Flame retardant shaped articles

Abstract
A shaped article is disclosed. The article includes a polymer composition that includes an olefinic polymer; a polar polymer; and a third polymer. The third polymer is a graft or block copolymer having first and second polymer portions. The first polymer portion is compatible with the olefinic polymer and the second polymer portion is compatible with the polar polymer. The polymer composition has a limiting oxygen index of at least about 25.
Description


BACKGROUND

[0002] This invention relates to articles made from polymer compositions, and more particularly to articles made from flame-retardant polymer compositions.


[0003] Polymer compositions can include polar polymers and olefinic polymers. These polymer compositions often include one or more additional compounds that act as compatibilizers for the polar and olefinic polymers. In addition, they can include additives that render the compositions flame retardant.



SUMMARY

[0004] The invention relates to polymer compositions. These compositions can exhibit good flame retardancy and/or low smoke generation. The polymer compositions can provide good mechanical properties, such as tensile strength. The compositions can have a combination of desirable properties, such as high tensile strength, high flex modulus, and a high limiting oxygen index.


[0005] The compositions can be suitable for use in shaped articles such as pipes, conduits, tube beams, and ducts, particularly for wire and cable applications. For example, the compositions can be used to make optical fiber conduits and extruded cable jackets. Thus, flame retardant conduits and pipes can be prepared using the compositions described herein. The polymer compositions can be substantially halogen-free. The compositions can be in the form of a blend.


[0006] In one aspect, the invention features a shaped article including a polymer composition. The polymer composition includes: an olefinic polymer; a polar polymer; and a third polymer. The third polymer is a graft or block copolymer with first and second polymer portions, the first polymer portion being compatible with the olefinic polymer and the second polymer portion being compatible with the polar polymer. The polymer composition has a limiting oxygen index (LOI) of at least about 25.


[0007] The article may be, e.g., a pipe, a tube, a conduit (e.g., an optical fiber conduit), or a duct. Preferably, the weight ratio of the polar polymer to the olefinic polymer is 1:1 or greater. For example, the weight ratio of the polar polymer to the olefinic polymer can be between 1:1 and 10:1 or between 1:1 and 5:1.


[0008] Preferably, the polymer composition contains a sufficient amount of the third polymer such that the tensile strength of the composition is improved by at least about 20%, relative to a composition without the third polymer. For example, the tensile strength can be improved by at least about 30%, 40%, 50%, 60%, or 70%. In preferred embodiments, both the olefinic polymer and the polar polymer are substantially free of halogens. The entire composition can be essentially free of halogens.


[0009] The article can consist essentially of the polymer composition. Preferably, the polymer composition has a limiting oxygen index of at least about 30, 35, or 40. In addition, the composition preferably has a tensile strength of at least 1500 psi or 1800 psi and/or a flex modulus of at least 80 Kpsi or 85 Kpsi.


[0010] A “shaped article” is an article that is rigid enough to maintain its shape. A shaped article can be made with a material having a flex modulus of about 80 to about 200 Kpsi and a tensile strength of about 1500 psi or greater.


[0011] The details of one or more embodiments of the invention are set forth in the detailed description below. Other features, objects, and advantages of the invention will be apparent from the description, and from the claims.







DETAILED DESCRIPTION

[0012] The preferred compositions include an olefinic polymer, a polar polymer and a compatibilizer. The compatibilizer can be a block or graft copolymer. The compatibilizer includes at least one olefinic polymer portion that is compatible with the olefinic polymer, and at least one polar polymer portion that is compatible with the polar polymer. The polymer portions can be in the form of blocks.


[0013] Typically, the compositions are in the form of a blend in which the components of the composition are intermixed. The blend can be a homogeneous blend.


[0014] Olefinic polymers are formed primarily of olefin monomers which are hydrocarbon monomers having at least one carbon-carbon double bond. Olefin monomers can be straight chained, branched or cyclic hydrocarbons. Examples of olefin monomers include ethylene, propylene, butylene and pentene. Examples of olefinic polymers include polyethylene, ethylene copolymers, polypropylene, propylene copolymers, ethylene propylene copolymers and polymethylpentene polymers.


[0015] In addition to olefin monomers, an olefinic polymer can include a minor amount of non-olefinic monomers, such as ethylene acrylic monomers. Preferably, an olefinic polymer includes less than about 20 weight percent non-olefinic monomers, more preferably less than about 10 weight percent non-olefinic monomers and most preferably less than about 5 weight percent non-olefinic monomers.


[0016] Preferably, an olefinic polymer includes at least about 80 weight percent olefin monomers, more preferably at least about 90 weight percent olefin monomers, and most preferably at least about 95 weight percent olefin monomers.


