Thermoplastic vulcanizates of carboxylated nitrile rubber and polyester thermoplastics

Low oil swell, processable carboxylated nitrile rubber thermoplastic vulcanizate compositions having high melting points are made utilizing a processing aid, for example, maleated polyethylene, and addition type curing agents such as bisoxazolines or bisimidazolines. The compositions generally contain polar thermoplastic high melting point crystalline polymers such as polyester as a continuous phase with the carboxylated nitrile rubber being dispersed therein.

FIELD OF INVENTION 
The present invention relates to thermoplastic vulcanizates (TPVs) 
containing high melting point thermoplastics such as polyesters, 
polycarbonates, or polyester block copolymers such as segmented 
polyester-ether copolymers, and small particles of cured carboxylated 
nitrile rubber dispersed therein. The present invention further relates to 
the use of processing aids and desirably addition type curing agents 
whereby the thermoplastic vulcanizates have properties similar to those of 
thermoset nitrile rubber. 
BACKGROUND OF THE INVENTION 
Heretofore, many types of thermoplastic vulcanizates were known. More 
specifically, U.S. Pat. No. 4,226,953 to Coran and Patel relates to 
thermoplastic compositions comprising blends of styrene-acrylonitrile 
(SAN) resin and nitrile rubber of high gel content. 
U.S. Pat. No. 4,141,863 to Coran et al. relates to a thermoplastic 
composition comprising blends of cross-linked rubber and thermoplastic 
linear crystalline polyester using thermoplastic polyesters having a 
softening point above 50.degree. C. Rubbers include natural or synthetic 
diene rubber polyurethane rubber and nitrile rubber. The blends may also 
contain plasticizers. 
U.S. Pat. No. 4,666,972 relates to polyalkylene terephthalates which 
contain a fluorinated polyolefin in addition to a polymer having a glass 
transition temperature of less than -30.degree. C. 
U.S. Pat. No. 5,397,839 relates to elastomeric compositions having improved 
heat aging properties provided by blends of thermoplastic polyester resin 
and hydrogenated nitrile rubber. The rubber component of the composition 
is at least partially cured. 
U.S. Pat. No. 5,550,190 to Hasegawa et al. relates to a thermoplastic 
elastomer composition obtained by dynamically crosslinking (A) 51-95% by 
weight of a thermoplastic polyester-ether elastomer and (B) 49-5% by 
weight of a rubber during kneading. 
U.S. Pat. No. 5,637,407 to Hert et al. relates to a composite including a 
rubber/thermoplastic blend adherent by itself to a thermoplastic material; 
the blend is in the form of a thermoplastic matrix containing rubber 
nodules functionalized and vulcanized during the mixing with the 
thermoplastic. Composite articles are obtained by overmoulding the 
vulcanized rubber/thermoplastic blend onto the thermoplastic. 
SUMMARY OF INVENTION 
The thermoplastic vulcanizate composition generally has a continuous phase 
of a thermoplastic having a melting point of at least about 170.degree. C. 
and a molecular weight sufficient to be considered an engineering plastic. 
A carboxylated nitrile rubber phase generally in the form of particles is 
made from acrylonitrile and a major amount of one or more conjugated diene 
monomers with butadiene or isoprene being preferred. Generally speaking, 
these compositions provide a product with poor processing characteristics. 
It was found that the addition of a processing agent allows the 
preparation of a processable thermoplastic product in contrast to the 
powdery products that are generally obtained in the absence of such 
agents. Curatives include phenolic resins, and addition type curing agents 
such as bisoxazolines and bismaleimides. The various components are 
dynamically vulcanized at a temperature above the melting point of the 
thermoplastic or the thermoplastic elastomer. 
DETAILED DESCRIPTION 
The thermoplastic polymers are desirably polar, crystalline, and have high 
melting points. The melting point of the thermoplastic polymers is 
desirably at least 170.degree. C., desirably at least 200.degree. C. and 
preferably at least 220.degree. C. Excessively high melt temperatures are 
avoided inasmuch as during melt mixing of the thermoplastic with the 
carboxylated nitrile rubber, the high melt temperature will degrade the 
nitrile rubber. Accordingly, the thermoplastic generally has a high 
melting point below 260.degree. C., and more desirably below 240.degree. 
C. Suitable thermoplastic polymers include polyesters, polycarbonates, 
block copolymers of polyester, and the like. 
Polyesters are condensation polymers. The various polyesters can be either 
aromatic or aliphatic or combinations thereof and are generally directly 
or indirectly derived from the reactions of diols such as glycols having a 
total of from 2 to 6 carbon atoms and desirably from about 2 to about 4 
carbon atoms with aliphatic acids having a total of from about 2 to about 
20 carbon atoms and desirably from about 3 to about 15 carbon atoms or 
aromatic acids having a total of from about 8 to about 15 carbon atoms. 
