Thermoplastic polyurethane molding composition

A thermoplastic molding composition was composed of PA0 A: 20-90% by weight of a thermoplastic polyurethane, PA0 B: 1-40% by weight of an elastomeric graft copolymer formed from PA0 b.sub.1 : 50-90% by weight of a grafting base comprising an elastomeric polymer which has a glass transition temperature of below -20.degree. C. and is based on butadiene or a C.sub.2 -C.sub.10 -acrylate and, if desired, a crosslinking agent and PA0 b.sub.2 : 10-50% by weight of a graft superstratum formed from styrene and acrylonitrile in the ratio of from 85:15 to 60:40 or styrene or methyl methacrylate, and PA0 C: 5-75% by weight of a copolymer formed from PA0 c.sub.1 : 55-90% by weight of .alpha.-methylstyrene and PA0 c.sub.2 : 10-45% by weight of acrylonitrile or methacrylonitrile or a mixture thereof, and PA0 D: up to 50% by weight of a reinforcing filler.

It is known that thermoplastic polyurethanes (TPUs) can be blended with 
copolymers of styrene, butadiene and acrylonitrile (ABS copolymers). 
Blends of ABS and TPU are described in U.S. Pat. Nos. 3,049,505 and 
4,179,479. There the ABS polymers always consist of styrene, acrylonitrile 
and butadiene. The molding compositions obtained show insufficient notched 
impact strength at low temperatures and incompatibility at high processing 
temperatures. 
We have found that replacing the styrene in copolymers of styrene, 
acrylonitrile and butadiene by .alpha.-methylstyrene dramatically improves 
the compatibility of blends with TPU and leads to molding compositions of 
excellent low-temperature notched impact strength. 
The present invention accordingly provides a thermoplastic molding 
composition composed of 
A: 20-90% by weight of a thermoplastic polyurethane A, 
B: 1-40% by weight of an elastomeric graft copolymer B formed from 
b.sub.1 : 50-90% by weight of a grafting base b.sub.1 comprising an 
elastomeric polymer which has a glass transition temperature of below 
-20.degree. C. and is based on butadiene or a C.sub.2 -C.sub.10 -acrylate 
and, if desired, a crosslinking agent and 
b.sub.2 : 10-50% by weight of a graft superstratum b.sub.2 formed from 
styrene and acrylonitrile in the ratio of from 85:15 to 60:40 or styrene 
or methyl methacrylate, and 
C: 5-75% by weight of a copolymer formed from 
c.sub.1 : 55-90% by weight of .alpha.-methylstyrene (c.sub.1) and 
c.sub.2 : 10-45% by weight of acrylonitrile or methacrylonitrile (c.sub.2) 
or a mixture thereof, and 
D: up to 50% by weight of a reinforcing filler D. 
In component b.sub.2, the .alpha.-methylstyrene may replace all or some of 
the styrene. The graft superstratum may be formed in more than one stage. 
The present invention also relates to the use of such molding compositions 
for preparing moldings and to moldings obtained from the molding 
compositions according to the present invention as essential components. 
Component A of the molding compositions according to the invention 
comprises from 20 to 90, preferably from 30 to 70, % by weight of 
thermoplastic polyurethane. 
The thermoplastic polyurethanes (component A) are known. They are 
essentially formed from long-chain polyols of molecular weight 400-10,000, 
poly(preferably di)isocyanates and chain extenders (preferably short-chain 
polyols having a molecular weight of up to for example 380), in which the 
equivalent ratio of isocyanates to the Zerewitinoff active H atoms (here 
called the NCO/OH ratio) is preferably set in the range from 0.95 to 1.10, 
particularly preferably from 0.98 to 1.08. 
