Soft touch polyolefin compositions

Information

  • Patent Grant
  • 6949605
  • Patent Number
    6,949,605
  • Date Filed
    Monday, June 9, 2003
    21 years ago
  • Date Issued
    Tuesday, September 27, 2005
    18 years ago
Abstract
The present invention provides a soft touch soft touch thermoplastic olefin composition. The soft touch thermoplastic olefin composition comprises a polypropylene-ethylene copolymer and a cross-linked or uncross-linked ethylene-propylene thermoplastic elastomer. The thermoplastic elastomer is present in a sufficient amount that the soft touch thermoplastic olefin composition has a 1% flexural secant modulus from about from about 10,000 psi to about 80,000 psi.
Description
BACKGROUND OF THE INVENTION

1. Field of the Invention


The present invention relates to soft touch polyolefin compositions and a method of making such soft touch polyolefin compositions, and in particular, soft touch polyolefin compositions that include cross-linked or uncross-linked ethylene-propylene thermoplastic elastomers.


2. Background Art


Thermoplastic polyolefins (“TPO”) resins are blends of polypropylene and elastomers. In many applications, TPO resins may include such additives as pigments, antioxidants, stabilizers, and fillers. They can be made by physically blending in an internal mixer, or by polymerizing in a reactor. TPO resins are useful in a number of molding processes, which include, for example, blow molding, injection molding, thermoforming, blown film extrusion, cast film extrusion, sheet extrusion, profile extrusion, and the like. Moreover, TPO resins are used to form a variety of items ranging from automotive components to plastic films to containers.


Each year, polymeric resins are used to form a multitude of plastic containers and storage bottles. In particular, the personal care industry distributes a significant portion of its products in plastic bottles (i.e., shampoo, lotions, and the like.) Furthermore, in the automotive industry, TPO resins are increasingly being used to form interior components. Presently, there is a trend to improve the aesthetics of such containers by improving the tactile softness of these containers when they are held by the user. Similarly, the automotive industry requires that many interior components have an aesthetically pleasing soft touch. The sensation of “softness” tends to be somewhat subjective, without a clear correlation to any particular physical property. However, properties which quantify stiffness and hardness such as the flexural modulus and Shore A hardness relate somewhat to softness and are useful in developing such materials. Currently, there has only been limited success in developing containers formed from polymeric resins that possess the requisite “softness.”


Accordingly, there is a need in the prior art to develop polymeric resins, and in particular, TPO resins that will improve softness when touched by the end user. Moreover, such resins should be formed by processes that are economical and relatively easy to implement.


SUMMARY OF THE INVENTION

The present invention overcomes the problems of the prior art by providing in one embodiment a soft touch thermoplastic olefin composition. The soft touch thermoplastic olefin composition comprises a polypropylene-ethylene copolymer and a cross-linked or uncross-linked ethylene-propylene thermoplastic elastomer. The thermoplastic elastomer is present in a sufficient amount that the soft touch thermoplastic olefin composition has a 1% flexural secant modulus from about from about 10,000 psi to about 80,000 psi. The polypropylene-polyethylene copolymers provided in U.S. Pat. No. 5,705,576, U.S. Pat. No. 5,587,436, and U.S. Pat. No. 5,314,746 were found to be particularly useful in practicing the invention. In a particularly preferred embodiment of the invention, the cross-linked or uncross-linked ethylene-propylene thermoplastic elastomer does not contain any C4 or higher α-olefin comonomers, such as for example, 1-butene, 1hexene, 1-octene, and the like. The soft touch thermoplastic olefin composition of the present invention is advantageously used to form such articles as automotive interior components, personal care bottles, over-molded grips, multilayer thermoformed containers, multilayered flexible packaging, multilayered profile pipe, and the like.


In another embodiment of the present invention, a method of forming the soft touch thermoplastic olefin compositions set forth above is provided. The method comprises combining a polypropylene-ethylene copolymer and a cross-linked or uncross-linked ethylene-propylene thermoplastic elastomer to form a mixture and blending the mixture at sufficient temperature to melt the mixture. Typically, the melt temperature is from about 400° F. to about 450° F.


DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENT(S)

Reference will now be made in detail to presently preferred compositions or embodiments and methods of the invention, which constitute the best modes of practicing the invention presently known to the inventors.


The term “elastomer” as used herein refers to a rubber polymer having the characteristic of being able to stretch under low stress. Examples of polymers which can be formulated as elastomers are butyl rubber, polyurethane, silicones, and ethylene-propylene copolymers.


The term “plastomer” as used herein refers to a plastic polymer usually added to a blend to confer plastic properties to a mixture. In general, plastomers have higher specific gravities than elastomers.


In an embodiment of the present invention, a soft touch thermoplastic olefin composition is provided. The soft touch thermoplastic olefin composition of the invention comprises a polypropylene-ethylene copolymer and a cross-linked or uncross-linked ethylene-propylene thermoplastic elastomer. The thermoplastic elastomer is present in a sufficient amount that the soft touch thermoplastic olefin composition has a 1% flexural secant modulus from about from about 10,000 psi to about 80,000 psi. More preferably, the thermoplastic elastomer is present in a sufficient amount that the soft touch thermoplastic olefin composition has a 1% flexural secant modulus that is less than about 20,000 psi; most preferably the thermoplastic elastomer is present in a sufficient amount that the soft touch thermoplastic olefin composition has a 1% flexural secant modulus from about 10,000 psi to about 30,000 psi. Most preferably, the thermoplastic elastomer is present in a sufficient amount that the soft touch thermoplastic olefin composition has a 1% flexural secant modulus that is less than about 20,000 psi. In a particularly preferred embodiment, the thermoplastic elastomer is present in a sufficient amount that the soft touch thermoplastic olefin composition has a 1% flexural secant modulus from about from about 10,000 psi to about 20,000 psi. The soft touch thermoplastic olefin composition of the present invention is further characterized by the Shore A hardness as determined from ASTM D2240 and a compression set as determined from ASTM D395. The thermoplastic elastomer is preferably present in a sufficient amount that the soft touch thermoplastic olefin composition has a maximum Shore A hardness of about 80 to 100. More preferably, the thermoplastic elastomer is present in a sufficient amount that the soft touch thermoplastic olefin composition has a Maximum Shore A hardness about 80 to 90; and most preferably, the thermoplastic elastomer is present in a sufficient amount that the soft touch thermoplastic olefin composition has a Maximum Shore A hardness about 80 to 85. Similarly, the thermoplastic elastomer is preferably present in a sufficient amount that the soft touch thermoplastic olefin composition has a compression set from about 67% to about 100%. More preferably, the thermoplastic elastomer is present in a sufficient amount that the soft touch thermoplastic olefin composition has a compression set from about 80% to about 90%.


Preferred polypropylene-polyethylene copolymers are provided in U.S. Pat. No. 5,705,576, U.S. Pat. No. 5,587,436, and U.S. Pat. No. 5,314,746. The entire disclosure of each of these patents is hereby incorporated by reference. The polypropylene-ethylene copolymer preferably has a 1% flexural secant modulus from about 5,000 psi to about 70,000 psi. More preferably, the polypropylene-ethylene copolymer has a 1% flexural secant modulus from about 10,000 psi to about 40,000 psi. In a variation, the polypropylene-ethylene copolymer has a 1% flexural secant modulus from about 15,000 psi to about 35,000 psi. In another variation, the polypropylene-ethylene copolymer has a 1% flexural secant modulus of about 25,000 psi. Moreover, the polypropylene-ethylene copolymer has from about 3 to about 50 weight percent ethylene and having a melt flow from 0.01 to 500 dg/min and melting point from 115° C. to 160° C. More preferably, the polypropylene-ethylene copolymer contains 8 to 40 weight percent ethylene and has a melt flow rate from 0.1 to 100 dg/min and a melting point from 125° C. to 160° C. Most preferably, the polypropylene-ethylene copolymer contains 15 to 30 weight percent ethylene. In a particular preferred variation, the polypropylene-ethylene copolymer is made by the method comprising homopolymerizing propylene in a first reactor maintained at 50° C. to 100° C. and 250 psig to 650 psig in the presence of a catalyst system comprising a titanium-containing catalyst component and organoaluminum cocatalyst component to produce a first product; feeding the first product into a second reactor maintained at 25° C. to 80° C. and 100 psig to 500 psig wherein propylene is copolymerized with ethylene, to obtain high rubber content modified polypropylene having reduced hexane extractables and improved paintability. Moreover, the polypropylene-ethylene copolymer has a control parameter Qc is calculated using eight integrated areas of the 13C NMR spectrum corresponding to molecular structural features for copolymers of propylene and ethylene in accordance with the equation:

Qc=A/B

where

    • A=1.167R1+0.75R2+1.5R3+1.5R4+1.167R8;
    • B=0.667R1+0.5R2+R5+R6+R7+0.667R8; and
    • R1 through R8 have the following peak assignments:



















R1
37.9
PPM



R2
37.5
PPM



R3
33.2
PPM



R4
31.2-30.9
PPM



R5
30.4
PPM



R6
30.0
PPM



R7
27.4
PPM



R8
24.9
PPM;












    • (b) the limits of Qc are selected to be within the range 0.65 to 1.35;

    • (c) the actual value of the parameter, QA, is determined for the polymer obtained from the second reactor; and

    • (d) the ethylene feed is controlled to maintain QA within the limits defined in (b). In one variation, the limits of Qc are from about 0.65 to about 1.35, while in a second particularly preferred variation Qc varies from about 0.90 to about 1.35. Typically, the first and second reactors are stirred, fixed-bed reactors. This preferred method of making the polypropylene-ethylene copolymer will preferably have an amount of ethylene sufficient to incorporate from 15 to 30 weight percent ethylene in the polymer is fed to the second reactor and an amount of hydrogen ranging from 0.1 to 5 mol percent is included in the first reactor and an amount of hydrogen from 1 to 10 mol percent is included in the second reactor. Moreover, one or more α-olefins containing from 4 to 8 carbon atoms included in the polymerization. Suitable polypropylene-polyethylene copolymers include, for example, PP0021, PPTR477, PP7200AF, PPTR346, PP8752HF, and TP 38KC01 commercially available from Equistar Chemicals, LP located in Houston Tex.





As set forth above, the soft touch thermoplastic olefin composition includes a cross-linked or uncross-linked ethylene-propylene thermoplastic elastomer in a sufficient amount that the soft touch thermoplastic olefin composition has a 1% flexural secant modulus from about from about 10,000 psi to about 80,000 psi. Typically, the thermoplastic elastomer is present in an amount from about 1% to about 80% of the total weight of the soft touch thermoplastic olefin composition. More preferably, the thermoplastic elastomer is present in an amount from about 5% to about 40% of the total weight of the soft touch thermoplastic olefin composition; and most preferably, the thermoplastic elastomer is present in an amount of about 30% of the total weight of the soft touch thermoplastic olefin composition. Suitable thermoplastic elastomers include, for example, Santoprene® 8000 Rubber 8211-35W237 commercially available from Advanced Elastomer Systems located in Akron, Ohio; Vistalon 878 and MDV-91-9 each commercially available from Exxon Mobile Chemical; Sunigum 7752 commercially available from Zeon Chemicals, L.P. located in Louisville Ky.; and Polybond 3150 (a functionalized polypropylene) commercially available from Kangshin Industrial Co., Ltd located in Seoul Korea.


The soft touch thermoplastic olefin composition of the invention optionally includes a plastomer or a compatiblizer. Suitable plastomers include, but are not limited to, a metallocene catalyzed polyethylene plastomer or a Ziegler catalyzed polyethylene plastomer. Suitable plastomers include, for example, Exact™ 8201 commercially available from Exxon Mobil Chemical.


