (en) Two steps of high-performance poly copolyether ester elastomer feed intake synthetic method
JPS5913531B2 (en) Copolyester manufacturing method
KR20160024218A (en) Copolymerized Polyester for Low-melting Binder with Excellent Form Stability and Polyester Binder Fiber Using Same
CN107245140B (en) Aliphatic-aromatic copolyester of high molecular weight and its preparation method and application
JP7369178B2 (en) Polyester resin and its manufacturing method
KR20170011081A (en) Polyester Binder Resin Composition and Polyester Binder Fibers with Low Melting Point
JP2020513057A (en) Method for producing polyarylene sulfone / polyester block copolymer (P)
JP7397671B2 (en) polyester copolymer
TWI703171B (en) Bibenzoate copolyesters and methods to produce them
JP2010031175A (en) Copolyester and production method thereof
KR101813395B1 (en) Polyester-amide and method for preparing the same
KR102043372B1 (en) Copolymerized Polyester for Low-melting Binder with Excellent Touch and Color and Polyester Binder Fiber Using Same
NL1040372C2 (en) Semi-crystalline polyester.
Zhao et al. Biodegradable poly (butylene succinate-co-butylene dimerized fatty acid) s: Synthesis, crystallization, mechanical properties, and rheology
JP2004217721A (en) Polyester and its manufacturing method
JPH0710979A (en) Amine-functional polyester

Legal Events

Date Code Title Description
121 Ep: the epo has been informed by wipo that ep was designated in this application

Ref document number: 14758677

Country of ref document: EP

Kind code of ref document: A1

NENP Non-entry into the national phase

Ref country code: DE

122 Ep: pct application non-entry in european phase

Ref document number: 14758677

Country of ref document: EP

Kind code of ref document: A1