Suitable essentially linear polyols having molecular weights of from 400 to 
10,000, preferably from 800 to 6,000, for the purposes of the present 
invention are virtually all those compounds known per se which contain 
preferably 2 or even--in minor amounts--3 Zerewitinoff active groups 
(essentially hydroxyl groups) such as polyesters, polylactones, 
polyethers, polythioethers, polyester amides, polycarbonates, polyacetals, 
vinyl polymers, eg. polybutadienediols, polyhydroxy compounds which also 
contain urethane or urea groups, modified or unmodified natural polyols 
and also those compounds which contain other Zerewitinoff active groups 
such as amino, carboxyl or thiol groups. These compounds are described, 
for example, in detail in German Laid-Open Applications DOS 2,302,564, DOS 
2,423,764 and DOS 2,549,372 (U.S. Pat. No. 3,963,679) and DOS 2,402,840 
(U.S. Pat. No. 3,984,607) and also German Published Application DAS 
2,457,387 (U.S. Pat. No. 4,035,213). According to the present invention, 
preference is given to hydroxyl-containing polyesters formed from glycols 
and adipic acid, phthalic and/or terephthalic acid and the hydrogenation 
products thereof, polycaprolactones, polyethylene oxide, polypropylene 
oxide, polytetrahydrofuran and copolyethers thereof. Particular preference 
is given to polyesters formed from glycols, adipic acid and 
polytetrahydrofuran. 
Diisocyanates to be used according to the present invention are the 
aliphatic, cycloaliphatic, aromatic, araliphatic and heterocyclic 
diisocyanates as described for example in German Laid-Open Applications 
DOS 2,302,564, DOS 2,423,764, DOS 2,549,372, DOS 2,402,840 and DOS 
2,447,387. The diisocyanates which are preferred according to the present 
invention are unsubstituted or methyl-substituted hexamethylene 
diisocyanate, isophorone diisocyanate, diphenylmethane diisocyanate and 
naphthylene 1,5-diisocyanate. 
The diisocyanates mentioned may be used together with up to about 15 mol % 
(based on diisocyanate) of a higher polyisocyanate; the amount of higher 
polyisocyanate, however, must be limited so as to produce a still fusible 
or thermoplastic product. A larger amount of higher isocyanate must in 
general be balanced by using on average less than difunctional hydroxy and 
amino compounds (or by including monoisocyanates) to prevent excessive 
chemical crosslinking of the product. Examples of higher isocyanates and 
monofunctional compounds may likewise be found in the above-cited prior 
art. Examples of monoamines such as butylamine, dibutylamine, octylamine, 
stearylamine, N-methylstearylamine, pyrrolidone, piperidine and 
cyclohexylamine and also monoalcohols such as butanol, 1-ethylhexanol, 
octanol, dodecanol, amyl alcohols, cyclohexanol and ethylene glycol 
monomethyl ether. Said monofunctional compounds can also be used as 
regulators. 
Similarly, the chain extenders which are usable according to the present 
invention are known and described for example in German Laid-Open 
Applications DOS 2,302,564, DOS 2,423,764, DOS 2,549,372, DOS 2,402,799, 
DOS 2,402,840 and DOS 2,457,387. They are low molecular weight 
polyalcohols (preferably glycols), polyamines, hydrazines and hydrazides. 
It is also possible to use aminoalcohols such as ethanolamine, 
diethanolamine, N-methyldiethanolamine, triethanolamine and 
3-aminopropanol according to the present invention. Preferred chain 
extenders are ethylene glycol, diethylene glycol, triethylene glycol, 
1,4-butanediol, 1,6-hexanediol and hydroquinone di-.beta.-hydroxyethyl 
ether. Particular preference is given to hydroquinone 
di-.beta.-hydroxyethyl ether, 1,4-butanediol and 1,6-hexanediol. 
The polyurethane components may of course be stabilized with the usual 
hydrolysis and oxidation stabilizers of the prior art. 
It is also advisable to add to the graft rubber antioxidants such as 
2,6-di-tert-butyl-4-methylphenol, other sterically hindered phenols or 
other customary antioxidants alone or mixed in an amount of about 0.1-1.5% 
by weight, based on the total blend. These additions may be incorporated 
either in the graft rubber or in the polyurethane. 
