Super absorbent polymer and method for preparing same
US-10711074-B2 · Jul 14, 2020 · US
US9650460B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-9650460-B2 |
| Application number | US-201414442674-A |
| Country | US |
| Kind code | B2 |
| Filing date | Jun 30, 2014 |
| Priority date | Jun 28, 2013 |
| Publication date | May 16, 2017 |
| Grant date | May 16, 2017 |
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The present invention relates to a long-chain branched elastic terpolymer capable of satisfying excellent processability and elasticity (flexibility) at the same time, which is obtained in the presence of a Group IV transition metal catalyst, and a preparation method thereof. The elastic terpolymer is a copolymer of ethylene, an alpha-olefin having 3 to 20 carbon atoms, and a diene, wherein i) its weight average molecular weight measured by GPC is 100,000 to 500,000, and ii) x which is the ethylene content (% by weight) and y which is the density value (g/cm 3 ) of the copolymer measured when the ethylene content is X satisfy a relationship of 0.0000175214x(x−75.65420571)+0.875≦y≦0.0000175214x(x−75.65420571)+0.881.
Opening claim text (preview).
The invention claimed is: 1. An elastic terpolymer, wherein the elastic terpolymer is a copolymer of ethylene, an alpha-olefin having 3 to 20 carbon atoms, and a diene, obtained in the presence of a Group IV transition metal catalyst, wherein i) its weight average molecular weight measured by GPC is 100,000 to 500,000, and ii) x which is an ethylene content (% by weight) and y which is a density value (g/cm 3 ) of the copolymer measured when the ethylene content is X satisfy a relationship of 0.0000175214x(x−75.65420571)+0.875≦y≦0.0000175214x(x−75.65420571)+0.881. 2. The elastic terpolymer of claim 1 , wherein an LCB Index which is a ratio of 1 st harmonics of storage modulus to 5 th harmonics of storage modulus measured at 125° C. using a rubber process analyzer according to a LAOS (Large Angles of Oscillation and high Strains) method has a positive value. 3. The elastic terpolymer of claim 2 , wherein the LCB Index is more than 0 and 5 or less. 4. The elastic terpolymer of claim 1 , wherein Re*Rc is less than 1, in which Re*Rc is a product of a reactivity ratio Re representing the distribution of ethylene in the copolymer and a reactivity ratio Rc representing the distribution of alpha-olefin in the copolymer, and Re=k11/k12 and Rc=k22/k21, wherein k11 is a growth reaction rate constant when ethylene binds next to ethylene in the copolymer chain, k12 is a growth reaction rate constant when alpha-olefin binds next to ethylene in the copolymer chain, k21 is a growth reaction rate constant when ethylene binds next to alpha-olefin in the copolymer chain, and k22 is a growth reaction rate constant when alpha-olefin binds next to alpha-olefin in the copolymer chain. 5. The elastic terpolymer of claim 4 , wherein, Re*Rc is 0.60 to 0.99. 6. The elastic terpolymer of claim 1 , wherein the copolymer of ethylene, the alpha-olefin having 3 to 20 carbon atoms, and the diene is a copolymer of 40 to 80% by weight of ethylene, 15 to 55% by weight of the alpha-olefin having 3 to 20 carbon atoms, and 4 to 6% by weight of the diene. 7. The elastic terpolymer of claim 1 , wherein the elastic terpolymer has a density of 0.840 to 0.895 g/cm 3 . 8. The elastic terpolymer of claim 1 , wherein the elastic terpolymer has Mooney viscosity (1+4{circle around (a)}125° C.) of 5 to 180. 9. The elastic terpolymer of claim 1 , wherein the elastic terpolymer has a molecular weight distribution of 2 to 4. 10. The elastic terpolymer of claim 1 , wherein the alpha-olefin is one or more selected from the group consisting of propylene, 1-butene, 1-hexene, and 1-octene, and the diene is one or more selected from the group consisting of 5-ethylidene-2-norbornene, 5-methylene-2-norbornene, and 4-hexadiene. 