[0017] Olefinic polymers preferably include less than about 2 weight percent halogen, more preferably less than about 1 weight percent halogen and most preferably less than about 0.5 weight percent halogen.


[0018] Olefinic polymers are available from, for example, Exxon, Mobil, Chevron, Amoco, Dow, Quantum, Solvay, Novacor, Rexene, Aristech, Hoechst Celanese, Fina, Montall and Shell.


[0019] A polar polymer includes olefin monomers and polar monomers having the formula CH2═CHOCOR, where R is a hydrocarbon group that can be straight chained or branched, saturated or unsaturated, and substituted or unsubstituted. Typically, R is a straight chained, saturated and unsubstituted alkyl group having from one to five carbon atoms, such as a methyl group, an ethyl group or a butyl group. In a polar polymer, a portion of the polar monomers can be hydrolyzed.


[0020] A polar polymer can include additional functional monomers such as carbon monoxide, acrylic monomers, glycidyl acrylic monomers, acid monomers, anhydride monomers and/or nitrile monomers.


[0021] Preferably, a polar polymer includes from about 20 weight percent to about 90 weight percent olefinic monomers, more preferably from about 35 weight percent to about 85 weight percent olefinic monomers, and most preferably from about 50 weight percent to about 80 weight percent olefinic monomers.


[0022] Preferably, a polar polymer includes from about 10 weight percent to about 80 weight percent polar monomers, more preferably from about 15 weight percent to about 65 weight percent polar monomers, and most preferably from about 20 weight percent to about 50 weight percent polar monomers.


[0023] Preferably, a polar polymer includes at most about 15 weight percent additional functional monomers, more preferably from about 2.5 weight percent to about 10 weight percent additional functional monomers.


[0024] Polar polymers preferably include less than about 2 weight percent halogen, more preferably less than about 1 weight percent halogen, and most preferably less than about 0.5 weight percent halogen.


[0025] In a preferred embodiment, the polar polymer is a terpolymer of ethylene monomers, vinyl acetate monomers and carbon monoxide.


[0026] Polar polymers are available from, for example, Exxon, Quantum, DuPont, Union Carbide, AT Plastics, Chevron, Bayer, Mitsubishi Petrochemicals and Sumitomo.


[0027] The compatibilizer is typically a graft or block copolymer that includes at least one olefinic polymer portion and at least one polar polymer portion. The polymer portions can be in the form of blocks.


[0028] The olefinic polymer portion is formed of an olefinic polymer, and the polar polymer portion is formed of a polar polymer. The olefinic polymer portion should be selected to be compatible with the olefinic polymer, and the polar polymer portion should be selected to be compatible with the polar polymer. Generally, the olefinic polymer portion of the compatibilizer and the olefinic polymer have substantially the same polarity, and the polar polymer portion of the compatibilizer and the polar polymer have substantially the same polarity.


[0029] Preferably, the olefinic polymer portion of the compatibilizer is the same polymer as the olefinic polymer. For example, if the olefinic polymer is polyethylene, the olefinic polymer portion of the compatibilizer is also polyethylene.


[0030] Preferably, the polar polymer portion of the compatibilizer includes functional groups that are the same as the functional groups in the polar polymer. For example, if the polar polymer is ethylene vinyl acetate, the polar polymer portion of the compatibilizer includes vinyl acetate monomers.


[0031] The polymer compositions can include from about 15 weight percent to about 65 weight percent ethylenic polymer, from about 20 weight percent to about 80 weight percent polar polymer, and from about 1 weight percent to about 40 weight percent compatibilizer.


[0032] The olefinic polymer portions and polar polymer portions of the compatibilizer can be directly chemically bonded or they can be connected by a linking agent that is chemically bonded to an olefinic polymer portion and an adjacent polar polymer portion.


[0033] When a linking agent is not used, the compatibilizer can be formed by reacting two polymers that contain functional groups that react to provide the compatibilizer. This reaction can occur in a mixture that contains the olefinic polymer and the polar polymer. Alternatively, the compatibilizer can first be formed then added to a mixture that contains the olefinic polymer and the polar polymer.


[0034] An amine and/or epoxy containing polymer, such as a nitrile rubber, can be reacted with an acid or anhydride containing polyolefin. An acid or anhydride containing polymer, such as a nitrile rubber, can be reacted with an amine and/or epoxy containing polyolefin. An isocyanate containing polyester (typically having a low molecular weight) can be reacted with an acid, anhydride or epoxy containing polyolefin. A compatibilizer can be formed by reacting an epoxy containing terpolymer of ethylene, vinyl acetate and carbon monoxide with a maleic acid modified polypropylene. A compatibilizer can be formed by reacting an ethylene methyl acrylate acid containing polar polymer with an epoxy containing styrene ethylene butylene styrene block copolymer.