Generally, aromatic polyesters are preferred such as 
polyethyleneterephthalate (PET), polytrimethyleneterephthalate (PTT), 
polybutyleneterephthalate (PBT), polyethyleneisophthalate, and 
polybutylenenapthalate. 
Various polycarbonates can also be utilized and the same are esters of 
carbonic acid. A suitable polycarbonate is that based on bisphenol A, 
e.g., poly(carbonyldioxy-1,4-phenyleneisopropylidene-1,4-phenylene). 
Suitable polyester block copolymers include segmented polyester-polyether 
and the like. These block copolymers contain at least one block of a 
polyester and at least one rubbery block such as a polyether derived from 
glycols having from 2 to 6 carbon atoms, e.g., polyethylene glycol, or 
from alkylene oxides having from 2 to 6 carbon atoms. A preferred block 
polyester-polyether polymer is 
polybuty-leneterephthalate-b-polytetramethylene glycol which is available 
as Hytrel from DuPont. 
The molecular weight of the various thermoplastic resins is such that it is 
a suitable engineering plastic. Accordingly, the weight average molecular 
weight of the various polyesters generally range from about 40,000 to 
above 110,000 with from about 50,000 to about 100,000 being preferred. 
The rubber phase of the thermoplastic vulcanizate composition of the 
present invention comprises carboxylated nitrile rubber. Such rubber 
desirably has a small particle size below 50 microns and preferably from 
about 1 to 10 microns to yield good physical properties and processing 
characteristics. Nitrile rubbers are generally derived from conjugated 
dienes having from 4 to 8 carbon atoms with isoprene being desired and 
butadiene being preferred, and from acrylonitrile. The amount of the 
conjugated diene content within the copolymer is generally a majority, 
that is, from about 50 to about 80 percent by weight, and desirably from 
about 60 to about 75 percent by weight. The acrylonitrile content of the 
copolymer is thus the corresponding minority amount, i.e., from about 20 
percent to about 50 percent by weight and preferably from about 25 to 
about 40 percent by weight. The actual amount of acrylonitrile will vary 
depending upon end use application since increased amounts of 
acrylonitrile improve oil resistance, tensile strength, hardness and 
abrasion resistance. However, increased amounts of acrylonitrile in 
nitrile rubber will adversely affect the low temperature properties. 
The nitrile rubbers utilized in the present invention contain pendant 
carboxyl groups thereon such as those derived from unsaturated acids, for 
example, acrylic acid, methacrylic acid, and the like. The amount of 
carboxylic acid monomer copolymerized in the nitrile rubber is generally 
from about 1 to about 10 parts by weight and preferably from about 3 to 
about 7 parts by weight based upon 100 parts by weight of the nitrile 
rubber derived from acrylonitrile and the conjugated diene monomers. Upon 
cure, the carboxylated nitrile rubber can be cross-linked via the 
unsaturation present in the copolymer, or alternatively via the pendent 
car- boxylic acid groups. 
The amount of the nitrile rubber utilized in the present invention 
generally ranges from about 50 to about 400 parts by weight, desirably 
from about 200 to about 375 parts by weight, and preferably from about 230 
to about 360 parts by weight for every 100 parts by weight of the one or 
more thermoplastic polymers. 
Heretofore, polar thermoplastic vulcanizate compositions containing 
carboxylated nitrile rubber in absence of a processing aid generally 
formed a powder during processing, such as at a 1 to 3 plastic to rubber 
ratio. It has now been unexpectedly found that when a processing aid is 
added to the composition during mixing and before curing, substantial 
improvement in processability results. For example, powder formation is 
prevented and the product obtained is a processable thermoplastic 
material. It is also noted that bisoxazoline grafting of the plastic 
polymer onto the rubber via the end groups of the plastic and the 
carboxylic acid cure sites in the rubber may occur during TPV formation. 
This compatibilizing agent that can be formed in situ would also 
contribute to TPV mechanical properties. 
