Note: Descriptions are shown in the official language in which they were submitted.
21 88~59
-
Docket No. 7092
THI~I~MOPLASTIC POL~U~ET~ANE COMrOSITIONS
IMPROVED UV ~ND llEAT I~ESIST~NCE:
BACKGROUND O~ THE INVENTION
1. Field of the Invention
The present invention pertains to thermoplastic polyurethane. More particularly,
the present invention provides tllermoplastic polyurethane compositions wllicll exllibit
optimum W and heat resistance while maintaining desirable performance properties and
a process for making molded thermoplastic articles having desirable W and heat
resistance properties.
15 2. Description of the Related Art
Commercial applications of thermoplastic polyurethane (TPU) continue to grow
at a rapid pace. Unlike their thermoset relatives, thermoplastic polyurethanes can be
processed in a manner similar to other thermoplastics in operations such as extrusion,
injection molding, wire coating, etc. In addition to its desirable processability, TPU
20 finds applicability in a wide variety of end use applications because of its optimum
combination of performance properties.
For example, TPU is desirable because of its llardness, tensile strength, modulus,
flexibility, and/or tensile elongation. The combination of SUCIl pllysical properties and a
ready adaptability to a wide variety of processing and molding parameters results in the
2s use of TPU in numerous end use applications, especially in many consumer goods.
2~88~
As a result of its use in consumer goods, in addition to optimum processing and
perforrnance properties, commercially desirable TPU formulations must be visually
appealing, and maintain such desirable visual characteristics over the lifetime of the part.
In consumer applications, this often translates into a desire for TPU compositions capable
of exhibiting good W resistance and heat stability.
With respect to heat stability, the TPU composition must not yellow or dull uponexposure to the temperatures normally encountered upon typical TPU composition
processing. Typical processing temperatures reach between 380F to 420F and often
result in a light yellow or dull appearance of the final TPU composition containing
0 product. In addition, the part must not yellow or dull upon long term exposure to
moderate and higher temperatures encountered during its lifetime. Typical temperatures
which may be encountered during part use are from 23C to 80C . It will be appreciated
that a yellowed or dulled appearance is detrimental, and in many consumer and
automotive applications, unacceptable.
Once a heat stable TPU composition has been achieved, the visually pleasing
appearance of the TPU containing product must be maintained over the lifetime of that
particular product. That is, upon exposure to outdoor light, and in particular, ultraviolet
light, the final product must not exhibit yellowing, dulling, chalking, whitening, or
blushing.
Thus, it would be desirable to provide a TPU composition which possesses
optimum processability and performance characteristics while still exhibiting good heat
21 88~59
stability and resistance to W degradation. Such a TPU composition would be
particularly desirable for use in consumer and automotive applications.
Accordingly, the prior art has long sought such a TPU composition.
For example, PVC has been added to TPU compositions in an attempt to improve
5 W resistance. However, although performance in W was improved, such compositions
are unacceptable due to poor heat stability, i.e., significant yellowing as a result of initial
processing.
n 06306248 A reports a heat and light resistant resin composition for slush
molding, comprising acrylic resin and thermoplastic polyurethane resin. The
0 composition is obtained by dispersing an aliphatic based polyurethane having isocyanate
groups which contain a reactive acrylic resin (cont~inin~ OH), in a dispersing medium
and by extending the chain and m~kin~ it into powder. The composition has ten$ile
strength at least 50 kg/cm2 and elongation at rupture at least 100% as a molded film. The
English abstract does not report any heat and/or light lesialallce data.
EP 459257 discloses a therrnoplastic blend of polyurethane and partly cured graft
rubber which has good mechanical properties and aging resistance. The thermoplastic
flexible composition consists of therrnoplastic polyurethane and partly crosslinked graft
rubbers based on an acrylate rubber with a core/shell structure and/or a silicone rubber.
The partly crosslinked graft rubber has a rubber content of 40-~5 weight percent and
20 contains a grafted copolymer of vinyl monomers, preferably styrene, alpha-
methylstyrene, acrylonitrile, 1-6 C alkyl methacrylate or vinyl 1-3 C carboxylate. The
' 2188~9
partly crosslinked graft rubber may have a polybutadiene core, acrylate rubber shell and
grafted vinyl monomers. No heat or W resistance data is reported.
US 5,237,001 discloses a thermoplastic composition which is a blend of A) a
thermoplastic polyurethane and B) at least partially cross-linked alkyl acrylate copolymer
5 of a C, 6 alkyl acrylate and a monomer selected from the group consisting of
acrylonitrile, styrene, vinyl acetate, Cl 6 alkyl methacrylates, and mixtures thereof.