[0035] Preferably, the functional groups that react to form the compatibilizer are at the terminus of the polymers.


[0036] Examples of linking agents include diepoxides, diamines and diisocyanates which can be reacted with an acid modified polar polymer and an acid modified olefinic polymer to provide a compatibilizer.


[0037] The polymer compositions can be prepared using standard mixing methods. For example, the polymer compositions can be formed using a Banbury mixer, a Brabender mixer and/or a twin screw mixer. Generally, twin screw mixers provide a higher shear during mixing, so polymer compositions formed using a twin screw extruder can exhibit better elongation and tensile properties. The polymer compositions can also include silicones, stabilizers, flame retardants, plasticizers, colorants, reinforcing fillers, lubricants, and/or compounds that improve the hydrolytic stability of esters. Preferably, the total amount of these compounds in the polymer compositions is from about 50 to about 200 parts per 100 parts of total amount of polymer (ethylenic polymer, polar polymer and compatibilizer). When the composition includes anti-oxidants or lubricants, these compounds make up from about 100 parts per million to about 10 weight percent of the composition relative to the total amount of polymer (ethylenic polymer, polar polymer and compatibilizer).


[0038] Examples of compounds that improve the stability of esters include polycarbodiimides, such as aromatic polycarbodiumides. These compounds are available from, for example, Bayer.


[0039] Examples of colorants include organic and inorganic colorants. Colorants are available from, for example, Ciba Geigy, BASF, Ferro, ICI, Harwick and Teknor Apex.


[0040] Examples of flame retardants include aluminum trihydrate, magnesium hydroxide, phosphorus compounds, nitrogen compounds, zinc borates, halogenated compounds, and Ultracarb (Microfine Minerals). Flame retardants are available from, for example, Lonza, Alcoa, Alcan, Huber, Martin Marietta, Hoechst Celanese, U.S. Borax, Melamine Chemicals, Microfine Minerals and Anzon. The compositions preferably include enough flame retardant such that the compositions have a limiting oxygen index of at least about 25.


[0041] Examples of stabilizers include heat stabilizers, metal deactivators and ultraviolet stabilizers. Stabilizers are available from, for example, Ciba Geigy, Sandoz, Cytec, Eastman Chemicals, Fairmount Chemicals, Hoechst Celanese and General Electric.


[0042] Examples of plasticizers include phosphate ester plasticizers, phosphoric esters, fatty acid esters, esters of azelaic acid, esters of sebacic acid, trimellitic esters and polymeric plasticizers. When the polymer compositions are used in flame retardant applications, phosphate ester plasticizers are preferably used. Plasticizers are available from, for example, Solutia, Teknor Apex, Ferro, Exxon, Eastman Chemical and Uniflex Chemical.


[0043] Lubricants are available from, for example, Akzo, Dow Corning, DuPont, Astor Wax, Henkel, Witco and Struktol.


[0044] Silicones are available from, for example, General Electric, Wacker silicones and Dow Corning.


[0045] Examples of reinforcing fillers include clay, silica and calcium carbonate. Reinforcing fillers are available from, for example, Huber, Engelhard and PPG.


[0046] The polymer compositions preferably have an elongation of at least about 50% as measured according to ASTM D-638.


[0047] The polymer compositions preferably have a tensile strength of at least about 1800 as measured according to ASTM D-638.


[0048] The polymer compositions preferably have a flex modulus of at least about 80 Kpsi as measured according to ASTM D-790.


[0049] The polymer compositions preferably have a peak smoke rating of less than 2/meter as measured using cone calorimetry according to ASTM E-1354.


[0050] When prepared for use as a flame retardant material, the polymer compositions preferably have a limiting oxygen index of at least about 25 as measured by ASTM D-2863. More preferably, the compositions have a limiting oxygen index of at least about 30, 35, or 40.


[0051] Tables I-V list polymer compositions and their properties. Compositions 1-9 and 11-25 were prepared using a Brabender mixer (PL 2000 equipped with roller type blades). Composition 10 was prepared using a Banbury mixer, as described below. For compositions 1-9 and 11-25, the speed was adjusted to keep the mixture at about 180° C. The polymers were first mixed, and the filler was slowly added. This mixture was mixed for about five minutes, and the stabilizer was added. This mixture was re-mixed for about one minute, removed from the Brabender mixer and pressed to a thin sheet in a cool press. The resulting material was compression molded at 220° C. This material was then cooled and the properties of the material were evaluated.