The thermoplatic olefin compositions of the present invention may also include one or more additives such as cross-linking agents, UV stabilizers, flame retardants, fillers, and pigments. Additives are potentially important in establishing the long term stability of the thermoplastic olefin compositions as well as chemical and impact resistance. Specifically, the thermoplatic olefin compositions of the present invention optionally includes UV stabilizers present in an amount from about 1500 ppm to about 2500 ppm. More preferably the UV stabilizers are present in an amount of 1750 ppm to about 2250 ppm, and most preferably, the UV stabilizers are present in an amount of about 2000 ppm. Suitable UV stabilizers include, but are not limited to hindered amine light stabilizers (“HALS”). Examples of HALS include: Chimassorb 944, Chimassorb 994, Chimassorb 905, Tinuvin 770, Tinuvin 992, Tinuvin 622, Tinuvin 144, and Spinuvex A36 available from Geigy; and Cyasorb UV 3346 and Cyasorb UV 944 commercially available American Cyanamide. Particularly preferred UV stabilizers are Cytec UV 3346 and Chemasorb 944 (poly[N,N-bis(2,2,6,6-tetramethyl-4-piperidinyl)-1,6-hexanediamine-co-2,4-dichloro-6-morpholino-1,3,5-triazine.) The thermoplatic olefin compositions still further optionally includes a flame retardant. Flame retardants include, for example, halogen-containing compounds, antimony oxides, or phosphorus compounds. Suitable flame retardants include, but are not limited to aluminum trihydrate, antimony oxide (Sb2O3), and decabromobiphenyl oxide (“decabrome”). Finally, the thermoplatic olefin compositions may also include fillers such as long glass fibers, carbon fiber, and talc. These fillers allow the material properties of the thermoplatic olefin compositions to be adjusted.


In another embodiment of the present invention, a method of forming the soft touch thermoplastic olefin compositions set forth above is provided. The method comprises combining a polypropylene-ethylene copolymer and a cross-linked or uncross-linked ethylene-propylene thermoplastic elastomer to form a mixture and blending the mixture at sufficient temperature to melt the mixture. Typically, the melt temperature is from about 400° F. to about 450° F. Again, as set forth above, the thermoplastic elastomer is present in a sufficient amount that the soft touch thermoplastic olefin composition has a 1% flexural secant modulus from about from about 10,000 psi to about 80,000 psi. Optionally, the plastomers and compatiblizer described above may also be added to the mixture prior to blending.


The following examples illustrate the various embodiments of the present invention. Those skilled in the art will recognize many variations that are within the spirit of the present invention and scope of the claims.







EXAMPLES

1. Blend Preparation


The soft touch blends summarized in Table 1 were prepared using a 40 mm twin screw Berstoff extruder. The extruder temperature profile ranged from 300-400° F. The melt temperature was around 400-450° F. The melt blend was subsequently pelletized and used for testing and evaluation. The properties of these blends are summarized in Tables 2 and 3. Shore A test were performed in accordance to ASTM D2240 to evaluate the hardness of the thermoplastic resins. The better compositions demonstrated lower Shore A hardness from about 84 to 94. The flexural modulus (“flex mod”) 1% and 2% secant were determined in accordance with ASTM D790. The better compositions were observed to have values of both under 20,000 psi. The melt flow ratio (“MFR”) and the high load melt flow index (“HLMFR”) were determined following ASTM D1238. The density was determined in accordance to ASTM D2839, the compression set in accordance with ASTM D395, and the heat deflection in accordance with ASTM D648.









TABLE 1







Compositions of soft touch polyolefin blends.