However, none of the foregoing provide TPU compositions having an optimum
blend of heat and light stability in conjunction with traditional TPU performance
properties. In particular, none of the foregoing provide TPU compositions having
o acceptable heat stability p.ope- Iies and resistance to W degradation. Accordingly, it
would be desirable to provide such a composition.
It is thus an object of the invention to provide a TPU composition having an
optimum combination of heat and light resistance in conjunction with traditional TPU
properties.
SUMMARY OF THE INVENTION
The foregoing objects of the invention are achieved with a thermoplastic
polyurethane composition having one or more thermoplastic polyurethanes A), one or
more acrylate based rubbers B), and one or more W and/or heat stabilizers C), wherein
the resulting composition of A) + B) + C) has a greater W stability as compared to a
20 mixture of A) + C), the W stability being measured as the difference between (l.) delta
E versus white tile after molded, and (2.) delta E versus white tile after 1000 hours of
5 ~
QW, with increasing stability being indicated by minimization of the difference
between (1.) and (2.).
More particularly, the invention provides a thermoplastic polyurethane
composition having one or more thermoplastic polyurethanes A) prepared using (i)polyetherols and (ii) aromatic isocyanates; one or more acrylate based rubbers B), a core
shell structure wherein the core is comprised of a partially crosslinked C, 6 alkyl acrylate
and a shell comprised of a Cl 6 alkyl methacrylate; one or more W and/or heat
stabilizers C) comprising an active ingredient which is 2-(2-hydroxy-3,5-di-tert-amyl-
phenyl)-2H-benzotriazole, 1,6-hexanediylbis(3-benzotriazol-N-yl)4-hydroxy-5-tert-
0 butyl) phenyl propionate, and mixtures thereof; wherein the resulting composition of A)
+ B) + C) has a 50% greater W stability as compared to a mixture of A) + C), wherein
W stability is measured as the difference between (1.) delta E versus white tile after
molded, and (2 ) delta E versus white tile after 1000 hours of QW, and increasing
stability is indicated by a minimization of the difference between (1 ) and (2.)The invention further provides a process for making molded thermoplastic
articles having the above-desired W and heat resistance plope- lies, said process
involving the use of the foregoing thermoplastic polyurethane composition
DESCRIPTION OF THE PREFERRED EMBODIMENTS
The thermoplastic polyurethane composition of the invention requires the use of
one or more thermoplastic polyurethanes A), one or more acrylate based rubbers B), and
one or more UV and/or heat stabilizers C), and optionally, one or more compatibilizers
D), and additives E) selected from the group consisting of lubricants, and inhibitors,
Q 5 9
stabilizers against hydrolysis, flame retardants, dyes, pigments, inorganic and/or organic
fillers and reinforcing agents.
The TPUs A) usable according to the present invention can be prepared by
reacting
a) organic, preferably aromatic, diisocyanates, in particular 4,4'-
diphenylmethane diisocyanate, with
b) polyhydroxy compounds, preferably essentially linear polyhydroxy
compounds, having molecular weights of from 500 to 800, in particular polyalkylene
glycol polyadipates having from 2 to 6 carbon atoms in the alkylene moiety and
o molecular weights of from 500 to 6000 or hydroxyl-containing polytetrahydrofuran
having a molecular weight of from 500 to 8000, and
c) diols as chain extenders having molecular weights of from the 60 to 400,
in particular 1,4-butanediol.
in the presence of
d) catalysts and optionally
e) aids and/or
f) additives
at elevated temperatures.
The TPU-forming components (a) to (d) and optionally (e) and/or (f) may be
described in detail as follows:
a) Suitable organic diisocyanates (a) are for example aliphatic, cycloaliphatic
and preferably aromatic diisocyanates. Specific examples are: aliphatic diisocyanates
~ ~ ~ 88~9
~.