[0052] Alternatively, the compositions can be prepared using a twin screw extruder (Berstoff Model 40). All ingredients are metered and added at the feed throat. The temperature is controlled such that the temperatures in the mixing zones is at most about 420° F. The mixing speed is about 120-200 rpm.


[0053] Alternatively, the compositions can be prepared by mixing the olefinic polymers and polar polymers in a Banbury mixer (Farrel Midget Banbury mixer) using a medium rotor speed. When the temperature reaches about 10° C. above the melting point of the polyethylene, the mixing speed is reduced to low for about 5 minutes. About one half of the filler (magnesium hydroxide) is added, and then the remaining half of the filler is added. The mixing speed is reduced, and the stabilizers are added while maintaining a low rotor speed. The resulting mixture is molded as described above. Procedures for preparing polymer compositions are described in more detail in Patel et al., U.S. Pat. No. 6,034,176, which is incorporated by reference in its entirety. The polymer compositions can be formed into shaped articles, such as pipes, using techniques known in the art.


[0054] A number of compositions and their properties are set forth in Tables I-V below.
1TABLE 112345Raw MaterialEthylene Vinyl Acetate60303040copolymer1Ethylene Vinyl Acetate30603030copolymer2HDPE31515151515Ethylene butyl acrylate55553epoxide4Maleic Acid Modified55552Ethylene Vinyl Acetateterpolymer5Maleic Acid Modified1515151510Polyethylene6Magnesium hydroxide7180180180180180Silane coupling agent822222Magnesium hydroxide9Magnesium hydroxide10Magnesium hydroxide11Stearic acid0.500.500.500.500.50Zinc stearate120.400.400.400.400.40Calcium stearate0.200.200.200.200.20Anti-oxidant131.001.001.001.001.00Anti-oxidant140.400.400.400.400.40Hindered amine light0.200.200.200.200.20stabilizer15Resin modifier165.005.005.005.005.00Silicone lubricant173.00Total289.70289.70289.70292.70289.70PropertiesSpecific Gravity1.481.501.491.491.49Hardness, Shore D67/6267/6265/6066/6165/60(Inst/10 sec)Tensile Strength (TAPEs),20902260231023602170psiElongation @ Break7566758569(TAPEs), %Flex Modulus, Kpsi100.092.299.299.598.6LTB, ° C.−21−11−13−12−11Melt Index, g/10 min  0/0.21  0/0.25  0/0.20  0/0.350.26/1.29(190° C./10, 20 kg)Dielectric constant @3.493.403.483.503.551 KHzDissipation factor @0.00900.00780.00270.00270.00281 KHzVolume resistivity,2.1252.2712.4061.4610.874X10{circumflex over ( )}14LOI, %4041414141Peak Heat Release148174154148145Rate @ 50 Kw/sqm,Kw/sqmAverage Heat Release8497918788Rate @ 50 Kw/sqm,Kw/sqmAverage Heat Release115124112124114Rate @ 50 Kw/sqm @3 min, Kw/sqmTotal heat release @17217016316516550 Kw/sqm, MJ/sqmPeak smoke @0.51.51.00.61.050 Kw/sqm, 1/mTime to sustained170175155163154ignition, secViscosity @ 230° C., L/D16/1, 1126N PFCalc. Visc. Pas−1@ Shear rate 100 s−145933844329532282960@ Shear rate 200 s−127532384198220191870@ Shear rate 500 s−114701307105710721030@ Shear rate 1000 s−19498496806786611Elvax 470, commercially available from DuPont 2Elvax 460, commercially available from DuPont 3HDPE HMAO34B, commerically available from Exxon Chemicals 4Elvaloy AS, commercially available from DuPont 5Fusabond C MC 250D, commercially available from DuPont 6Fusabond EMB 100D, commercially available from DuPont 7Magnifin H-10 8commercially available from Dow Corning or OSI 9Magshield, commerically available from Martin Marietta 10Kisuma 5A, commercially available from Kisuma Chemicals BV, the Netherlands 11Kisuma 5B, commercially available from Kisuma Chemicals BV, the Netherlands 12Coad 21 13Irganox 1010, commercially available from Ciba-Geigy 14Irganox 1024 MD, commercially available from Ciba-Geigy 15Chimassorb 944FD, commerically available from Ciba-Geigy 164-7051, commercially available from Dow Corning 17MB 50-314, commercially available from Dow Corning


[0055]