The processing aids, which further act as a bulk compatiblizing agent, is 
generally a hydrocarbon polymer and optionally but preferably such 
polymers which have functional groups thereon, e.g., preferably pendant 
therefrom. Such hydrocarbon polymers include polyolefins derived from 
C.sub.2 to C.sub.8 monomers such as polyethylene or polypropylene. Another 
class of processing aids is the various copolymers of olefins with an 
unsaturated acid having a total of from 3 to about 10 carbon atoms such as 
maleic acid, acrylic acid, and the like with a suitable copolymer being 
poly(ethylene-acrylic acid). Ethylene-vinyl alcohol or ethylene vinyl 
acetate copolymers and the like are also suitable processing aids. Still 
another class of processing aids are various hydrocarbon based rubbers 
such as ethylene-propylene copolymers, ethylene-propylene-diene copolymers 
(i.e., EPDM), and the like. A still further class are various hydrocarbon 
block copolymers such as styrene-butadiene-styrene (e.g., the various 
Kraton.RTM. grades manufactured by Shell), styrene-ethylene-butene-styrene 
block copolymers, and the like. 
The functional group of the processing aid can generally include any group 
which can react with the polar group of the thermoplastic resin, or the 
carboxylated nitrile rubber, or the curatives set forth herein below. Such 
functional groups include hydroxyl groups, as in an ethylenevinyl alcohol 
copolymer, with acid groups or anhydride groups being preferred. The acid 
groups are generally obtained from unsaturated acids having from 3 to 10 
carbon atoms such as acrylic acid, methacrylic acid, maleic acid, fumaric 
acid, and the like. The anhydrides include the various anhydrides of the 
above acids with maleic anhydride being preferred. The amount of the 
entire functional compound is generally from about 0.2 to about 6 or 10 
percent by weight of the total weight of the above-noted processing aids. 
Preferred processing aids which also act as compatibilizing aids include 
maleated polyethylene, maleated polypropylene, an ethylene-acrylic acid 
copolymer, maleated styrene-ethylene-butene-styrene-block copolymers, 
maleated styrene-butadiene-styrene block copolymers, maleated 
ethylene-propylene rubber, blends and cured blends of polypropylene or 
polyethylene and EPDM rubber (e.g., Santoprene.RTM. having a hardness of 
from about 35 Shore A to about 50 Shore D), and the like. Maleated 
polyethylene, maleated ethylene-propylene rubber and maleated 
styrene-butadiene-styrene block copolymers are highly preferred. 
The amount of the processing and/or compatibilizing aids generally range 
from about 3 parts to about 30 parts by weight and preferably from about 5 
parts to about 20 parts by weight based upon 100 parts by weight of the 
thermoplastic resin. 
The utilization of the processing aids with the carboxyl containing nitrile 
rubbers results, after dynamic vulcanization, in the formation of a highly 
compatible blend wherein the thermoplastic or thermoplastic elastomer 
generally constitutes a continuous phase and the rubber particles 
constitute a discontinuous phase. However, other possible morphologies may 
exist. 
Another important aspect of the present invention is the utilization of 
addition type curatives which, do not break down the plastic phase and do 
not form volatile compounds such as water. While other curing agents can 
be utilized such as free radical generating compounds, the same are not 
desired and thus used in small amounts such as generally less than 1.0 
parts by weight and desirably less than 0.5 parts by weight based upon 100 
parts by weight of the carboxylated nitrile rubber. A highly preferred 
addition curative or cross-linking agent is the various oxazolines or 
oxazines such as those having the formula 
##STR1## 
wherein R or R' is an aliphatic or aromatic hydrocarbon group such as 
alkylene or arylene having 1 to 24 carbon atoms optionally substituted 
with one or more alkyl groups having 1 to 6 carbon atoms or substituted 
with an aryl group having 6 to 9 carbon atoms; n is 0 or 1, when n equals 
1 then X and Y are hydrogen atoms or independently an 2-oxazoline group or 
a 1,3-oxazine group, or a 2-oxazoline group or a 1,3-oxazine group and a 
hydrogen atom, with the remaining carbon atoms having hydrogen atoms 
thereon, p and q, independently, is 1 or 2, and when n equals 0 then R, X 
, and Y are nonexistent. Further, each oxazoline group of the above 
formula may optionally be substituted with an alkyl of 1 to 6 carbon 
atoms. Further descriptions of said polyvalent oxazolines are set forth in 
U.S. Pat. No. 4,806,588, herein incorporated by reference. Preferred 
oxazolines include 2,2'-bis(oxazoline-2), 
2,2'hexamethylenedicarbamoylbis(oxazoline-2), and 
1,3-phenylene-2,2'bis(oxazoline-2). 
Various bismaleimides as well as phenolic resins can also be used as 
curatives. Examples of bismaleimides include a bismaleimide based on 
methylene dianiline (e.g., Matrimid 5292A from Ciba-Geigy), a bismaleimide 
based on toluene diamine (e.g., HVA-2 from DuPont), and the like. The 
phenolic curing agents are well known to the art and literature and 
include polymers obtained by the polymerization of phenol with 
formaldehyde. The polymerization rate is pH dependent, with the highest 
reaction rates occurring at both high and low pH. A more detailed 
description of the preparation of phenolic resins is set forth in 
"Principles of Polymerization" 3rd Edition, George Odian, pages 125-131, 
John Wiley Sons, Inc., New York., N.Y., 1991, which is hereby fully 
incorporated by reference. Examples of specific phenolic resins include 
##STR2## 
such as SP-1045 where R is isooctyl and n is 1 to 12, and HRJ-1367 where R 
is t-butyl and n is from 1 to 10, from Schenectedy Chemicals. 