such as 1,6-hexamethylene diisocyanate, 2-methyl-lxS-pentamethylene diisocyanate, 2-
ethyl- 1, 4-butylene diisocyanate and mixtures of at least two of said aliphaticdiisocyanates, cycloaliphatic diisocyanates such as isophorone diisocyanate, 1,4-
cyclohexane diisocyanate, 1-methyl-2,4-cyclohexane diisocyanate and 1-methyl-2,6-
s cyclohexane diisocyanate and the collespollding isomeric mixtures, 4,4'-, 2,4'- or 2,2'-
or 2,2'-dicyclohexylmethane diisocyanate and the collesponding isomeric mixtures and
preferably aromatic diisocyanates such as 2,4-toluylene diisocyanate, mixtures of 2,4-
and 2,6- toluylene diisocyanate, 4,4'-,2,4'- and 2,2'-diphenylmethane diisocyanate,
mixtures of 2x4'- and 4x4'-diphenylmethane diisocyanate, urethane-modified liquid
o 4,4' - and/or 2,4'-diphenylmethane diisocyanates, 4,4'-diisocyanato- 1 ,2-diphenylethane,
mixtures of 4,4'-2,4- and 2,2'-diisocyanato-1,2-diphenylethane, preferably those having
a 4,4'-diisocyanato-1,2-diphenylethane content of at least 95% by weight, and 1,5-
naphthylene diisocyanate. Preference is given to using diphenylmethane diisocyanate
isomer mixtures having a 4,4'-diphenylmethane diisocyanate content of greater than 96
by weight and in particular essentially pure 4,4'-diphenylmethane diisocyanate.
b) Preferred polyhydroxy compounds (b) having molecular weights of from
500 to 8000 are polyetherols and in particular polyesterols. However, it is also possible
to use other hydroxyl-containing polymers cont~ining ether or ester groups as bridge
members, for example polyacetals, such as polyoxymethylenes and in particular water-
soluble formals, e.g. polybutanediol formal and polyhexanediol formal, and
polycarbonates, in particular those formed from diphenyl carbonate and 1,6-hexanediol,
prepared by transesterification. The polyhydroxy compound must be at least
2 ~ 3 ~
predominantly linear, i.e., difunctional within the meaning of the isocyanate reaction.
The polyhydroxy compounds mentioned may be used as individual components or in the
form of mixtures.
Suitable polyetherols can be prepared from one or more alkylene oxides having
from 2 to 4 carbon atoms in the alkylene moiety in a conventional manner, for example
by anionic polymerization with alkali metal hydroxides, such as sodium hydroxide or
potassium hydroxide, or alkali metal alcoholates, such as sodium methoxide, sodium
ethoxide, potassium ethoxide or potassium isopropoxide, as catalysts and in the presence
of at least one initiator molecule which contains 2 to 3, preferably 2 reactive hydrogen
o atoms, or by cationic polymerization with Lewis acids, such as antimony pentachloride,
boron fluoride etherate, etc. or bleaching earth, as catalysts.
Preferred alkylene oxides are for example tetrahydrofuran, 1,3-propylene oxide,
1,2-butylene oxide, 2,3-butylene oxide and in particular ethylene oxide and 1,2-propylene oxide. The alkylene oxides may be used individually, alternately in succession
or as mixtures. Suitable initiator molecules are for example: water, organic dicarboxylic
acids, such as succinic acid, adipic acid and/or glutaric acid, alkanolamines, such as
ethanolamine, N-alkylalkanolamines, N-alkyldialkanolamines, e.g. N-methyl- and N-
ethyl-diethanolamine, and preferably dihydric alcohols which may contain ether linkages,
e.g. ethanediol, 1,2-propanediol, 1,3-propanediol, 1,4-butanediol, diethylene glycol, 1,5-
pentanediol, 1,6-hexanediol, dipropylene glycol, 2-methyl- 1,5-pentanediol and 2-ethyl-
1,4-butanediol. The initiator molecules may be used individually or as mixtures.
s 9
Preference is given to using polyetherols from 1,2-propylene oxide and ethylene
oxide in which more than 50%, preferably from 60 to 80%, or the OH groups are
primary hydroxyl groups and where at least some of the ethylene oxide units are present
as a terminal block. Such polyetherols can be obtained by, for example, polymerizing
5 onto the initiator molecule first the 1,2-propylene oxide and then the ethylene oxide, or
first the entire 1,2-propylene oxide mixed with some of the ethylene oxide and then the
remainder of the ethylene oxide, or step by step first some of the ethylene oxide, then the
entire 1,2-propylene oxide and then the remainder of the ethylene oxide.
Other preferred possibilities are the hydroxyl-containing polymerization products
of tetrahydrofuran.
The essentially linear polyetherols have molecular weights of from 500 to 8000,
preferably from 600 to 6000, in particular from 800 to 3500, the polyoxytetramethylene
glycols preferably having molecular weights of from 500 to 2800. They can be used not
only individually but also in the form of mixtures with one another.