2











TABLE II











6
7
8
9
10





















Raw Material







Ethylene Vinyl Acetate copolymer1
40
30
30
30
30


Ethylene Vinyl Acetate copolymer2
30
30
30
30
30


HDPE3
15
15
15
15
15


Ethylene butyl acrylate epoxide4
3
5
5
5
5


Maleic Acid Modified Ethylene
2
5
5
5
5


Vinyl Acetate terpolymer5


Maleic Acid Modified Polyethylene6
10
15
15
15
15


Magnesium hydroxide7


Silane coupling agent8
2
2
2
2
2


Magnesium hydroxide9
180
180


Magnesium hydroxide10


180

180


Magnesium hydroxide11



180


Stearic acid
0.50
0.50
0.50
0.50
0.50


Zinc stearate12
0.40
0.40
0.40
0.40
0.40


Calcium stearate
0.20
0.20
0.20
0.20
0.20


Anti-oxidant13
1.00
1.00
1.00
1.00
1.00


Anti-oxidant14
0.40
0.40
0.40
0.40
0.40


Hindered amine light stabilizer15
0.20
0.20
0.20
0.20
0.20


Resin modifier16
5.00
5.00
5.00
5.00
5.00


Silicone lubricant17

3.00


3.00


Total
289.70
292.70
289.70
289.70
292.70


Properties


Specific Gravity
1.45
1.50
1.49
1.49
1.49


Hardness, Shore D (Inst/10 sec)
66/61
65/60
63/58
65/59
64/58


Tensile Strength (TAPEs), psi
1770
1820
1870
1920
1880


Elongation @ Break (TAPEs), %
62
79
25
25
26


Flex Modulus, Kpsi
83.6
81.3
93.3
77.3
85.5


LTB, ° C.
>0
>0
>0
>0
>0


Melt Index, g/10 min (190° C./10,
0.23/1.35
0.11/0.68
0.26/1.72
0.15/1.09
0.38/3.17


20 kg)


Dielectric constant @ 1 KHz
3.96
3.81
3.41
3.27
3.32


Dissipation factor @ 1 KHz
0.0108
0.0080
0.0056
0.0050
0.0241


Volume resistivity, X10{circumflex over ( )}14
1.915
1.962
0.453
0.327
4.33


LOI, %
40
38
41
39
41


Peak Heat Release Rate @ 50
156
155
140
136


Kw/sqm, Kw/sqm


Average Heat Release Rate @ 50
80
79
77
80


Kw/sqm, Kw/sqm


Average Heat Release Rate @ 50
126
129
111
102


Kw/sqm @ 3 min, Kw/sqm


Total heat release @ 50 Kw/sqm,
171
160
170
163


MJ/sqm


Peak Smoke @ 50 Kw/sqm, 1/m
0.5
0.8
0.7
0.7


Time to sustained ignition, sec
177
170
165
126


Viscosity @ 230° C., L/D 16/1,


1126N PF


Calc. Visc. Pas−1


@ Shear rate 100 s−1
3500
2912
2603
2499
2128


@ Shear rate 200 s−1
2241
1881
1665
1595
1334


@ Shear rate 500 s−1
1217
1009
930
896
740


@ Shear rate 1000 s−1
755
609
601
586
484








1-17
The raw materials in Table II are the same as those listed in Table I









[0056]

3











TABLE III











11
12
13
14
15





















Raw Material







Ethylene Vinyl Acetate copolymer1
40
40
30
40
60


Ethylene Vinyl Acetate copolymer2
30
30
30
30


HDPE3
15
20
15
20
15


Epoxidized polyethylene4


Ethylene butyl acrylate epoxide5
3
3
5
3
5


Maleic Acid Modified Ethylene
2
2
5
2
5


Vinyl Acetate terpolymer6


Maleic Acid Modified Polyethylene7
10
5
15
5
15


Magnesium hydroxide8
160
160
160

180


Silane treated magnesium hydroxide9
20
20
20
20


Magnesium hydroxide10



160


Silane treated magnesium


hydroxide11


Phosphate plasticizer12


Stearic acid
0.50
0.50
0.50
0.50
0.50


Zinc stearate13
0.40
0.40
0.40
0.40
0.40


Calcium stearate
0.20
0.20
0.20
0.20
0.20


Anti-oxidant14
1.00
1.00
1.00
1.00
1.00


Anti-oxidant15
0.40
0.40
0.40
0.40
0.40


Hindered amine light stabilizer16
0.20
0.20
0.20
0.20
0.20


Resin modifier17
5.00
5.00
5.00
5.00
5.00


Silicone lubricant18


Silane coupling agent 19




2


Total
287.70
287.70
287.70
287.70
287.70


Properties


Specific Gravity
1.49
1.49
1.49
1.51
1.51


Hardness, Shore D (Inst/10 sec)
65/60
58/51
59/52
64/58
68/63


Tensile Strength (TAPEs), psi
2170
1890
1900
1770
2110


Elongation @ Break (TAPEs), %
69
52
28
19
58


Flex Modulus, Kpsi
98.6


LTB, ° C.
−11
−23
−22
−6
−21


Melt Index, g/10 min (190° C./10,
0.26/1.29
0.22/4.46
0.22/2.44
 1.55/11.86
0.10/1.10