A review of thermoplastic polyurethanes and their properties and 
applications is given for example in Kunststoffe 68 (1978), 819-825 and in 
Kunststoff-Handbuch, Volume 7, Polyurethanes, 2nd edition, edited by Dr. 
G. Oertel (Carl Hanser Verlag, Munich, Vienna 1983). 
They can be prepared continuously or batchwise by various processes. The 
best known ones, which are also used in industry, are the belt process and 
the extruder process; the belt process, which is preferred, proceeds as 
follows: 
According to GB-A-1 057 018, the polyhydroxy compound and excess organic 
diisocyanate are combined to prepare a prepolymer which is fed by a 
metering pump into a mixing head where it is mixed with a certain amount 
of low molecular weight diol. The reaction mixture obtained is fed onto a 
conveyor belt and passed through an oven at 70.degree.-130.degree. C. 
until it solidifies. The reaction product is then comminuted and 
heat-treated at up to 120.degree. C. for 6-40 hours. 
Component B of the molding compositions comprises 5-40, preferably 10-30, % 
by weight of 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. 
Of these, particularly suitable ones are the ABS polymers described in 
DE-A-2 035 390, DE-A-2 248 242 and EP-A-22 216, the last being 
particularly preferred. 
Component B) may also be a graft polymer formed from 
50-90, preferably 60-80, % by weight of an acrylate rubber having a glass 
transition temperature of below -20.degree. 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.degree. C., as graft superstratum. 
The grafting base comprises acrylate or methacrylate rubbers which may 
contain up to 40% by weight of further comonomers. The C.sub.1 -C.sub.8 
-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, .alpha.-methylstyrene, acrylamides, 
methacrylamides and also vinyl C.sub.1 -C.sub.6 alkyl ethers. 
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-2 726 256 and EP-A-50 265. 
Preferred crosslinking monomers are triallyl cyanurate, triallyl 
isocyanurate, triacryloylhexahydro-s-triazine 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. 
Particularly preferred grafting bases are emulsion polymers have a gel 
content of more than 60% by weight (as determined in dimethylformamide at 
25.degree. C. by the method of M. Hoffman, H. Kromer, R. Kuhn, 
Polymeranalytik, Georg-Thieme-Verlag, Stuttgart, 1977). 
Other suitable grafting bases are acrylate rubbers having a diene core, as 
described for example in EP-A-50 262. 
Suitable graft monomers are in particular styrene, .alpha.-methylstyrene, 
acrylonitrile, methacrylonitrile, methyl methacrylate and mixtures of, in 
particular mixtures of styrene and acrylonitrile in a weight ration of 
90/10 to 50/50. 
The graft yield, ie. 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-2 444 584 and DE-A-2 726 256. 
The rubbers on a butadiene basis preferably have a glass transition 
temperature of below -40.degree. C., in particular below -50.degree. C., 
which results in good impact strength even at low temperatures. 
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 
polymerization. 
Component C of the molding compositions according to the present invention 
comprises from 5 to 75, preferably from 10 to 60 and in particular from 10 
to 40, % by weight of copolymers formed from 
c.sub.1) 55-90, preferably 60-90 and in particular 75-90, % by weight of 
.alpha.-methylstyrene and 
c.sub.2) 10-45, preferably 10-40 and in particular 10-25, % by weight of 
acrylonitrile and/or methacrylonitrile. 
Such products can be prepared for example by the process described in 
DE-B-1,001,001 and DE-B-1,003,436. Such copolymers are also commercially 
available. Preferably, the light scattering weight average molecular 
weight is within the range from 50,000 to 500,000, in particular from 
70,000 to 250,000. 
The weight ration of B:C is within the range from 1:3 to 3:1, preferably 
from 1:2 to 2:1, in particular from 1:1.5 to 1.5:1. 
Up to 50% of the .alpha.-methylstyrene may be replaced by other 
unsubstituted or substituted styrenes, eg. styrene or p-methylstyrene. 