Suitable polyesterols may be prepared for example from dicarboxylic acids of
from 2 to 12, preferably from 4 to 6, carbon atoms and polyhydric alcohols. Suitable
dicarboxylic acids are for example: aliphatic dicarboxylic acids, such as succinic acid,
glutaric acid, adipic acid, suberic acid, azelaic acid and sebacic acid, and aromatic
dicarboxylic acids, such as phthalic acid, isophthalic acid and terephthalic acid. The
20 dicarboxylic acids can be used individually or as mixtures, for example in the form of a
mixture of succinic acid, glutaric acid and adipic acid. To~ prepare the polyesterols it may
be advantageous to use instead of the dicarboxylic acids the co-les~onding dicarboxylic
~I&~
~ acid derivatives, such as dicarboxylic monoesters or diesters having from 1 to 4 carbon
atoms in the alcohol moiety, dicarboxylic anhydrides or dicarbonyl dichlorides.
Examples of polyhydric alcohols are glycols of from 2 to 10, preferably from 2 to 6,
carbon atoms, such as ethylene glycol, diethylene glycol, 1,4-butanediol, 1,5-pentanediol,
s 1,6-hexanediol, 1,10-decanediol, 2,2-dimethylpropane-1,3-diol, 1,3-propanediol and
dipropylene glycol. Depending on the pl ope~ lies which are desired, the polyhydric
alcohols may be used alone or optionally mixed with one another.
It is also possible to use esters of carbonic acid with the diols mentioned, in
particular those having from 4 to 6 carbon atoms, such as 1,4-butanediol and/or 1,6-
lo hexanediol, condensation products of ~-hydroxycarboxylic acids, e.g. a)-hydroxycaproic
acid, and preferably polymerization products of lactones, for example substituted or
unsubstituted ~-caprolactones.
Preferred polyesterols are ethanediol polyadipates, 1,4-butanediol polyadipates,ethanediol/1,4-butanediol polyadipates, 1,6-hexanediol/neopentylglycol polyadipates,
1,6-hexanediol/1,4-butanediol polyadipates and polycaprolactones.
The polyesterols have molecular weights of from 500 to 6000, preferably from
800 to 3500.
c) Suitable chain extenders (c) having molecular weights of from 60 to 400,
preferably from 60 to 300, are preferably aliphatic diols of from 2 to 12 carbon atoms,
preferably of 2, 4 or 6 carbon atoms, e.g. ethanediol, 1,6-hexanediol, diethylene glycol,
dipropylene glycol and in particular 1,4-butanediol. However, it is also possible to use
diesters of terephthalic acid with glycols of from 2 to 4 carbon atoms, e.g. bisethylene
.
glycol terephthalate, 1,4-butanediol terephthalate, and hydroyxalkylene ethers of
hydroquinone, e.g. 1,4-di-(13-hydroxyethyl)-hydroquinone, and also polytetramethylene
glycols having molecular weights of from 162 to 378.
To set the hardness and the melt flow index, the formative conlponents can be
s varied within relatively wide molar ratios bearing in mind that the hardness and melt
viscosity increase with an increasing level of chain extenders (c) while the melt flow
index decreases.
To prepare relatively soft TPUs A), which are especially preferred for use in the
instant invention, for example those having a Shore A hardness of less than 95,
o preferably from 95 to 70, it is advantageous to use the essentially difunctional
polyhydroxy compounds (b) and the diols (c) in a molar ratio of from 1:1 to 1: 5,
preferably from 1:1.5 t~ 1:4,5, so that the resulting mixtures of (b) and (c) have a hydroxy
equivalent weight of greater than 200, in particular form 239 to 450, while greater than
200, in particular form 239 to 450, while harder TPUs (a), for example those having a
1S Shore A hardness of greater than 98, preferably from 55 to 75 hardness of greater than
98, preferably from 55 to 75 Shore D, are plepaled using a molar ratios of (b):(c) within
the range of 1:5.5. to 1:15, preferably from 1:6 to 1:12, so that the resulting mixtures of
(b) and (c) have a hydroxy equivalent weight of from 110 to 200, preferably from 120 to
180.
d) Suitable catalysts, in particular for the reaction between the NCO groups
of the diisocyanates (a) and the hydroxyl groups of the formative components (b) and (c),
are the customary tertiary amines, such as triethylamine, dimethylcyclohexylamine, N-
8 ~
methylmorpholine, N,N'-dimethylpiperazine, diazabicyclo[2.2.-2]octane and the like, in
particular organic metal compounds such as titanic esters, iron compounds, tin
compounds, e.g. tin diacetate, tin dioctoate, tin dilaurate or the tin dialkyl salts of
aliphatic carboxylic acids such as dibutyltin diacetate, dibutyltin dilaurate and the like.
The catalysts are customarily used in amounts of from 0 001 to 0.1 parts by weight per
100 parts by weight of the mixture of polyhydroxy compounds (b) and diols (c).