20 kg)


Dielectric constant @ 1 KHz
3.55
3.42
3.46
3.38
3.54


Dissipation factor @ 1 KHz
0.0028
0.0032
0.0032
0.0031
0.0036


Volume resistivity, X10{circumflex over ( )}14
0.874


1.880
11.3330


LOI, %
41



41


Peak Heat Release Rate @ 50
145
151
128
127
147


Kw/sqm, Kw/sqm


Average Heat Release Rate @ 50
88
92
79
75
95


Kw/sqm, Kw/sqm


Average Heat Release Rate @ 50
114
116
100
103
131


Kw/sqm @ 3 min, Kw/sqm


Total heat release @ 50 Kw/sqm,
165
150
146
138
157


MJ/sqm


Effective HOC, MJ/kg


Peak Smoke @ 50 Kw/sqm, 1/m
1.0
0.9
0.9
0.6
1.1


Time to sustained ignition, sec
154
119
131
126
102


Viscosity @ 230° C., L/D 16/1,


1126N PF


Calc. Visc. Pas−1


@ Shear rate 100 s−1




3342


@ Shear rate 200 s−1




2114


@ Shear rate 500 s−1




1066


@ Shear rate 1000 s−1




598








1
Elvax 470, commercially available from DuPont







2
Elvax 460, commercially available from DuPont







3
HDPE HMAO34B, commerically available from Exxon Chemicals







4
Lotader 8840, commercially available from Elf Atochem







5
Elvaloy AS, commercially available from DuPont







6
Fusabond C MC 250D, commercially available from DuPont







7
Fusabond EMB 100D, commercially available from DuPont







8
Magnifin H−10, commercially available from Lonza







9
Teknisperse MH100EX, commercially available from TDI







10
Kisuma 5B, commercially available from Kisuma Chemicals BV, the Netherlands







11
Teknisperse 50G (50% Amino G), commercially available from TDI







12
Santicizer 141, commercially available from Solutia







13
Coad 21







14
Irganox 1010, commercially available from Ciba−Geigy







15
Irganox 1024 MD, commercially available from Ciba−Geigy







16
Chimassorb 944FD, commerically available from Ciba−Geigy







17
4−7051, commercially available from Dow Corning 3







18
MB 50−314, commercially available from Dow Corning







19
commercially available from Dow Corning or OSI









[0057]

4











TABLE IV











16
17
18
19
20





















Raw Material







Ethylene Vinyl Acetate copolymer1
60
60
60
60
60


Ethylene Vinyl Acetate copolymer2


HDPE3
15
15
22.1
30.4
15


Epoxidized polyethylene4


Ethylene butyl acrylate
5
5
5
5
5


epoxide5


Maleic Acid Modified Ethylene
5
5
5
5
5


Vinyl Acetate terpolymer6


Maleic Acid Modified Polyethylene7
15
15
15
15
15


Magnesium hydroxide8
180
180
191.4
204.6
180


Silane treated magnesium



1.4
3.1


hydroxide9


Magnesium hydroxide10


Silane treated magnesium


hydroxide11


Phosphate plasticizer12
5
10
5
5


Stearic acid
0.50
0.50
0.50
0.50
0.50


Zinc stearate13
0.40
0.40
0.40
0.40
0.40


Calcium stearate
0.20
0.20
0.20
0.20
0.20


Anti-oxidant14
1.00
1.00
1.00
1.00
1.00


Anti-oxidant15
0.40
0.40
0.40
0.40
0.40


Hindered amine light stabilizer16
0.20
0.20
0.20
0.20
0.20


Resin modifier17
5.00
5.00
5.00
5.00
5.00


Silicone lubricant18

2
2
2
2


Silane coupling agent19
2
2
2
2
2


Total
294.70
299.70
314.60
337.80
289.70


Properties


Specific Gravity
1.48
1.48
1.49
1.49
1.48


Hardness, Shore D (Inst/10 sec)
65/60
62/57
65/60
66/61
66/61


Tensile Strength (TAPEs), psi
1850
1750
2050
2120
2060


Elongation @ Break (TAPEs), %
60
53
43
31
51


Flex Modulus, Kpsi


TS/UE, % Retained (100° C./7 d)
122/57 
124/58 
112/70 
109/71 
110/86 


LTB, ° C.
−20
−28
−24
−19
−28


Melt Index, g/10 min (190° C./10,
1.08/7.28
 1.93/13.36
0.95/6.05
1.53/9.68
0.22/1.8 


