THERMOPLASTIC BLOCK COPOLYESTER ELASTOMER
The invention relates to a thermoplastic block copolyester elastomer comprising hard segments composed of units derived from at least one alkylene glycol and at least one aromatic dicarboxylic acid, and soft segments of a triblock copolymer containing one, optionally hydrogenated, polyalkadiene block and two poly (alkylene oxide) blocks, which segments are linked to each other by ester bonds.
The invention also relates to a triblock copolymer, the preparation of the triblock copolymer, its use as a soft segment and the preparation of the thermoplastic block copolyester elastomer.
Thermoplastic block copolyether ester elastomers with hard segments composed of units derived from at least one alkylene glycol and at least one aromatic dicarboxylic acid and with soft segments derived from at least one pol alkylene oxide are known and are described extensively in for instance Chapter 8 of the book entitled "Thermoplastic Elastomers", ed. by G. Holden et al . , 2nd ed. (1996) from Hanser Verlag, Munich, Vienna and New York, ISBN 1-56990-205-4.
The known block copolyether esters find application in many areas and offer advantages over other thermoplastic elastomers, e.g. due to better processability as a result of the presence of the rapidly crystallising polyester hard segments.
An important area of application is that of breathable films, i.e. films that are permeable to water vapour, but impermeable to water. Such films find application in sanitary products such as diapers, in surgical protective clothing, in rainproof clothing, in tent cloth and as sheets in roofing and housing constructions. In order to ensure a
good water vapour permeability the film used in these products should be very thin. In order to retain sufficient mechanical strength, such films are mostly applied onto a fabric or a non-woven carrier, for instance a polyester fabric. The water vapour permeability of the film can be influenced in various manners by the chemical composition of the polyether ester block copolymer. A low hard segment : soft segment ratio has a favourable effect on the water vapour permeability. However, the processability of such a material into film is adversely affected. In presently current commercial film materials the aim is to have the lowest possible C:0 ratio in the polyether soft segments. This is achieved by applying the highest possible content of units based on polyethylene oxide. However, the drawback then encountered is the high water absorption capacity of the film, which results in swelling and a considerable decline in mechanical properties in case of prolonged contact with water.
The object of the invention therefore is to provide a material which exhibits improved water vapour permeability, but does not have said restrictions or only to a much lesser extent. This object is achieved with the thermoplastic block copolyester elastomer defined in the first paragraph .
Another advantage of the block copolyester elastomers according to the invention is that they show surprisingly good mechanical properties, in particular very good elastic properties. It has been observed that for example tension set, i.e. the residual deformation after relaxation of an initially elongated sample is significantly lower than with known a block copolyether ester elastomer with similar length of the polyester hard soft segment .
Still another advantage of the block copolyester elastomers according to the invention is that they retain much of their mechanical properties at low temperatures, until just
above the glass transition of the polyalkadiene blocks.
The improved mechanical properties are not only ofadvantage for said applications as breathable films, but also for other applications, like for example boots and bellows, tubes and hoses, sheets, films and fibers.
The alkylene glycol preferably used is a C -C6 alkylene glycol, for instance ethane diol, 1,3 -propane diol and 1,4 -butane diol. Suitable aromatic dicarboxylic acids are for example terephthalic acid, 1 , 6-naphthalene dicarboxylic acid, 4 , 4 ' -diphenyl dicarboxylic acid and, to a lesser extent, isophthalic acid or mixtures of these dicarboxylic acids. Particularly suitable as hard segment is for instance polybutylene terephthalate, because of its favourable crystallisation behaviour. The polyalkadiene blocks in the soft segments are preferably derived from butadiene or isoprene; but in general C3-C8 alkadienes are suitable. The polyalkadienes are preferably, at least partly, hydrogenated. Advantages thereof are better low temperature properties, e.g. a lower glass transition, and better properties at elevated temperatures, e.g. improved thermal -oxidative stability.
The poly (alkylene oxide) blocks are by preference derived from one or more alkylene oxides chosen from the group comprising C2-C4 alkylene oxides. Most prefered areethylene oxide and propylene oxide or combinations of these, because of their hydrophilicity/polarity .
The invention also relates to a triblock copolymer containing one, optionally hydrogenated, polyalkadiene block and two poly (alkylene oxide) blocks, characterised in that the poly (alkylene oxide) blocks have a number-averaged molecular weight of less than 5000 g/mol .
In JP-A-62 232493 a triblock copolymer containing one polybutadiene block and two poly (alkylene oxide) blocks is disclosed, but without said selection of molecular weight. In
this accidental anticipation the triblock copolymer is used as a dispersion aid to make coal/water slurry compositions with a high concentration of coal .