Other addition type curatives can be utilized including various isocyanates 
such as 1,4-phenylenediisocyanate, isophorone diisocyanate, and .alpha., 
.omega.-isocyanate terminated polymers; various carbodiimides such as 
poly(triisopropylphenylene carbodiimide) i.e., Stabaxol-P from Rhein 
Chemie, and the like, as well as various bisimidazolines. 
The multifunctional imidazolines have the formula 
##STR3## 
where R and n are defined as above for the multifunctional (polyvalent) 
oxazolines and X and Y, are a hydrogen atom, or, independently, an 
imidazoline group, or an imadazoline group and an hydrogen atom. A 
preferred multifunctional imidazoline is bismidazoline. 
Still another group of addition type curatives are the various 
multifunctional epoxides such as the various Shell Epon.RTM. resins, 
epoxidized vegetable oils, tris(2,3-epoxypropyl)isocyanate, and 
4,4'-methylene bis(N,N-diglycidylaniline), and multifunctional aziridines. 
The amount of the curative is generally from about 1 to 12, desirably from 
2 to 10, and preferably from about 2.5 to about 7 parts by weight for 
every 100 parts by weight of the carboxylated nitrile rubber. The addition 
curatives effect cross-linking by reacting with the carboxylic acid groups 
present in the nitrile rubber or double bonds of the diene hydrocarbon 
portion derived from the diene monomer. The amount of curatives used 
results in at least a partially cured nitrile rubber and preferably a 
fully or completely vulcanized nitrile rubber. 
The terms "fully vulcanized" and "completely vulcanized" as used in the 
specification and claims means that the rubber component to be vulcanized 
has been cured to a state in which the elastomeric properties of the 
cross-linked rubber are similar to those of the rubber in its conventional 
vulcanized state, apart from the thermoplastic vulcanizate composition, or 
as indicated by no more change in tensile strength. The degree of cure can 
be described in terms of gel content or, conversely, extractable 
components. Alternatively, the degree of cure may be expressed in terms of 
cross-link density. All of these descriptions are well known in the art, 
for example, in U.S. Pat. Nos. 5,100,947 and 5,157,081, both of which are 
fully incorporated herein by this reference. By the term "partially 
vulcanized" (i.e., degree of cure), it is meant that about 30 percent or 
less and desirably about 10 percent or less by weight of a carboxylated 
nitrile rubber is soluble in methyl ethyl ketone at 80.degree. C. By the 
term "fully vulcanized" (i.e., degree of cure), it is meant that about 5 
percent or less of the cured carboxylated nitrile rubber is soluble in a 
methyl ethyl ketone at 80.degree. C. 
In addition to the thermoplastic resin, nitrile rubber, the processing aid, 
and the curative, the compositions of the present invention can include 
various conventional additives such as reinforcing and non-reinforcing 
fillers, extenders, antioxidants, stabilizers, rubber processing oil, 
extender oils, lubricants, plasticizers, anti-blocking agents, anti-static 
agents, waxes, foaming agents, pigments, flame retardants and other 
processing aids known in the rubber compounding art. Such additives can 
comprise up to about 60 weight percent of the total composition, and can 
be in the plastic phase, the rubber phase or both. Fillers and extenders 
which can be utilized include conventional inorganics such as calcium 
carbonate, clays, silica, talc, titanium dioxide, carbon black, and the 
like. The rubber processing oils generally are paraffinic, naphthenic or 
aromatic oils derived from petroleum fractions. The type will be that 
ordinarily used in conjunction with the specific rubber or rubbers present 
in the compositions, and the quantity based on the total rubber content 
may range from zero to about 100 phr and preferably from about 10 to about 
40 phr. 