Ethylene-

Wt. %


2% TiO2 in



propylene
Thermoplastic
Thermoplastic

Wt. %
PP0021


Example
copolymer
elastomer
elastomer
Plastomer
Plastomer
mixture (Wt %)
















1
PP0021
8211-35W237
15





2
PP0021
8211-35W237
15
Exact 8201
10


3
PP0021
8211-35W237
30


4
PP0021
8211-35W237
30


5


5
PP0021
8211-35W237
30
Exact 8201
10


6
PP0021
8211-35W237
30
Exact 8201
10
5


7
PP0021
Vistalon 878
15


8
PP0021
Vistalon 878
15
Exact 8201
10


9
PP0021
Vistalon 878
30


10
PP0021
Vistalon 878
30


5


11
PP0021
Vistalon 878
30
Exact 8201
10


12
PP0021
Vistalon 878
30
Exact 8201
10
5


13
PP0021
MDV-91-9
15


14
PP0021
MDV-91-9
15
Exact 8201
10


15
PP0021
MDV-91-9
30


16
PP0021
MDV-91-9
30


5


17
PP0021
MDV-91-9
30
Exact 8201
10


18
PP0021
MDV-91-9
30
Exact 8201
10
5


19
PP0021
Vistalon 878
40


5


20
PP0021
MDV-91-9
40


21
PPTR477
8211-35W237
30


22
PPTR477
8211-35W237
50


23
PP7200AF
8211-35W237
30


24
PP7200AF
8211-35W237
50


25
PPTR346
8211-35W237
30


26
PPTR346
8211-35W237
50


27
PP8752HF
8211-35W237
30


28
PP8752HF
8211-35W237
50


29
TP38KC01
8211-35W237
30


30
TP38KC01
8211-35W237
50


31
PP0021
Sunigum 7752
30
Polybond
10






3150
















TABLE 2







Properties of soft touch polyolefin blends - part 1.














MFR
HLMFR
Ratio of
Density

Shore A (15


Example
(g/10 min)
(g/10 min)
HLMFR/MFR
(g/ml)
Shore A (max)
seconds)
















1
1.72
143
83.1

96
93


2
1.83
143
78.1
0.8883
94
91


3
2.27
263
115.9
0.895
93
89


4
2.5
302
121
0.8966
94
90


5
2.3
232
101
0.8952
91
86


6
2.53
271
107
0.8962
94
89


7
1.55
106
68.3
0.8783
96
93


8
1.51
97.6
64.6
0.8783
95
92


9
1.57
87.6
55.8
0.8737
95
89


10
1.56
89.3
57.2
0.8738
94
87


11
1.55
83.5
53.8
0.8747
92
86


12
1.285
73.0
56.8
0.8809
93
89


13
1.53
85.4
55.8
0.8786
96
92


14
1.53
89.9
58.7
0.8779
96
92


2
1.83
143
78.1
0.8883
94
91


15
2.09
107
51.2
0.8746
84
88


16
2.18
123
56.4
0.8750
94
88


17
2.16
104
48.1
0.8751
92
85


18
2.17
110
50.7
0.8769
94
88


19
1.5
74.9
49.9
0.8749
92
87


20
2.33
124
53.2
0.8739
92
86


21
5.5
>1000
>182
0.9140
99
97


22
15.3
>1000
>65
0.9196
97
96


23
4.02
772
192
0.9107
98
97


24
4.22
>1000
>237
0.9162
97
96


25
3.493
627
180
0.8957
98
97


26
3.858
>1000
>260
0.9113
97
95


27
3.885
691
178
0.8985
98
96


28
4.762
>1000
>210
0.9071
95
93


29
1.86
283
152
0.8939
98
96


30
2.39
732
306
0.9083
97
93


31
0.63
70.6
112
0.9294
97
95
















TABLE 3







Properties of soft touch polyolefin blends - part 2.














Deflection
Compression





Temperature
Set (70° F.,



Flex Mod 1%
Flex Mod 2%
@
22 hrs.)