Suitable reinforcing fillers D are for example mineral fillers such as 
wollastonite, talcum, kaolin or SiO.sub.2, preferably glass fibers. Glass 
fibers find application for example in the form of glass weaves, mats, 
webs and/or preferably glass filament rovings or cut glass filament made 
of low-alkali E-glasses having a diameter of 5 to 200 .mu.m and preferably 
from 6 to 15 .mu.m, and after incorporation the average length is from 0.5 
to 1 mm, preferably from 0.1 to 0.5 mm. 
Other suitable fillers are for example wollastonite, calcium carbonate, 
glass spheres, quartz powder, silicon nitride, boron nitride and mixtures 
thereof. 
Of the aforementioned reinforcing fillers, in particular glass fibers have 
proven advantageous, in particular when high heat distortion resistance or 
very high stiffness is required. 
The proportion of component D is from 0 to 60, preferably from 2 to 50, in 
particular from 5 to 30, % by weight, based on the total weight of the 
molding compositions. 
Besides components A to D the molding compositions according to the present 
invention may contain customary additives and processing aids. The amount 
thereof is in general up to 20, preferably up to 10, % by weight, based on 
the total weight of components A to D. 
Customary additives are for example stabilizers, antioxidants, agents 
against thermal decomposition and decomposition by ultraviolet light, 
lubricants, release agents, colorants, such as dyes and pigments, 
nucleating agents and plasticizers. 
Antioxidants and heat stabilizers which may be added to the thermoplastic 
compositions according to the present invention are for example sterically 
hindered phenols, hydroquinones, substituted representatives of this group 
and mixtures thereof, preferably in concentrations of up to 1% by weight, 
based on the weight of the mixture. 
Examples of UV stabilizers are various substituted resorcinols, 
salicylates, benzotriazoles and benzophenones, which in general are used 
in amounts of up to 2.0% by weight. 
Lubricants and release agents, which in general are added to the 
thermoplastic composition in amounts of up to 1% by weight, are C.sub.12 
-C.sub.36 -fatty acids, fatty alcohols, fatty acid esters and amides and 
also montan ester waxes. 
It is also possible to add organic dyes, such as nigrosine, pigments, eg. 
titanium dioxide, cadmium sulfide, cadmium sulfide selenide, 
phthalocyanines, ultramarine blue or carbon black. Nucleating agents, such 
as talcum, can be used in amounts of up for example 5% by weight, based on 
components A to D. 
The molding compositions according to the present invention can be prepared 
in a conventional manner in customary mixing apparatus, such as extruders, 
kneaders and mixers, for example by incorporating components B and C and 
any D if used into the TPU at 190.degree.-250.degree. C., in particular 
210.degree.-240.degree. C. 
The molding compositions according to the present invention are easily 
convertible into moldings which combine good surface characteristics and 
improved impact strength with high stiffness, in particular at low 
temperatures. There is no separation of the polymer components either in 
the molding or in the melt.

EXAMPLES 
Thermoplastic molding compositions according to the present invention were 
prepared using the following starting materials (the stated amounts and 
ratios are by weight, as in the rest of the text). 
A1) Thermoplastic polyurethane based on butanediol adipate (molecular 
weight 2,000), determined from the OH number: MDI and 1,4-butanediol 
having an NCO/OH ratio of 1.00 and a Shore D hardness of 59. 
A2) same as A1) except NCO/OH=1.04 
A3) same as A1) except Shore 64D 
A4) same as A1) except Shore 90A 
A5) same as A1) except based on a butanediol/ethylene glycol adipate having 
a butanediol/ethylene glycol ratio of 1:1 
All the TPU polymers A1)-A5) additionally contain 1% of 
diisopropylphenylcarbodiimide, based on the polyester content. 
A6) same as A1), except based on p-THF having a molecular weight of 1,000 
g/mol, determined from the OH number. 