Partial or preferably complete cross-linking can be achieved by adding one 
or more of the above-noted rubber curatives to the blend of a 
thermoplastic or the thermoplastic elastomer and rubber and vulcanizing 
the rubber to the desired degree under conventional vulcanizing 
conditions. However, it is preferred that the rubber be cross-linked by 
the process of dynamic vulcanization. As used in the specification and 
claims, the term "dynamic vulcanization" means a vulcanization or curing 
process for a rubber contained in a thermoplastic vulcanizate composition, 
wherein the rubber is vulcanized under conditions of shear at a 
temperature above the melting point of the polyester component. The rubber 
is thus simultaneously cross-linked and dispersed as fine particles within 
the polyester matrix, although as noted above, other morphologies may also 
exist. Dynamic vulcanization is effected by mixing the thermoplastic 
vulcanizate components at elevated temperature in conventional mixing 
equipment such as roll mills, Banbury mixers, Brabender mixers, continuous 
mixers, mixing extruders, and the like. The unique characteristic of 
dynamically cured compositions is that, notwithstanding the fact that the 
rubber component is partially or fully cured, the compositions can be 
processed and reprocessed by conventional plastic processing techniques 
such as extrusion, injection molding, blow molding and compression 
molding. Scrap or flashing can be salvaged and reprocessed. 
The following general procedure was used in the preparation of 
thermoplastic vulcanizates of the present invention as set forth in the 
examples. Thermoplastic polyester, nitrile rubber, and the processing aids 
were mixed in a Brabender mixer at a temperature sufficient to melt the 
thermoplastic and form a blend. Curatives were then added to cross-link 
the rubber and mixing was continued until a maximum melt consistency was 
reached, usually between one and five minutes, then for an additional two 
to three minutes thereafter. The sequence of ingredient addition may vary, 
but generally all of the fillers should be added before substantial 
cross-linking, or vulcanization occurs. The stabilizers and plasticizers 
may be added either before or after vulcanization. The vulcanized 
composition was removed from the mixer, sheeted, and compression molded at 
30.degree. to 50.degree. C. above the melting point of the thermoplastic 
component, and cooled below 100.degree. C. under pressure. Properties of 
the molded sheet were then measured. 
The thermoplastic vulcanizate compositions of the present invention 
generally have good tensile strength, good elongation and good compression 
set properties. Most notably, they have very low oil swell, i.e., 
excellent oil resistance properties comparable to that of the thermoset 
nitrile rubber. Oil swell values as measured by the percent of weight gain 
at 150.degree. C. for 72 hours is generally 25 percent or less, desirably 
20 percent or less, and preferably 15 percent or less. 
The thermoplastic vulcanizate compositions of the present invention can be 
used in applications wherever nitrile rubber is used. Thus they can be 
utilized as seals, as gaskets, hoses, boots, and the like, especially for 
automotive applications. The invention will be better understood by 
reference to the following examples which serve to illustrate, but not to 
limit, the present invention. 
Thermoplastic vulcanizates (TPVs) were produced in a laboratory 
Brabender-Plasticorder, model EPL-V5502. The mixing bowl had a capacity of 
60 ml with roller type rotors, which gave good mixing for samples with a 
batch weight of 40-45 grams. For higher batch weight TPVs, less bulky cam 
rotors were used, which gave a bowl capacity of 85 ml. TPVs were prepared 
at 240.degree. C. and at 75-rpm rotor speed, unless indicated otherwise. 
The plastic materials were melted or partially melted in the mixer cavity 
prior to rubber addition. After a steady torque was obtained for 1 to 2 
minutes in order to ensure as complete a homogenization as possible of the 
rubber and plastic melt blend, the curative was added and curing continued 
for about 8 minutes. The torque rise observed on curing leveled off after 
about 4 to 5 minutes into the cure. The TPV obtained was sheeted when hot 
in a cold press, and subsequently compression molded at 250.degree. C. in 
order to produce plaques for physical testing. Plasticizers were added to 
the rubber and plastic melt blended prior to cure. When melt blending the 
plastic and rubber materials, it is important to at least partially melt 
the plastic prior to rubber addition. Masticating the rubber alone in the 
mixer will lead to thermooxidative crosslinking of the rubber which 
results in powdering of the rubber. 
Utilizing the above general procedure, specific recipes as set forth in 
Tables 1-4 were formulated and prepared. 