Example
secant (psi)
secant (psi)
66 psi (° C.)
(%)














1
17000
15600
43
83


2
14100
13000
41
84


3
10300
9500
38
85


4
11000
10100
39
84


5
8900
8400
37
88


6
10700
9900
38
87


7
20500
18800
42
84


8
16300
15400
41
80


9
14700
13600
38
82


10
13200
12300
38
86


11
12200
11400
37
95


12
14300
13200
38
95


13
19600
18100
40
69


14
17700
16300
39
81


15
15400
14100
38
88


16
17200
15800
39
87


17
12000
11100
37
98


18
14900
13700
38
98


19
12800
11800
38
87


20
14300
13100
38
100


21
75200
65500
66
71


22
37600
32800
53
66


2
14100
13000
41
84


23
49000
42800
61
73


24
27300
24000
50
67


25
56900
48600
58
79


26
26200
22600
46
69


27
50700
43000
53
71


28
27100
23100
45
66


29
39900
34500
56
82


30
23600
20500
46
76


31
30100
26900
46
75










2. Preparation of Soft Touch Bottles


Soft touch bottles were made using the blends in Table 1. A Krupp Kautex KB3 unit was used to blow mold 16 oz round bottles with the soft touch layer on the outside and an HD or PP layer inside. The temperature profile in the two extruders and in the die head was maintained around 375° F. Bottles formed in this manner were found to have improved soft touch/stiffness balance.


While embodiments of the invention have been illustrated and described, it is not intended that these embodiments illustrate and describe all possible forms of the invention. Rather, the words used in the specification are words of description rather than limitation, and it is understood that various changes may be made without departing from the spirit and scope of the invention.