The present invention therefore also relates to the use of a triblock copolymer containing one, optionally hydrogenated, polyalkadiene block and two poly (alkylene oxide) blocks as a soft segment for the preparation of block copolymer elastomers . These block copolymers generally are thermoplastic in nature, although some crosslinking may have taken place. Examples of such elastomers are segmented block copolymers comprising hard segments derived from a polycondensation polymer. Suitable polycondensation polymers include for example polyurethanes , polyamides, or polyesters. Especially polyesters are preferred in view of the favourable combination of properties of the resulting block copolyester elastomers .
The invention also relates to a process for the preparation of the triblock copolymer containing one polyalkadiene block and two poly (alkylene oxide) blocks, starting from hydroxy-terminated (optionally hydrogenated) polyalkadiene and at least one alkylene oxide, comprising: a) reaction of the hydroxy-terminated, optionally hydrogenated, polyalkadiene with an organic compound, whereby the terminal hydroxyl groups are substituted by groups that initiate anionic ring-opening polymerisation, and b) started by the initiator groups introduced in step a) , anionic ring-opening polymerisation of the at least one alkylene oxide on the (hydrogenated) polyalkadiene until a desired poly (alkylene oxide) block length has been obtained. In JP-A-62 232493 preparation of a triblock copolymer containing one polybutadiene block and two poly (alkylene oxide) blocks via addition polymerisation in general is indicated. The anionic ring-opening polymerisation process of the present invention has the advantage that the
block length of the poly (alkylene oxide) can be well controlled.
For the anionic ring-opening polymerisation any suitable initiator group, which can be substituted for the hydroxyl group in the hydroxy-terminated, optionally hydrogenated polyalkadiene, can in principle be used, for instance radical anions, alkali metal hydroxides, alkali metal alkyls, alkali metal aryls, alkali salts of aromatic amines, (carbazole derivatives) , or tetraphenyl porphyrine Al- complexes. Anionic ring-opening polymerisation is described extensively for instance in "Comprehensive Polymer Science" , Vol. 3, Chapter 32, Pergamon Press, Oxford (1989), pp. 467 ff. and in the contribution from S.S. Pomkowski and A. Dude, Anionic Ring-opening Polymerization, in "Ring-opening polymerization", D.J. Brunelle, ed. , Hanser Verlag, Munich (1993) pp. 87. ff.
The length of the blocks in the triblock copolymer can vary within wide limits. Especially for use as soft segment in block copolymer elastomers, this length is preferably chosen such that the polyalkadiene segment shows entanglement, while the poly (alkylene oxide) blocks show no entanglement. The number-averaged molecular weight, Mn, of the hydroxy-terminated polyalkadiene started from is therefore preferably at least 2,000, more preferably at least 3,000 g/mol . , The number-averaged molecular weight, Mn, of the poly (alkylene oxide) blocks is preferably less than 5,000, more preferably less than 3,000 and still more preferably less than 2,000 g/mol. A minimum value of Mn of the poly (alkylene oxide) blocks of 500 is preferred to give the triblock copolymer some polar character. The number-averaged molecular weight of the triblock copolymer preferably varies between approx. 4,500 and 13,000 g/mol, more preferably between 5,000 and 10,000 g/mol.
The block copolyester elastomer according to the
invention can subsequently be obtained by a process similar to the process for the preparation of polyether ester block copolymer according to the state of the art, as described for instance in the above-mentioned reference in the book 'Thermoplastic Elastomers'.
The process for the preparation of the thermoplastic block copolyester elastomer according to the invention, starting from the triblock copolymer containing one, optionally hydrogenated, polyalkadiene block and two poly (alkylene oxide) blocks, derived from at least one polyalkadiene and at least one alkylene oxide, and at least one alkylene glycol and at least one aromatic dicarboxylic acid or an ester thereof, comprises a) a transesterification reaction at about 200CC at atmospheric pressure and optionally in the presence of a transesterification catalyst, in which process volatile reaction products are removed by distillation and a low- molecular prepolymerizate is formed, followed by b) polycondensation at a temperature of about 250 °C and reduced pressure, in which process volatile compounds are removed until a product having the desired molecular weight is obtained.
The proportions of the starting materials in step a) are chosen such that the desired ratio between hard and soft segments in the end product is obtained. The hard : soft segments weight ratio is normally between 10:90 and 90:10, preferably between 15:85 and 80:20, still more preferably between 20:80 and 50:50.
Any current transesterification and polycondensation catalyst can be used as catalyst, for instance Ti-tetraisobutoxide . The transesterification and polycondensation reactions are preferably carried out in the presence of a thermal -oxidative stabiliser. Suitable antioxidants are for instance sterically hindered phenolic
compounds such as IRGANOX® 1330 from Ciba.
The invention will now be elucidated with reference to the following example, without however being limited thereto.
Chemicals used:
Hydroxy-terminated hydrogenated polybutadiene KRATON LIQUID® Polymer HPVM-2203, from Shell, Mn = approx. 3600, OH functionality approx. 1.9. Dried by freeze-drying with benzene.