11. A method for preparing the elastic terpolymer of claim 1 , comprising the step of continuously feeding a monomer composition containing 40 to 80% by weight of ethylene, 15 to 55% by weight of the alpha-olefin having 3 to 20 carbon atoms, and 4 to 6% by weight of the diene to a reactor to perform copolymerization in the presence of a catalytic composition including a first transition metal compound represented by the following Chemical Formula 1 and a second transition metal compound represented by the following Chemical Formula 2: wherein R 1 to R 13 are the same as or different from each other, and are each independently hydrogen, an alkyl radical having 1 to 20 carbon atoms, an alkenyl radical having 2 to 20 carbon atoms, an aryl radical having 6 to 20 carbon atoms, a silyl radical, an alkylaryl radical having 7 to 20 carbon atoms, an arylalkyl radical having 7 to 20 carbon atoms, or a hydrocarbyl-substituted metalloid radical of a Group IV metal; of R 1 to R 13 , two different neighboring groups are connected to each other by an alkylidine radical containing an alkyl having 1 to 20 carbon atoms or an aryl radical having 6 to 20 carbon atoms to form an aliphatic or aromatic ring; M is a Group IV transition metal; and Q 1 and Q 2 are the same as or different from each other, and are each independently a halogen radical, an alkyl radical having 1 to 20 carbon atoms, an alkenyl radical having 2 to 20 carbon atoms, an aryl radical having 6 to 20 carbon atoms, an alkylaryl radical having 7 to 20 carbon atoms, an arylalkyl radical having 7 to 20 carbon atoms, an alkylamido radical having 1 to 20 carbon atoms, an arylamido radical having 6 to 20 carbon atoms, or an alkylidene radical having 1 to 20 carbon atoms. 12. The method of claim 11 , wherein the first transition metal compound is one or more selected from the group consisting of the following compounds: wherein R 2 and R 3 are the same as or different from each other and are each independently hydrogen or a methyl radical, M is a Group IV transition metal, and Q 1 and Q 2 are the same as or different from each other and are each independently a methyl radical, a dimethylimido radical, or a chlorine radical. 13. The method of claim 11 , wherein the second transition metal compound is one or more selected from the group consisting of the following compounds: wherein R 2 and R 3 are the same as or different from each other and are each independently hydrogen or a methyl radical, M is a Group IV transition metal, and Q 1 and Q 2 are the same as or different from each other and are each independently a methyl radical, a dimethylimido radical, or a chlorine radical. 14. The method of claim 11 , wherein the catalytic composition further includes one or more co-catalytic compounds selected from the group consisting of the following Chemical Formula 3, Chemical Formula 4, and Chemical Formula 5: —[Al(R)—O] n — [Chemical Formula 3] wherein R's are the same as or different from each other and are each independently a halogen, a hydrocarbon having 1 to 20 carbon atoms, or a halogen-substituted hydrocarbon having 1 to 20 carbon atoms, and n is an integer of 2 or more; D(R) 3 [Chemical Formula 4] wherein R is the same as defined in Chemical Formula 3, and D is aluminum or boron; and [L-H] + [ZA 4 ] − or [L] + [ZA 4 ] − [Chemical Formula 5] wherein L is a neutral or cationic Lewis acid, H is a hydrogen atom, Z is an element of Group 13, and A's are the same as or different from each other and are each independently an aryl group having 6 to 20 carbon atoms or an alkyl group having 1 to 20 carbon atoms, in which one or more hydrogen atoms are unsubstituted or substituted with a halogen, a hydrocarbon having 1 to 20 carbon atoms, an alkoxy, or a phenoxy. 15. The method of claim 11 , wherein the alpha-olefin is one or more selected from the group consisting of propylene, 1-butene, 1-hexene, and 1-octene, and the diene is one or more selected from the group consisting of 5-ethylidene-2-norbornene, 5-methylene-2-norbomene, and 4-hexadiene. 16. The method of claim 11 , wherein copolymerization is performed while continuously feeding the monomer composition, the first and second transition metal compounds, and the co-catalyst in a solution state to a reactor. 17. The method of claim 16 , wherein the copolymerization step is continuously performed while continuously discharging the copolymerized elastic terpolymer from the reactor. 18. The method of claim 11 , wherein the copolymer
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