In addition to catalysts, the formative TPU components may also contain aids (e)and/or additives (f). Examples are lubricants, inhibitors, stabilizers against hydrolysis,
flame retardants, dyes, pigments, inorganic and/or organic fillers and reinforcing agents
lo To prepare the TPUs A), the formative components (a), (b) and (c) are made to
react in the presence of a catalyst (d) and in the presence or absence of aids (e) and/or
additives (f) in such amounts that the equivalence ratio of the diisocyanate NCO groups
to the total number of hydroxyl groups of components (b) and (c) is from 0.95 to 1.10:1,
preferably 0.98 to 1.08:1, in particular approximately 1.0 to 1.05:1.
The TPUs A) which are usable according to the present invention and which
customarily contain from 8 to 20% by weight, preferably from 8 to 16% by weight,based on the total weight, of urethane groups and have a melt flow index at 210C. of
from 500 to 1, preferably from 100 to 1, can be prepared by the extruder technique or the
belt technique by batch wise or continuous mixing of formative components (a) to (d)
and optionally (e) and/or (f), reacting the mixture in an extruder or on a support belt at
from 60 to 250 C., preferably at from 70 to 150 C., and then granulating the resulting
TPUs A). The reactor extruder technique, such as is well known in the art is most
~ 8~9
preferred. It may be advantageous to heat the resulting TPU A) at from 80 to 120 C.,
preferably at from 100 to 110 C., for a period of from I to 24 hours before further
processing.
The one or more acrylate based rubbers B) of the composition generally
comprise an elastomeric graft copolymer with butadiene, butadiene/styrene,
butadiene/acrylonitrile and acrylic esters as described for example in DE-A-1 694 173
and DE-A-2 348 377.
Component B) will preferably be a grafl polymer formed from 50-90, preferably
60-80, % by weight of an acrylate rubber having a glass transition temperature of below -
o 20 C., as grafting base, and 10-50, preferably 20-40, % by weight of a copolymerizable
ethylenically unsaturated monomer whose homopolymers and copolymers have a
transition temperature of more than 35 C., as graft superstratum. With respect to graft
copolymers having a core/shell structure, the term 'grafting base' is understood to refer
to the composition of the core, while the term 'graft superstratum' is understood to refer
to the composition of the shell.
The grafting base comprises acrylate or methacrylate rubbers which may contain
0 to 40% by weight of further comonomers. The C~-C8-esters of acrylic or methacrylic
acid and halogenated derivatives thereof, and also aromatic acrylic esters and mixtures
thereof are preferred. Suitable comonomers for the grafting base are acrylonitrile,
methacrylonitrile, styrene, a-methylstyrene, acrylamides, methacrylamides and also
vinyl C,-C6 alkyl ethers.
13
218~59
The grafting base may be uncrosslinked or partially or completely crosslinked.
The crosslinking is produced by copolymerizing preferably 0.02-5% by weight, in
particular 0.05-2% by weight, of a crosslinking monomer having more than one double
bond. Suitable crosslinking monomers are described for example in DE-A-2726 256 and
s EP-A-50 265.
Preferred crosslinking monomers are triallyl cyanurate, triallyl isocyanurate,
triacryloylhexahydro-s-tria-zine and trialkylbenzenes.
If the crosslinking monomers have more than 2 polymerizable double bonds, it is
advantageous to limit their amount to not more than 1% by weight, based on the grafting
base.
Suitable grafting bases are emulsion polymers having a gel content of more than
60% by weight (as determined in dimethylformamide at 25 C. by the method of M.
Hoffman, H. Kromer, R. Kuhn, Polymeranalytik, George-Thieme-Verlag, Stuttgart,
1977).
Other suitable grafting bases are acrylate rubbers having a diene core, as
described for example in EP-A-50 262.
[insert most preferred core]
Suitable graft monomers are in particular styrene, ~-methylstyrene, acrylonitrile,
methacrylonitrile, methyl methacrylate and mixtures thereof, in particular mixtures of
styrene and acrylonitrile in a weight ration of 90/10 to 50/50. An especially preferred
graft monomer is methyl methacrylate.
14
. ~ I B8~59
The graft yield, i.e. the ratio of the amount of grafted-on monomer to the
amount of graft monomer used, is in general within the range from 20 to 80%.
Rubbers based on acrylates which may be used according to the present invention
are described for example in DE-A-2 444 S84 and DE-A-2 726 256. Particularly
s preferred acrylate rubbers are the Cl lo alkyl acrylates
It is of course the case that it is also possible to use mixtures of the
abovementioned types of rubber.