Claims
  • 1. A soft touch thermoplastic olefin composition, the composition comprising: a polypropylene-ethylene copolymer having from about 3 to about 50 weight percent ethylene, a 1% flexural secant modulus from about 10,000 psi to about 40,000 psi, and having a melt flow from 0.01 to 500 dg/min and melting point from 115° C. to 160° C., and a cross-linked or uncross-linked ethylene-propylene thermoplastic elastomer, the thermoplastic elastomer being present in an amount from about 5% to about 40 percent of the weight of the soft touch thermoplastic olefin, wherein the soft touch thermoplastic olefin composition has a 1% flexural secant modulus from about from about 10,000 psi to about 80,000 psi and a Maximum Shore A hardness is from about 80 to about 100 and the compression set is from about 67% to about 100%.
  • 2. The soft touch thermoplastic olefin composition film of claim 1 wherein the polypropylene-ethylene copolymer contains 8 to 40 weight percent ethylene and has a melt flow rate from 0.1 to 100 dg/min and a melting point from 125° C. to 160° C.
  • 3. The soft touch thermoplastic olefin composition film of claim 1 wherein the polypropylene-ethylene copolymer contains 15 to 30 weight percent ethylene.
  • 4. The soft touch thermoplastic olefin composition of claim 1 wherein the thermoplastic elastomer is present in an amount of about 30% of the total weight of the soft touch thermoplastic olefin composition.
  • 5. The soft touch thermoplastic olefin composition of claim 1 wherein the polypropylene-ethylene copolymer has a 1% flexural secant modulus from about 15,000 psi to about 35,000 psi.
  • 6. The soft touch thermoplastic olefin composition of claim 1 wherein the polypropylene-ethylene copolymer has a 1% flexural secant modulus of about 25,000 psi.
  • 7. The soft touch thermoplastic olefin composition of claim 1 further comprising a plastomer or a compatiblizer.
  • 8. The soft touch thermoplastic olefin composition of claim 7 wherein the plastomer is a metallocene catalyzed polyethylene plastomer or a Ziegler catalyzed polyethylene plastomer.
  • 9. The soft touch thermoplastic olefin composition of claim 1, wherein the polypropylene-ethylene copolymer is made by the method comprising: homopolymerizing propylene in a first reactor maintained at 50° C. to 100° C. and 250 psig to 650 psig in the presence of a catalyst system comprising a titanium-containing catalyst component and organoaluminum cocatalyst component to produce a first product; feeding the first product into a second reactor maintained at 25° C. to 80° C. and 100 psig to 500 psig wherein propylene is copolymerized with ethylene, to obtain high rubber content modified polypropylene having reduced hexane extractables and improved paintability.
  • 10. The soft touch thermoplastic olefin composition of claim 9 wherein: (a) a control parameter Qc is calculated using eight integrated areas of the 13C NMR spectrum corresponding to molecular structural features for copolymers of propylene and ethylene in accordance with the equation: Qc=A/B
  • 11. The soft touch thermoplastic olefin composition of claim 10 wherein the limits of Qc are from about 0.65 to about 1.35.
  • 12. The soft touch thermoplastic olefin composition of claim 10 wherein the limits of Qc are from about 0.90 to about 1.35.
  • 13. The soft touch thermoplastic olefin composition of claim 10 wherein the first and second reactors are stirred, fixed-bed reactors.
  • 14. The soft touch thermoplastic olefin composition of claim 10 wherein one or more a-olefins containing from 4 to 8 carbon atoms are included in the polymerization.
  • 15. The soft touch thermoplastic olefin composition of claim 14 wherein an amount of ethylene sufficient to incorporate from 15 to 30 weight percent ethylene in the polymer is fed to the second reactor.
  • 16. The soft touch thermoplastic olefin composition of claim 15 wherein an amount of hydrogen ranging from 0.1 to 5 mol percent is included in the first reactor and an amount of hydrogen from 1 to 10 mol percent is included in the second reactor.
  • 17. An article made from the soft touch thermoplastic olefin composition of claim 1.
  • 18. A method of forming a soft touch thermoplastic olefin composition, the method comprising: combining a polypropylene-ethylene copolymer and a cross-linked or uncross-linked ethylene-propylene thermoplastic elastomer to form a mixture, the ethylene-propylene thermoplastic elastomer being present in an amount from about 5 to about 40% of the total weight of the soft touch thermoplastic olefin composition and the polypropylene-ethylene copolymer having from having from about 3 to about 50 weight percent ethylene, a 1% flexural secant modulus from about 10,000 psi to about 40,000 psi, and having a melt flow from 0.01 to 500 dg/min and melting point from 115° C. to 160° C.; and blending the mixture at a sufficient temperature to melt the mixture;
  • 19. The method of claim 18 wherein the thermoplastic olefin composition has a Maximum Shore A hardness is from about 80 to about 100 and the compression set is from about 67% to about 100%.
  • 20. The method of claim 18 wherein the polypropylene-ethylene copolymer contains 8 to 40 weight percent ethylene and has a melt flow rate from 0.1 to 100 dg/min and a melting point from 125° C. to 160° C.
  • 21. The method of claim 18 wherein the polypropylene-ethylene copolymer has a 1% flexural secant modulus from about 15,000 psi to about 35,000 psi.
  • 22. The method of claim 18 wherein the polypropylene-ethylene copolymer has a 1% flexural secant modulus of about 25,000 psi.
  • 23. The method of claim 18 further comprising a plastomer or a compatiblizer.
  • 24. The method of claim 23 wherein the plastomer is a metallocene catalyzed polyethylene plastomer or a Ziegler catalyzed polyethylene plastomer.
  • 25. The method of claim 18, wherein the polypropylene-ethylene copolymer is made by the method comprising: homopolymerizing propylene in a first reactor maintained at 50° C. to 100° C. and 250 psig to 650 psig in the presence of a catalyst system comprising a titanium-containing catalyst component and organoaluminum cocatalyst component to produce a first product; feeding the first product into a second reactor maintained at 25° C. to 80° C. and 100 psig to 500 psig wherein propylene is copolymerized with ethylene, to obtain high rubber content modified polypropylene having reduced hexane extractables and improved paintability.
  • 26. The method of claim 25 wherein: (a) a control parameter Qc is calculated using eight integrated areas of the 13C NMR spectrum corresponding to molecular structural features for copolymers of propylene and ethylene in accordance with the equation: Qc=A/B
US Referenced Citations (6)
Number Name Date Kind
5314746 Johnson et al. May 1994 A
5587436 Klimek et al. Dec 1996 A
5705576 Buehler et al. Jan 1998 A
5747592 Huff et al. May 1998 A
6207754 Yu Mar 2001 B1
6498214 Laughner et al. Dec 2002 B2
Related Publications (1)
Number Date Country
20040249080 A1 Dec 2004 US