This invention relates generally to synthetic polymers, generally with improved balance of processability, resilience and durability. These polymers are generally of the ethylene, alpha-olefin, diene terpolymer type.
Drawings
Claims91
A solid multimodal polymer composition comprising units derived from ethylene, alpha-olefin and diene, the polymer composition comprising:
a) at least 50 weight percent based on the total polymer weight of a first fraction having a Mooney viscosity of over 120 (1+4@125° C.);
and
b) from 5 to 50 weight percent based on the total polymer weight of a second fraction having a Mooney viscosity of 120 or less (1+4@125° C.) and a Mn of at least 3500 g/mol,
wherein the polymer composition has a tan (δ) of 0.5 or less when measured at 125° C. and at a frequency of 10.4 rad/sec, and an overall Mooney viscosity of at least 30(1+4@125° C.).
1 more element
The composition of claim I wherein the first and second fractions comprise less than 10 wt % of diene based on the total weight of ethylene, alpha-olefin, and diene.
A solid multimodal polymer composition comprising units derived from ethylene, alpha-olefin and diene, the polymer comprising:
a) at least 60 weight percent based on the total polymer weight of a first fraction having a Mooney viscosity of over 120 (1+4@125° C.);
and
b) from 5 to 40 weight percent based on the total polymer weight of a second fraction having a Mooney viscosity of 120 or less (1+4@125° C.) and a Mn of at least 3500 g/mol,
wherein the polymer composition has a tan (δ) of 0.5 or less when measured at 125° C. and at a frequency of 10.4 rad/sec, and an overall Mooney viscosity of at least 30 (1+4@125° C.).
1 more element
A solid multimodal polymer composition comprising units derived from ethylene, alpha-olefin and diene, the polymer composition comprising:
a) at least 50 weight percent based on the total polymer weight of a first fraction having a Mooney viscosity of over 120 (1+4@125° C.) and a molecular weight distribution of 3.0 or less;
and
b) from 5 to 50 weight percent based on the total polymer weight of a second fraction having a Mooney viscosity of 120 or less (1+4@125° C.), a molecular weight distribution of 3 or less, and a Mn of at least 25000 g/mol,
wherein the polymer composition has a tan (δ) of 0.5 or less when measured at 125° C. and at a frequency of 10.4 rad/sec, and an overall Mooney viscosity of at least 30 (1+4@125° C.).
1 more element
A multimodal polymer composition comprising from 40 to 90 mole percent ethylene derived units, from 0.2 to 5.0 mole percent non-conjugated diene derived units, and the remainder of the polymer units comprised of propylene derived units;
said polymer composition being essentially free of oil additive and having a tan(δ) less than 0.5 when measured at 125° C. and at a frequency of 10.4 rad/sec, an overall Mooney viscosity of from 30 to 100 (1+4@125° C.), a branching index of at least 0.7, and said polymer composition comprising:
a) at least 50 weight percent based on the total polymer weight of a first fraction having a Mooney viscosity of over 120 (1+4@125° C.) and a molecular weight distribution of 3 or less;
and
b) from 5 to 50 weight percent based on the total polymer weight of a second fraction having a Mooney viscosity lower than 120 (1+4@125° C.), a Mn of at least 3500 and a molecular weight distribution of 3 or less;
and
wherein the amount (wt %) of ethylene derived units in the first and second fraction differ by no more than 20%.
3 more elements
A process for the preparation of multimodal polymer composition comprising:
contacting in a first reactor activated metallocene catalyst with ethylene, diene and propylene monomers thereby producing an effluent containing a first polymer component;
feeding the effluent to a second reactor wherein activated metallocene catalyst is contacted with additional ethylene, diene and propylene monomers to produce a second polymer component and final product;
and controlling conditions in each reactor in order to obtain a first polymer component having a Mooney viscosity of over 120 (1+4@125° C.) and a second polymer component having a Mooney viscosity of 120 or less (1+4@125° C.) and a Mn of at least 3500 g/mol, and the final product has tan (δ) of 0.5 or less when measured at 125° C. and at a frequency of 10.4 rad/sec, has an overall Mooney viscosity of at least 30 (1+4@125° C.), and contains no more of the second polymer component than the first polymer component.
A vibration damping device comprising a multimodal polymer composition containing units derived from ethylene, alpha-olefin and diene, said polymer composition having a tan (δ) of 0.5 or less when measured at 125° C. and at a frequency of 10.4 rad/sec, and an overall Mooney viscosity of at least 30 (1+4@125° C.);
said polymer comprising:
a) at least 50 weight percent based on the total polymer weight of a first fraction having a Mooney viscosity of over 120 (1+4@125° C.);
and
b) from 5 to 50 weight percent based on the total polymer weight of a second fraction having a Mooney viscosity of 120 or less (1+4@125° C.) and a Mn of at least 3500 g/mol.