Ethylene oxide 3.0, Linde > 99.90%, dried over CaH2 Tetrahydrofuran, water-free (THF) 1,4 -butane diol dimethyl terephthalate - potassium naphthalide, obtained by reacting potassium with naphthalene in tetrahydrofuran (0.4 mmol/1) titanium tetraisobutoxide Ti(OBu)4 IRGANOX® 1330
Synthesis of the triblock copolymer
The polymerisation reactions were carried out in a 1- or 3-litre glass autoclave, Bϋchi make.
The KRATON HPVM-2203, to be referred to in the following shortly as "polybutadiene diol', was dissolved in water-free THF to an end-group content of approx. 10 mmol/1 and supplied in a known quantity to the reactor.
Then, using a syringe, the potassium naphthalide solution was added slowly and with stirring at 30°C until a permanent green coloration persisted, i.e. for at least 45 minutes.
Next, the reactor was cooled to 0°C and the required amount of ethylene oxide was supplied to the reactor at a slight underpressure. This resulted in an immediate decoloration of the reaction solution. The solution was heated
to 55 °C. The polymerisation was terminated after 4 days through the addition at room temperature of a 1:5 mixture (vol/vol) mixture of methanol and acetic acid. The reactor contents were filtered and concentrated by means of a rotary evaporator. After removal of acetic acid by azeotropic distillation with toluene the crude product was dissolved in chloroform and extracted with distilled water. After drying over water-free sodium sulphate the chloroform is evaporated. The resulting product, as an approximately 10% solution in THF, was precipitated in a 10-fold excess of acetone at -30°C, filtered off and dried for more than one day at 40CC in vacuum.
With quantities of some tens of grams this process already gave yields of 85% of the theoretical value. By means of differential scanning calorimetry
(DSC) the transition temperatures, Tons, Tm and Tg as well as ΔHm of the triblock copolymers obtained were determined. Tons is the onset temperature at which the polyethylene oxide block starts to melt, Tm the maximum in the melt transition and Tg the glass transition temperature and ΔHm the melt enthalpy. In Table 1 are also given the calculated average length of the polyethylene oxide blocks and the lengths derived from NMR measurements by correlating the integrals on the basis of the signal at δ = 0.85 ppm and the average molecular weight Mn = 3590 of the polybutadiene diol.
rH
LD
Synthesis of the copolyester elastomers
The synthesis was carried out via a two-step melt polycondensation in the presence of titanium tetrabutoxide as a transesterification and polycondensation catalyst and Irganox® 1330 as a thermal -oxidative stabilizer. In the first step of the polycondensation the reactor mixture was heated at atmospheric pressure at 190, 210 en 220°C successively, each time for 1 hour, with the methanol forming in the transesterification being distilled off. In the subsequent second step of the polycondensation the temperature was raised to 230-250°C and the excess of butanol was removed under reduced pressure (2-5.10"2 mbar) . After about 2.5 hours the polycondensation was stopped.
Table 2 presents an overview of the synthesised copolyester elastomers. The nomenclature is based on the weight proportion of the PBT and the length of the polyethylene oxide blocks of the triblock copolymer used. The yield was in virtually all cases more than 95% with reference to the theoretical value. The thermal transition points were determined by means of DSC (20°C/min) .
Dumb-bell -shaped specimens were made of the various polymers for testing on an Instron 5565 tensile test machine at room temperature .
Table 2
In the range of 3-4% strain a drawing rate of 0.2 mm/s was chosen in order to determine the modulus of elasticity. Then the rate was increased to 20 mm/s and measurement was continued until the specimen failed. (Table 3] (Figure 1)
Table 3
Figure 1 shows the stress-strain diagrams of some copolyester elastomers: (■) PBT40-1000, (•) PBT30-1000, (A) PBT20-1000, (▼) PBTlO-100.
On sample PBT20-1000 some additional tensile tests were performed. The sample was initially elongated to 500%, and subsequently the stress was released. The sample was allowed to relax after which an elastic recovery of 397%, i.e. a tension set of 103%, was observed. This points to a significant improvement in elastic properties compared to a known copolyether ester containing polyester hard segments of similar length.
Further the water absorption (swelling) of a large number of samples was determined by keeping specimens submerged in water for 3 weeks at room temperature and measuring their increase in weight . Figure 2 shows the dependence of the water absorption, i.e. weight increase in %, of the proportion by weight of the triblock copolymer [%] and the block length of the PEO (g/mol) .
From the results it appears that the copolyester elastomers in the tensile test show the typical behaviour of a thermoplastic elastomer. There is a clear separation between the different phases in the copolyester, as a result of which
the water vapour migration in the polyethylene oxide phase is promoted. The water absorption of the novel copolyester elastomer is low in spite of a high content of high-molecular polyethylene oxide in the segments.