B1) Graft rubber comprising a grafting base (75% by weight) of poly(n-butyl 
acrylate) which has been reacted with butanediol diacrylate and a graft 
sheath (25% by weight) of a copolymer of styrene and acrylonitrile (weight 
ratio 75:25) prepared by emulsion polymerization in a conventional manner 
(median particle size d.sub.50 =450 nm). The median particle diameter 
d.sub.50, as the name implies, is that diameter on either side of which 
are the diameters of 50% by weight of the particles. 
B2) Graft rubber comprising a grafting base of polybutadiene (75%) and a 
graft sheath (25%) of a copolymer of styrene and acrylonitrile (weight 
ration 75:25) prepared by emulsion polymerization in a conventional manner 
(d.sub.50 =250 nm). 
B3) Graft rubber as in the case of B2 except with .alpha.-methylstyrene 
instead of styrene. 
B4) Graft rubber (d.sub.50 =240 .mu.m) comprising a grafting base of 
polybutadiene (70%), a first sheath of styrene (10%) and a second sheath 
of methyl methacrylate, n-butylacrylate and glycidyl methacrylate in a 
ratio of 89:1, prepared by emulsion polymerization. 
C1) Styrene-acrylonitrile copolymer having an S/AN ratio of 65:35 and a 
viscosity number (VN) of 80, measured in 0.5% strength DMF at 25.degree. 
C. 
C2) same as C1) except for a VN of 60, measured in the same way as in the 
case of C1). 
C3) .alpha.-Methylstyrene-acrylonitrile copolymer having an .alpha.-MS/AN 
ratio of 70:30 and a VN of 58, measured in the same way as C1). 
D) E-glass fiber, roving or staple, diameter 10 .mu.m. 
The molding compositions were produced by intensively mixing the 
components, melting the mixture in a twin-screw extruder at 230.degree. C. 
and homogenizing the melt and extruding it into a waterbath. After 
granulation and drying, the mixture was injection molded at 230.degree. C. 
(compound temperature) into test specimens which were tested without 
further aftertreatment. If glass fibers were used, they were added to the 
homogenized melt in the form of staple or roving. 
The results are summarized in Tables 1 and 2 below. 
The notched impact strength was determined by IN 53 453, the impact 
strength by German Standard Specification DIN 53 453, the tensile 
strength, given in units of N/mm.sup.2, by German Standard Specification 
DIN 53 455, and the modulus of elasticity by German Standard Specification 
DIN 53 457. The heat distortion resistance is reported in terms of the 
Vicat B temperature, measured by German Standard Specification DIN 53 460. 
TABLE 1 
______________________________________ 
Tensile 
modulus 
Component of elasticity 
ak ak 
No. A B C (in N/mm.sup.2) 
-20.degree. C. 
-30.degree. C. 
______________________________________ 
1* 60 A1 10 B2 30 C2 650 12 5 
2* 60 A1 20 B2 30 C2 550 21 6 
3* 60 A3 10 B2 30 C2 900 10 4 
4 60 A1 10 B2 30 C3 650 32 11 
5 60 A1 10 B2 30 C3 550 54 19 
6 60 A3 10 B2 30 C3 900 31 9 
7 60 A2 20 B2 20 C3 540 58 23 
8 60 A4 20 B2 20 C3 420 no break 
34 
9 60 A5 20 B2 20 C3 590 48 14 
10 60 A6 20 B2 20 C3 500 no break 
39 
11 60 A1 20 B1 20 C3 570 36 5 
12 80 A1 10 B2 10 C3 450 60 35 
13 40 A1 30 B2 30 C3 1100 28 12 
14 40 A1 20 B4 20 C3 520 42 16 
______________________________________ 
*Comparative test 
TABLE 2 
______________________________________ 
Tensile 
mod- 
ulus 
Component of elas- 
ak ak 
No. A B C D ticity 
-20.degree. C. 
-30.degree. C. 
______________________________________ 
1* 48 A1 16 B2 16 C2 20 3600 14 5 
2 48 A4 16 B2 16 C3 20 3200 32 11 
3* 48 A1 16 B2 16 C3 20 3600 28 8 
4 48 A3 16 B2 16 C3 20 4200 18 6 
______________________________________ 
*Comparative test