20 kg)


Dielectric constant @ 1 KHz
3.52
3.54
3.58
3.55
3.43


Dissipation factor @ 1 KHz
0.0045
0.0035
0.0033
0.0031
0.0039


Volume resistivity, X10{circumflex over ( )}14
1.110
2.670
1.700
1.600
9.110


LOI, %
39
35
39
40
42


Peak Heat Release Rate @ 50
140
142
137
143
159


Kw/sqm, Kw/sqm


Average Heat Release Rate @ 50
83
79
84
88
88


Kw/sqm, Kw/sqm


Average Heat Release Rate @ 50
126
120
121
128
129


Kw/sqm @ 3 min, Kw/sqm


Total heat release @ 50 Kw/sqm,
161
168
163
166
159


MJ/sqm


Effective HOC, MJ/kg
30
30
30
31
30


Peak Smoke @ 50 Kw/sqm, 1/m
0.8
0.8
0.7
0.9
0.9


Time to sustained ignition, sec
90
87
99
96
105


Viscosity @ 230° C., L/D 16/1,


1126 N PF


Calc. Visc. Pas−1


@ Shear rate 100 s−1
1923
1322

1423
3626


@ Shear rate 200 s−1
1328
1027

1178
2068


@ Shear rate 500 s−1
749
638

756
962


@ Shear rate 1000 s−1
456
399

466
531








1-19
The raw materials in Table IV are the same as those listed in Table III









[0058]

5











TABLE V











21
22
23
24
25





















Raw Material







Ethylene Vinyl Acetate copolymer1
60
55
60
60
60


Ethylene Vinyl Acetate copolymer2


HDPE3
15
20
15
15
15


Epoxidized polyethylene4


Ethylene butyl acrylate epoxide5
5
5
5
5


Maleic Acid Modified Ethylene
5
5
5
5
10


Vinyl Acetate terpolymer6


Maleic Acid Modified Polyethylene7
15
15
15
15
10


Magnesium hydroxide8
160
176
176
156
176


Silane treated magnesium hydroxide9
20


Magnesium hydroxide10



20


Silane treated magnesium

4
4
4
4


hydroxide11


Phosphate plasticizer12


Stearic acid
0.50
0.50
0.50
0.50
0.50


Zinc stearate13
0.40
0.40
0.40
0.40
0.40


Calcium stearate
0.20
0.20
0.20
0.20
0.20


Anti-oxidant14
1.00
1.00
1.00
1.00
1.00


Anti-oxidant15
0.40
0.40
0.40
0.40
0.40


Hindered amine light stabilizer16
0.20
0.20
0.20
0.20
0.20


Resin modifier17
5.00
5.00
5.00
5.00
5.00


Silicone lubricant18
2.00
2.00
2.00
2.00
2.00


Total
289.70
289.70
289.70
289.70
289.70


Properties


Specific Gravity
1.49
1.47
1.49
1.48
1.49


Hardness, Shore D (Inst/10 sec)
70/65
70/65
68/63
68/63
68/63


Tensile Strength (TAPEs), psi
2340
2420
2180
2300
2260


Elongation @ Break (TAPEs), %
98
98
60
95
72


Flex Modulus, Kpsi
92.7
106.1
101.4
98.0
82.8


TS/UE, % Retained (100° C./7 d)
104/72 
103/71 
108/72 
106/71 
107/83 


LTB, ° C.
−43
−37
−37
−37
−36


Melt Index, g/10 min(190° C./10,
 0.0/0.37
 0.0/0.58
 0.0/0.56
0.17/1.18
 0.0/0.62


20 kg)