10/360,973Filed 7 Feb 2003 · us provisional application
Priority
8 Feb 2002
Published
US 2003/0162926 A128 Aug 2003
Granted
3 Feb 2004
Term ended
23 Feb 2023Estimated · howhide20 years from earliest known nonprovisional domestic filing plus recorded patent term adjustment, including 16 days of adjustment. Maintenance-fee lapses, terminal disclaimers and statutory extensions have not been checked. The continuity chain may be incomplete; this is not an enforceability determination.
Containing two or more polymers of the same C08L -group: containing two or more polymers of the same hierarchy C08L, and differing only in…
Life of this patent
Term ended 23 Feb 2023 (estimated)
Priority8 Feb 2002
Granted3 Feb 2004
Term ended23 Feb 2023
Priority8 Feb 2002
Granted3 Feb 2004
Term ended23 Feb 2023
Priority claimedParent application 60/355,779
Application filedUS 10/360,973
Assigned to Exxonmobil Chemical Patents Inc.assignment of assignor's interest
PublishedUS 2003/0162926 A1
GrantedUS 6,686,419 B2
Term endedEstimated, includes 16 days of adjustment
Description10,265 words
Summary2,610 words
#This invention relates generally to multimodal ethylene, alpha-olefin and diene polymer compositions, processes for making them and to devices comprising such compositions. These compositions have been found to have an improved balance of processability, resilience and durability.
#Elastomers useful in applications requiring high resilience have in general a high elasticity in the medium to high frequency range (typically between 5 and 600 rad/sec) which results in low loss tangent (tan δ), at temperatures ranging from approximately room temperature to over 100° C. Natural rubber is an elastomer of this type.
#Ethylene elastomers contain sufficient copolymerised alpha-olefin to produce amorphous to semi-crystalline compounds of density generally below 0.9. In the class of ethylene based elastomers, such as EPDM elastomers, polymers of very high molecular weight (as measured by their Mooney viscosity) are usually required for high resilience applications. Although high molecular weight EPDM elastomers are commercially available, their inherently very high viscosity (Mooney viscosity in general greater than 200) creates difficulties in processability which requires them to be produced with the addition of extender oil to reduce their apparent viscosity. Very high molecular weight polymers are not only difficult to separate from their polymerization solvent without inducing significant macromolecular chain breakage, but they are difficult to mix and compound. The addition of extender oil to the elastomer eases processability in terms of production process recovery, elastomer mixing and compounding.
Brief description of the drawings1 figure
#FIGS. 1, 2 and 3 are graphs of the tan delta versus frequency of several comparative and inventive compositions.
Detailed description7,636 words
#The polymer compositions of this invention comprise units derived from ethylene, alpha-olefin and diene. Such “EPDM-type” or “EODM” terpolymers are well known in the art. The alpha olefin is preferably one or more C3 to C8 alpha olefins, more preferably propylene or butene, most preferably propylene. The diene is preferably a non-conjugated diene selected from the group consisting of 5-ethylidene-2-norbornene (ENB), 1,4-hexadiene, 1,6 octadiene, 5-methyl-1,4-hexadiene, 3,7-dimethyl-1,6-octadiene, dicyclopentadiene (DCPD), norbornadiene, 5-vinyl-2-norbornene (VNB), and combinations thereof, most preferably ENB.
#In a preferred embodiment, the maximum amount of ethylene derived units is 90 mole percent (corresponding to 85 wt % in EPDM), more preferably 80 mole percent and most preferably 75 mole percent based on the total moles of monomer. The preferred minimum amount of ethylene derived units is 35 mole percent, more preferably 40 mole percent, even more preferably 50 mole percent based on the total moles of monomer. The diene content maximum is preferably 5.0 mole percent (15 wt %), more preferably 3.0 mole percent even more preferably 2.5 mole percent, with the preferred minimum being 0.2 mole percent (0.7 wt %), more preferably 0.3 mole percent, and even more preferably 0.5 mole percent. The balance of the polymer units is preferably made up of alpha olefin. Ethylene content is determined by FTIR, ASTM D3900, and is not corrected for diene content. ENB content is determined by FTIR, ASTM D6047. Other dienes can be measured via 1H NMR. All ranges disclosed herein are inclusive unless otherwise noted.
#One well known measure of resiliency is tan (δ) which denotes the ratio of the loss modulus G″, to the elastic modulus G′. This quantifies the ability of a material to dissipate mechanical energy into heat versus the purely elastic storage of mechanical motion during one cycle of oscillatory movement. The measurement of tan (δ) can be made by a dynamic analyzer, and may be made by a sweep of frequencies at a fixed temperature, then repeating that sweep of frequencies at several other temperatures, followed by the development of a master curve of tan (δ) versus frequency by curve alignment. An alternate method is to measure tan (δ) at constant frequency and strain over a temperature range. As used herein tan (δ) is measured at 10.4 rad/sec and 13.95 % strain using A Rubber Processing Analyzer RPA 2000 (by Alpha Technologies Co).