TABLE I 
__________________________________________________________________________ 
Example 1 2 3 4 5 6 7 8 9 10 
__________________________________________________________________________ 
Composition 
Nipol 1072 .times. 28 76 76 76 68 68 70 80 76.5 76.5 76 
Valox 315 24 24 24 32 32 30 20 23.50 23.50 24 
1,3-PBO -- -- -- 2.27 2.27 2.12 2.87 -- -- -- 
Polybond 3009 -- -- 2.38 -- 4.53 2.12 2.49 2.35 2.35 2.38 
SP-1045 -- 3.56 3.56 -- -- -- -- -- -- -- 
Ultramox 626 -- -- -- -- -- -- -- 1.56 1.56 -- 
TPAP -- -- -- -- -- -- -- -- -- 5.12 
Irganox B225 -- -- -- -- -- -- -- -- -- 3.14 
HVA-2 -- -- -- -- -- -- -- 2.51 -- -- 
Matrimid 5292A -- -- -- -- -- -- -- -- 2.51- -- 
Properties 
Hardness (Shore A) 67 78 79 85 87 86 79 83 83 79 
UTS (psi) 1208 1756 1891 2423 2855 3271 1803 2563 2515 1849 
UE (%) 205 193 216 203 243 256 202 254 247 231 
M 100 (psi) 700 946 966 1317 1393 -- 883 1057 1063 874 
CS (%, 22 hr, 100.degree. C.) -- 9 10 17 18 19 11 13 15 -- 
CS (%, 22 hr, 150.degree. C.) -- 29 29 40 35 35 23 29 29 52 
Wt. Gain (%, 72 hr, 150.degree. C.) -- 18 23 15 21 17 22 19 18 16 
Tension Set(%) 13 9 11 
16 18 13 7 11 11 9 
Consistency of Product T 
T P T T T T T T 
__________________________________________________________________________ 
T: Thermoplastic P: Powder 
TABLE II 
______________________________________ 
Example 11 12 13 14 15 16 
______________________________________ 
Composition 
Nipol 1072 .times. 28 75 76 76 76 76 76 
Valox 315 25 24 24 24 24 24 
1,3-PBO 2.34 2.38 2.38 2.38 2.38 2.41 
Polybond 3009 -- 2.38 -- -- -- -- 
Royaltuf 490 -- -- -- -- -- 7.22 
Kraton FG-1901X -- -- -- 2.38 -- -- 
Irganox B225 3.10 3.14 3.14 -- -- 2.24 
HD 6706.19 -- -- 2.38 -- 2.38 -- 
Properties 
Hardness (Shore A) -- -- -- 79 81 73 
UTS (psi) -- -- -- 2289 2048 1277 
UE (%) -- -- -- 238 225 188 
M 100(psi) -- -- -- 915 923 669 
CS (%, 22 hr, 150.degree. C.) -- -- -- 30 32 -- 
Wt. Gain (%, 72 hr, -- -- -- 18 18 -- 
150.degree. C.) 
Tension Set (%) -- -- -- 7 8 6 
Consistency of Product P T T T T T 
______________________________________ 
P: Powder 
T: Thermoplastic 
TABLE III 
______________________________________ 
Example 17 18 19 
______________________________________ 
Composition 
Nipol 1072 .times. 28 76 76 69.00 
Irganox B225 3.17 -- -- 
75PBT/25PBI 24 -- -- 
PET 13339 -- 24 -- 
Hytrel 8238 -- -- 31.00 
Polybond 3009 2.38 2.38 2.37 
1,3-PBO 2.38 3.40 3.04 
Properties 
Hardness (Shore A) 79 82 85 
UTS (psi) 1911 1566 2630 
UE (%) 253 161 242 
M 100 (PSI) 773 1052 1144 
CS (%, 22 hr, 100.degree. C.) 20 14 25 
CS (%, 22 hr, 150.degree. C.) 40 26 40 
Wt. Gain (%, 72 hr, 150.degree. C.) 19 20 -- 
Tension Set (%) 7 11 12 
Consistency of Product T T T 
______________________________________ 
T: Thermoplastic 
TABLE IV 
__________________________________________________________________________ 
Example 20 21 22 23 24 25 26 27 28 29 30 
__________________________________________________________________________ 
Composition 
Nipol 1072 .times. 28 65 65 65 70 76 76 70 76 76 76 76 
Valox 315 35 35 35 30 24 24 30 24 24 24 24 
Polybond 3009 2.58 2.57 2.57 6.55 2.38 2.39 6.56 2.38 2.38 2.38 2.41 
1,3-PBO 2.03 2.04 2.04 
2.18 2.40 2.41 2.19 
2.38 2.38 2.38 2.41 
Irganox B225 3.14 3.14 
3.14 2.18 2.29 2.29 
2.45 2.29 2.29 2.29 
2.29 
Reofos 50 -- 16.32 25.35 -- -- -- -- -- -- -- 11.39 
Uniplex 809 -- -- -- -- 7.71 -- -- -- -- -- -- 
Uniplex 413 -- -- -- -- 7.67 -- -- -- -- -- -- 
Plalsthall BSA -- -- -- -- -- 18.75 -- -- -- -- -- 
Paraplex G30 -- -- -- -- -- -- -- 17.62 -- -- -- 
Remarc P-40-60 -- -- -- -- -- -- -- 11.50 -- -- -- 
Calsol 8450 -- -- -- -- -- -- -- -- 7.76 -- -- 
Calsol 5120 -- -- -- -- -- -- -- -- -- 7.71 -- 
Flexxon 885 -- -- -- -- -- -- -- -- -- -- 7.60 
Properties 
Hardness (Shore A) 90 86 83 86 77 71 82 72 78 76 65 
UTS (psi) 2709 1927 1698 2643 1672 1595 1771 1533 1891 1664 1103 
UE (%) 249 231 235 262 
250 254 248 251 239 230 
204 
M 100 (PSI) 1447 1034 902 1230 687 623 880 644 779 758 602 
CS (%, 22 hr, 100.degree. C.) 19 19 21 20 -- 13 18 -- -- -- 14 
CS (%, 22 hr, 150.degree. C.) 36 36 36 38 34 29 34 -- -- -- 34 
Wt. Gain 14 1 -4 18 4 8 9 -- -- -- 5 
(%, 72 hr, 150.degree. C.) 