Dielectric constant @ 1 KHz
3.59
3.55
3.58
3.53
3.60


Dissipation factor @ 1 KHz
0.00326
0.00296
0.00284
0.00288
0.00300


Volume resistivity, X10{circumflex over ( )}14
12.460
9.680
9.820
5.530
11.67


LOI, %
41
38
40
40
41


Peak Heat Release Rate @ 50
147
151
155
167
166


Kw/sqm, Kw/sqm


Average Heat Release Rate @ 50
94
98
97
106
100


Kw/sqm, Kw/sqm


Average Heat Release Rate @ 50
128
136
134
135
135


Kw/sqm @ 3 min, Kw/sqm


Total heat release @ 50 Kw/sqm,
165
164
163
176
162


MJ/sqm


Effective HOC, MJ/kg
30
30
30
31
29


Peak Smoke @ 50 Kw/sqm, 1/m
1.2
1.0
1.0
1.0
1.2


Time to sustained ignition, sec
103
102
109
105
107








1-18
The raw materials in Table V are the same as those listed in Table III









[0059] All publications, patents, and patent applications mentioned in this application are herein incorporated by reference to the same extent as if each individual publication, patent, or patent application was specifically and individually indicated to be incorporated by reference.


[0060] A number of embodiments of the invention have been described. Nevertheless, it will be understood that various modifications may be made without departing from the spirit and scope of the invention. Accordingly, other embodiments are within the scope of the following claims.


Claims
  • 1. A shaped article comprising a polymer composition, wherein the polymer composition includes: an olefinic polymer; a polar polymer; and a third polymer, wherein the third polymer is a graft or block copolymer, and wherein the third polymer comprises first and second polymer portions, the first polymer portion being compatible with the olefinic polymer and the second polymer portion being compatible with the polar polymer, wherein the polymer composition has a limiting oxygen index of at least about 25.
  • 2. The article of claim 1, wherein the article is a pipe, a tube, a conduit, or a duct.
  • 3. The article of claim 1, wherein the article is an optical fiber conduit.
  • 4. The article of claim 1, wherein the weight ratio of the polar polymer to the olefinic polymer is 1:1 or greater.
  • 5. The article of claim 1, wherein the weight ratio of the polar polymer to the olefinic polymer is between 1:1 and 10:1.
  • 6. The article of claim 1, wherein the weight ratio of the polar polymer to the olefinic polymer is between 1:1 and 5:1.
  • 7. The article of claim 1, wherein the polymer composition contains a sufficient amount of the third polymer such that the tensile strength of the composition is improved by at least about 20%, relative to a composition without the third polymer.
  • 8. The article of claim 1, wherein the polymer composition contains a sufficient amount of the third polymer such that the tensile strength of the composition is improved by at least about 30%, relative to a composition without the third polymer.
  • 9. The article of claim 1, wherein the polymer composition contains a sufficient amount of the third polymer such that the tensile strength of the composition is improved by at least about 40%, relative to a composition without the third polymer.
  • 10. The article of claim 1, wherein the polymer composition contains a sufficient amount of the third polymer such that the tensile strength of the composition is improved by at least about 50%, relative to a composition without the third polymer.
  • 11. The article of claim 1, wherein the polymer composition contains a sufficient amount of the third polymer such that the tensile strength of the composition is improved by at least about 60%, relative to a composition without the third polymer.
  • 12. The article of claim 1, wherein the polymer composition contains a sufficient amount of the third polymer such that the tensile strength of the composition is improved by at least about 70%, relative to a composition without the third polymer.
  • 13. The article of claim 1, wherein both the olefinic polymer and the polar polymer are substantially free of halogens.
  • 14. The article of claim 1, wherein the composition is essentially free of halogens.
  • 15. The article of claim 1, wherein the article consists essentially of the polymer composition.
  • 16. The article of claim 1, wherein the polymer composition has a limiting oxygen index of at least about 30.
  • 17. The article of claim 1, wherein the polymer composition has a limiting oxygen index of at least about 35.
  • 18. The article of claim 1, wherein the polymer composition has a limiting oxygen index of at least about 40.
  • 19. The article of claim 1, wherein the tensile strength of the polymer composition is at least about 1500 psi.
  • 20. The article of claim 1, wherein the tensile strength of the polymer composition is at least about 1800 psi.
  • 21. The article of claim 1, wherein the flex modulus of the polymer composition is at least about 80 Kpsi.
  • 22. The article of claim 1, wherein the flex modulus of the polymer composition is at least about 85 Kpsi.
  • 23. The article of claim 1, wherein the tensile strength of the polymer composition is at least about 1800 psi and the flex modulus of the polymer composition is at least about 80 Kpsi.
CROSS-REFERENCE TO RELATED APPLICATIONS

[0001] This application claims priority from provisional application No. 60/261,998, filed Jan. 16, 2001.

Provisional Applications (1)
Number Date Country
60261998 Jan 2001 US
Continuations (1)
Number Date Country
Parent 10052818 Jan 2002 US
Child 10215617 Aug 2002 US