The graft superstratum may be produced in one or more, namely up to 4, stages.
The graft rubbers are prepared in a conventional manner by emulsion
o polymerization.
Most preferably, the one or more acrylate based rubbers B) will generally have
from 30 to 90%, and preferably from 40 to 85% of a Cl ~0 alkyl acrylate. Preferably, the
alkylacrylate will be a C, 6 alkyl acrylate and more preferably, either propyl, butyl, or
hexyl acrylate, with butyl being especially preferred. The 30 to 90% C~ ~0 alkyl acrylate
will generally be present in conjunction with one or more monomers selected from the
group consisting of styrene, acrylonitrile, vinyl acetate and/or Cl 6 alkylalmethacrylates.
Preferred monomers are acrylonitrile, styrene, and methyl methacrylate. Methyl
methacrylate is especially preferred Such monomers are generally present in amounts of
from 50 to 10% by weight and more particularly, 40 to 20% by weight.
As indicated above, most preferably, the one or more acrylate based rubbers B),
will be present in the form of a graft copolymer having a core/shell structure. Those
skilled in the art will appreciate that in such a structure, the 30 to 90% C~ ~0 alkylacrylate
2 1 8~059
.
will generally form the partially or totally crosslinked inner core structure, with the one
or more monomers selected from the group consisting of styrene, acrylonitrile, vinyl
acetate, and/or C, 6 alkyl methacrylates forming the enveloping outer shell structure.
Examples of suitable commercially available materials are those from Rohm &
s Haas' Paraloid~l line, especially KM 334, KM 390, EXL 3330 and EXL 3361.
The most preferred corelshell graft products may be obtained via polymerization of
the foregoing monomers in the presence of an elastomer component prepared in a
sèparate polymerization step. The graft products may be produced by non-
polymerization processes, including emulsion, suspension and bulk polymerization and
o combinations of these processes.
Alternatively, the one or more acrylate based rubbers may be in the form of
copolymers or terpolymers. It will be appreciated by those skilled in the art that in
general such materials will not have the preferred core/shell structure discussed above.
An example of an illustrative commercially available material is Goodyear Chemicals'
I S Sunigum~2.
The one or more W and/or heat stabilizers C) are additives which will
preferentially absorb and dissipate energy by relieving excited molecules of excess
energy and releasing it as heat. In general, the stabilizers preferred for use herein will be
effective in the range of from 300 to 360 nm. An example of suitable W and heat
20 stabilizers are derivatives of o-hydroxybenzophenone, o-hydroxyphenyl salicylates, 2-
(o-hydroxyphenyl)-benzotriazoles, and hindered phenols.
1 Pa~loid~ is a regislered l~ld~ k of Rohm & Haas
2 Sll~ligllllt(~9 iS a registered l~del.~h of Goodvear Chemical
16
218~
Also suitable for use herein as W and heat stabilizers are hindered amine light
stabilizers.
Preferred W stabilizers are those having active ingredients which are sterically
hindered benzotriazol type stabilizers. It will be appreciated that many W stabilizers are
5 concentrates containing other materials in addition to the active ingredient. Particularly
preferred active ingredients for W and heat stabilizers are 2-(2-hydroxy-3,5-di-tert-
amyl-phenyl)-2H-benzotriazole, 1,6-hexanediylbis(3-benzotriazol-N-yl)-4-hydroxy-5-
tert-butyl) phenyl propionate, and mixtures thereof.
In particular, the most preferred one or more W and/or heat stabilizers C) for use
o in the instant invention will be stabilizer concentrates cont~ininF the aforementioned
most preferred active ingredients. Such stabilizer concentrates will preferably further
contain thermoplastic polyurethanes (TPU) and 1,3,5-triglycidyl-isocyanurate. Such
stabilizer W stabilizer concentrates are discussed in DE 4211335 A, herein incorporated
by reference. The most preferred W and heat stabilizer concentrates will contain
approximately 40 to 80 weight percent of thermoplastic polyurethanes, 10 to 30 weight
percent 1,3,5-triglycidyl-isocyanurate and 10 to 30 weight percent 2-(2-hydroxy-3,5-di-
tert-amyl-phenyl)-2H-benzotriazole, 1,6-hexanediylbis(3-benzotriazol-N-yl)-4-hydroxy-
5-tert-butyl) phenyl propionate, or mixtures thereof.
In addition, the thermoplastic polyurethane compositions of the invention may
20 further optionally contain one or more compatibilizers D). Such compatibilizers are
generally comprised of copolymers formed from styrene, alpha-methylstyrene,
acrylonitrile, methacrylonitrile, butadiene, acrylate, and mixtures thereof. Preferred
~1 8805'~
compatibilizers are poly(styrene-acrylonitrile) and ABS. Especially preferred is
poly(styrene-acrylonitrile).