Tension Set (%) 19 13 13 16 9 5 13 7 8 7 7 
Consistency of Product T T T T T T T T T T T 
__________________________________________________________________________ 
T: Thermoplastic 
Elastomeric Materials 
Nipol 1072 X 28: Carboxylic acid functional nitrile rubber. Bound 
acrylonitrile .about.27 weight percent. Carboxylic acid content: 
.about.0.08 equivalents per hundred parts of rubber. Gel content: 50-60 
weight percent in methyl ethyl ketone (Zeon Chemicals, Inc., Louisville, 
Ky.). 
Nipol DN3635: Gel free nitrile rubber. Bound acrylonitrile: 36 weight 
percent (Zeon Chemicals, Inc., Louisville, Ky.). 
Chemigum HR 665: Nitrile rubber with bound antioxidant and 34 weight 
percent bound acrylonitrile (Goodyear Tire and Rubber Company, Akron, 
Ohio). 
Plastic Materials 
Valox 315: Poly(tetramethylene terephthalate) with weight average molecular 
weight of about 105,000, and number average molecular weight of about 
50,000 (GE Plastics, Pittsfield, Mass.). 
75PBT/25PBI: 75:25 weight percent poly(butylene terephthalate/isophthalate) 
experimental polymer (AMOCO Chemicals, Naperville, Ill.). 
PET 13339: Modified poly(ethylene terephthalate), m.p. 235.degree. C. 
(Eastman Chemical Company, Kingstport, Tenn.). 
Hytrel 8238: Polyester-ether segmented block copolymer thermoplastic 
elastomer with 82 Shore D hardness (DuPont Company, Wilmington, Del.). 
Processing Aids 
Royaltuf 490: Maleated EPDM rubber with 1 weight percent bound maleic 
anhydride (Uniroyal Chemical Company, Middlebury, Conn.). 
Kraton FG-1901X: Maleated styrene/ethylene-butene/styrene triblock 
copolymer with 2 weight percent bound maleic anhydride (Shell Chemical 
Company, Houston, Tex.). 
Polybond 3009: Maleated high-density polyethylene with 1 weight percent 
bound maleic anhydride (Uniroyal Chemical Company, Middlebury, Conn.). 
HD 6706.19: High-density polyethylene (Exxon Chemical Company, Houston, 
Tex.). 
Crosslinking Compounds 
1,3-PBO: 1,3-phenylenebis2,2'-(oxazoline-2) (Tramaco Japan Ltd., Tokyo, 
Japan). 
SP-1045: Alkylated phenol/formaldehyde resin (Schenectady International,, 
Inc., Schenectady, N.Y.). 
HVA-2: 2,4-bismaleimidotoluene (DuPont Dow Elastomers, Stow, Ohio). 
Matrimid 5292A: Bis(4-maleimidophenyl)methane (Ciba-Geigy Corporation, 
Brewster, N.Y.). 
TPAP: Trimethylolpropane tris(2-methyl-1-aziridenepropionate) (Aldrich 
Chemical Company, Milwaukee, Wis.). 
Plasticizers 
Reofos 50: Isopropylated triphenyl phosphate (C.P. Hall Company, Stow, 
Ohio). 
Uniplex 809: Polyethylene glycol bis(2-ethylhexanoate) (Unitex Corporation, 
Greensboro, N.C.). 
Uniplex 413: Substituted benzenesulfonamide (Unitex Corporation, 
Greensboro, N.C.). 
Plasthall BSA: N-n-butylblenzenesulfonamide (C. P. Hall Company, Stow, 
Ohio). 
Paraplex G-30: Mixed dibasic acid polyester (C. P. Hall Company, Stow, 
Ohio). 
Remarc P-40-60: Chlorinated paraffinic oil with 39 weight percent chlorine 
(Harwick Chemical Corporation, Akron, Ohio). 
Calsol 8450; 5120: Napthenic process oil (Sun Company, Canton, Ohio). 
Flexon 885: Paraffinic process oil (Exxon Oil Company, Houston, Tex.). 
Antioxidant 
Irganox B225: Phenolic/Phosphite based antioxidant (Ciba Specialty 
Chemicals Corporation, Troy, Mich.). 
Example 1 describes the preparation of a thermoplastic blend of 
carboxylated nitrile rubber and poly(butylene terephthalate).

EXAMPLES 
Table I illustrates the effects of processing aids on cured compositions of 
carboxylated nitrile rubber and PBT. 
On curing the blend of Example 1 with phenolic resin, a sticky and powdery 
product was isolated (Example 2). The compression molded plaque of this 
powdery product, however, exhibited good mechanical properties. In Example 
3, the addition of maleated high density polyethylene (Polybond 3009) to 
the recipe of Example 2 yielded a TPV that did not powder and could be 
easily removed from the mixer. It should be noted that the mechanical 
properties of the TPVs are considerably better than that of the uncured 
blend of Example 1. 
Attempted TPV preparation from a blend of carboxylated nitrile rubber and 
poly(butylene terephthalate) with the use of 
1,3-phenylenebis-2,2'-(oxazoline-2) as a curative also yielded a sticky 
and powdery product (Example 4) in the absence of a process aid. The use 
of a process aid along with the oxazoline curative allowed the production 
of a thermoplastic product that could be readily removed from the mixer 
cavity (Example 5). Example 6 illustrates the preparation of a TPV with a 
reduced amount of process aid when compared to the amount used in Example 
5. In general, the lower the plastic content in a TPV recipe, the greater 
the chances of the production of an unprocessable product. The use of 
Polybond 3009 allows the preparation of a processable TPV unit with 
extremely low plastic to rubber ratio (20:80, Example 7). 
Examples 8-10 demonstrate the production of processable TPVs based upon 
carboxylated nitrile rubber, poly(butylene terephthalate), and a maleated 
high density polyethylene process aid, with maleimide and aziridine 
curatives. 
Table II illustrates the use of different processing aids. 
In Example 11, a melt blend of Nipol 1072 x 28 and Valox 315 (75:25 rubber 
to plastic weight ratio) was produced at 240.degree. C. and 75 rpm cam 
rotor speed. After adding the 1,3-PBO curative, the rotor speed was 
increased to 200 rpm and curing was continued at this speed for 9 minutes. 
During the cure, shear heating caused the material temperature to rise to 
296.degree. C. A "crumbly" product that stuck to the mixer cavity was the 
result. The procedure of Example 11 was repeated where part of the plastic 
phase (Valox 315) was replaced either with high-density polyethylene or 
maleated high-density polyethylene (Examples 12 and 13). In both cases, 
the material obtained was cleanly removed from the mixer and only slightly 
more "crumbly" when compared with the corresponding experiments where the 
curing was conducted at 75 rpm. These examples illustrate further the 
importance of a process aid in the production of the thermoplastic TPVs of 
this invention. 
Examples 14, 15, and 16 document the properties of processable TPVs 
obtained with the aid of a maleated styrene/ethylene butene/styrene 
triblock copolymer of a high density polyethylene and a maleated EPDM 
rubber, respectively. When maleated EPDM is the process aid, soft 
compositions can be obtained. 
Table III illustrates the use of different thermoplastic resins. 
Various polyester based plastic materials such as poly(butylene 
terephthalate-co-isophthalate) (Example 17), a modified polyethylene 
terephthalate) (Example 18), and a poly(butylene 
terephthalate)/poly(tetramethylene glycol) segmented block copolymer 
(Example 19) can also be used in the practice of this invention. 
Table IV illustrates the applicability of plasticizers. 
The hard TPV composition of Example 20 was plasticized to softer 
compositions in Examples 21 and 22 with the aid of an isopropylated 
triphenyl phosphate as plasticizer. About 63 grams of the TPVs of Examples 
20-22 were passed through a small single screw extruder at 500.degree. F. 
Good melt strength was observed for these TPVs, with the plasticized TPVs 
exhibiting good surface smoothness. The fair surface smoothness of the 
TPVs of Example 20 was improved in a formulation containing additional 
Polybond 3009 (Example 23). Examples 24-30 illustrate the suitability of 
various polar and nonpolar plasticizers. In the practice of this 
invention. 
While in accordance with the Patent Statutes, the best mode and preferred 
embodiment has been set forth, the scope of the invention is not limited 
thereto, but rather by the scope of the attached claims.