Finally, the thermoplastic polyurethane compositions of the invention may further
optionally contain additives E) selected from the group consisting of lubricants,
s inhibitors, stabilizers against hydrolysis, flame retardants, dyes, pigments, inorganic
and/or organic fillers and reinforcing agents. Particularly preferred additives E) are dyes
and pigments. Titanium dioxide is a commonly used pigment. Of course, those skilled
in the art will appreciate that the incorporation of such dyes and pigments depends upon
the desired appearance of the end use application.
lo With respect to the foregoing components of the thermoplastic polyurethane
compositions of the invention, such compositions will preferably contain from 50 to
100% of one or more thermoplastic polyurethanes A), from greater than 10 to 49% of
one or more acrylate based rubbers B), and from 0.1 to 5.0% of active ingredients of one
or more W and/or heat stabilizers C), as based on the total combined weight of A), B)
1S and (C).
More preferably, the thermoplastic polyurethane compositions of the invention
will contain from 60 to 80% of one or more thermoplastic polyurethanes A), from greater
than 20 to 40% of one or more acrylate based rubbers B), and from 1.0 to 4.0% of active
ingredient of one or more W and/or heat stabilizers C), as based on the total combined
20 weight of A), B) and C).
If the thermoplastic polyurethane composition of the invention also comprise
compatibilizing polymer D), such polymer D) should be present in an amount of from I
18
0 $ 9
to 10% as based on the total weight of A), B), C) and D). More preferably, the
thermoplastic polyurethane composition comprising compatibilizing polymer D) will
contain less than 5% of polymer D), and most preferably, will comprise from 2 to 4% of
compatibilizing polymer D). It will be appreciated that additives E) will be present in
amounts dependent upon the desired end p.ope, lies of the molded articles.
It will be appreciated that in the instant invention, the thermoplastic polyurethane
composition is a blend wherein the predominant matrix is comprised of thermoplastic
polyurethane A). Dispersed in said matrix are particles of one or more acrylate based
rubbers B). If present, compatibilizing polymer D) will serve as the interface between
lo said acrylate based rubber particles and the TPU matrix. Also interspersed within the
matrix TPU will be UV and/or heat stabilizers C). It will be appreciated by those skilled
in the art that the incorporation of materials B) and C) will ideally not detract from the
performance properties of TPU A).
Molded thermoplastic polyurethane articles made of the thermoplastic
polyurethane compositions of the invention may be made by introducing the
compositions disclosed herein into a mold such as those known to those skilled in the art
and subjecting the composition to processing temperatures such as those disclosed above.
The composition will be maintained in the mold subject to said elevated heating
conditions for a time sufficient to result in a molded article.
In general, molded thermoplastic polyurethane articles made of thermoplastic
polyurethane compositions of the invention should have a Shore hardness of from 60A to
74D, and most preferably from 65A to 95A. The articles should further have a modulus
~1 8~S~
(300%) of from 750psi to 5000 psi and most preferably from 1200 psi to 3000 psi while
the 100% modulus of the molded articles of the invention should be from 500 psi to 5000
psi, and most preferably from 750 psi to 2000 psi. The elastic modulus should be from
750 psi to 6000 psi, and most preferably from 1000 psi to 4000 psi, while the percent
s elongation should be from 250 % to 1000% and most preferably from 400% to 800%.
With respect to heat stability measurements, such will generally be measured as
indicated in the following working examples. In particular, delta E should be measured
versus white tile provided by the manufacturer of an applupriate spectrophotometer as
illustrated below. Initial measurements should be post molding. Ideally, delta E versus
o white tile after molding should be as low a number as possible, and preferably less than
10, and most preferably less than 8 and preferably less than or equal to 6.
In addition, heat stability should be measured as delta E versus white tile after 14
days at 100C, i.e. after accelerated testing. This number should preferably be less than
18 and most preferably less than or equal to 15 with numbers less than or equal to 14
being most preferred.
In addition to the foregoing heat stablity values, those skilled in the art willappreciate that the difference between (delta E vs white tile after molding) and (delta E
vs white tile after 14 days at 100 degrees C) is particularly important with respect to
desireable performance. This difference, which for the purposes of the instant invention
may be termed 'delta HS', should be as small as possible, with desireable delta HS
values being less than or equal to 10, but preferably less than 8, and most preferably less
than 5.
.. ~ ,
2 1 ~059
With respect to measurements of W stability, such should be measured using a
commercially available QW instrument provided by Q Panel. Delta E versus white tile
aRer 1000 hours of QW is an approp~ iate measurement of W stability. Delta E values
should be less than 20, preferably less than 15 and ideally less than or equal to 10.
In addition to the foregoing UV stablity values, those skilled in the art will
appreciate that the difference between (delta E vs white tile after molding) and (delta E
vs white tile after 1000 hours QUV) is particularly important with respect to desireable
performance. This difference, which for the purposes of the instant invention may be
terrned 'delta WS', should be as small as possible, with desireable delta WS values
o being less than or equal to 8, but preferably less than 6, and most preferably less
than or equal to 4.
Finally, it will be appreciated that the sum of both delta HS and delta WS will
ideally be minimized as much as possible. Such minimi7ed values represent an optimum
level of both W and heat stability.
The invention will now be illustrated by the following working examples, which
are not to be construed as limiting the scope of the invention.
WORKING EXAMPLES
Ellastollan~3 El 180A-IO,E1 180A-50, and E1 185A-10 are commercially
available TPU compositions available from BASF Corporation of Wyandotte, Michigan
All three TPU compositions comprise the reaction product of polyetherols and aromatic
3 Ellastolan~ is a registered trademark of Elasto~am Gmbh.
2188~5~
-
isocyanates. Tinuvin 328 is a commercially available W stabilizer. The TiO2 used was
commercially available from DuPont as TI PURE R-103.
Sample preparation
All ingredients were mixed in a mixer to fonn a dry blend. The dry blend was
5 extruded by a Brabender twin-screw mixer (L/d=15/1) and pelletizing die (~ 75 rpm
with the following temperab~re profile.
Zone # 1: 370 F
Zone #2: 380F
Zone #3: 390F
o Die: 390F
Melt: 400-41 OF
The blends were injection molded into 4"x6"xO.08" plaques on a Cincinnati 110-
ton machine with the following temperature profile:
Zone#l: 370F
Zone #2: 380F
Zone #3: 390F
Noz71e: 400F
Table 1
Example #I E~ample #2 Exnmple #3 Example #4 E~ample #S E~ample #6 El~mple #7
Comp. A E1180A- 10 E 1180A- 10 E 1180A-50E 1180A-50 E 1180A-50 E 1180A-50 E 1185A- 10
(TPU) (100 wt%) (100 wt%) (80 wt%) (60 wt%) (80 wt%) (60 wt%) (100 ~%)
Comp B None None PVC (Apex PVC (ApexAcrylic RubberAclylic Rubber None
(other polymer 584, 20 584, 40 (Paraloid EXL-(Paraloid EXL-
vlt%) wt%) 3330, 20 wt%)3330, 40 ~vt%)
Comp C NoneTinuvin 328Tinuvin 328Tinuvin 328 Tinuvin 328 Tinuvin 328 Conc. 929
(UV stabilizer) (3.S phr) (3.5 phr)(3.5 phr) (2.8 phr) (2.1 phr) (4 phr)
Comp E Tio2 TiO2 TiO2 TiO2 TiO2 TiO2 TiO.
(pigment) (2.5phr) (2:5phr) (2 5 phr)(2.5 phr) (2.5 phr) (2-5 phr) (2.5 phr)
21 ~8059
The plaques prepared in Examples 1-7 were tested for heat and W
- resistance/stability according to the following test parameters. Hardness was tested per
ASTM D2240 and tensile plope- ~ies per ASTM D4 12.
W Stability
s W stability was measured on QW Testing Equipment commerially available
from Q-PANEL with a W A-35 1 lamp according to ASTM G-53. The test cycles were
of 4 hrs W exposure ~ 60 C, followed by 4 hrs condensation (~ 50 C.
Heat Stability
Heat stability was measured on a DATACOLOR 3890 Spectrophotometer with a
lo port #27 viewing port. White Tile provided by DATACOLOR was used as the standard
for delta E calculation.
Table 2
aE vs. white 6 7 14 12 6 6 5
tile af~er
molded
~E vs. whi~e 36 15 14 14 10 9 15
tile afler 1000 ` --
hrs of QW
~E vs. white N/A 15 30 30 14 13 N/A
tile after 14
days ~ 100 C
~lardness 80 78 81 84 82 83 87
(Shore A)
300% Modulus1500 1600 1780 1360 1590 1620 1600
(Psi)
100% Modulus800 790 910 980 780 810 950
(Psi)
Elastic 1700 1360 1740 2480 1640 2280 2700
Modulus (psi)
Elongation(%) 600 870 630 520 690 590 650
