Ethylene copolymer having multiple pitch molecular weight distribution and the method of preparing the same
View Patent ↗Disclosed are an ethylene polymerization process, a catalyst for use in the process, a production method employing the catalyst, and a product produced thereby. More specifically, disclosed is a process of producing an ethylene copolymer from ethylene and an alpha-olefin comonomer, in which the produced ethylene copolymer has a multimodal molecular weight distribution and excellent processability and physical properties, and thus can increase the value and productivity of products, including pipes and films. Particularly, the produced ethylene copolymer has a trimodal or higher molecular weight distribution or density distribution, and thus, when it is a linear low-density copolymer, it has an excellent effect of improving the impact strength of films, and when it is a medium-density ethylene copolymer, it can be produced into pipes, which have slow crack growth rate and can be used even at high temperature.
1. A method for producing an ethylene copolymer having a multimodal molecular weight distribution, the method being carried out by a multistage solution polymerization using at least three polymerization reactors adiabatically operated under stirring, and comprising the steps of:
(a) polymerizing ethylene with at least one C4-C10 α-olefin in a first reactor using a metallocene catalyst represented by the following formula 1, which comprises a cyclopentadienyl group containing ligand around a transition metal and aryloxide ligand or ligands substituted with aryl derivatives at the ortho-positions, the ligands not being bridged, thus producing a first copolymer solution in which a polymer fraction has a density of 0.860-0.920 g/cm 3 and a melt index (MI) of 0.001-1.0 g/10 min.
(b) passing the first copolymer solution through a second reactor, which contains the same metallocene catalyst as used in step (a), ethylene and at least one C4-C10 α-olefin, at a temperature higher than the reaction temperature of step (a), thus producing a second copolymer solution in which a polymer fraction has a density of 0.900-0.940 g/cm 3 and a melt index (MI) of 0.1-10.0 g/10 min; and
(c) passing the second copolymer solution through a third reactor, which contains a Ziegler-Natta catalyst different from the catalyst used in step (b), ethylene and at least one C4-C10 α-olefin, at a temperature higher than the reaction temperature of step (b), thus producing a third copolymer solution:
wherein M is a group-IV transition metal in the periodic table; Cp is cyclopentadienyl or a derivative thereof, which can form an η 5 -bond with the central metal; R 1 , R 2 , R 3 , R 4 , R 5 , R 6 , R 7 , R 8 and R 9 on the aryloxide ligands are each independently a hydrogen atom, a halogen atom, a C1-C20 linear or nonlinear alkyl group optionally substituted with at least one halogen atom, a silyl group containing a C1-C20 linear or nonlinear alkyl group optionally substituted with at least one halogen atom, a C6-C30 aryl group optionally substituted with at least one halogen atom, an C7-C30 arylalkyl group optionally substituted with at least one halogen atom, an alkoxy group having a C1-C20 linear or nonlinear alkyl group optionally substituted with at least one halogen atom, a siloxy group substituted with C3-C20 alkyl or C6-C20 aryl, an amido or phosphido group having a C1-C20 hydrocarbon group, or a mercapto or nitro group substituted with C1-C20 alkyl, wherein these substituents may also optionally bind to each other to form a ring; and X is selected from the group consisting of a halogen atom, a C1-C20 alkyl group other than a Cp derivative, a C7-C30 arylalkyl group, an alkoxy group having a C1-C20 alkyl group, a siloxy group substituted with C3-C20 alkyl, and an amido group having a C1-C20 hydrocarbon group; and n is an integer between 1 and 3.
2. The method of claim 1 , wherein ethylene copolymer fractions obtained from the first copolymer solution, the second copolymer solution and the third copolymer solution are 2-20 wt % , 5-78 wt % and 20-75 wt %, respectively, based on the weight of the polymer obtained through steps (a)-(c).
3. The method of claim 1 , wherein the first reactor is operated at a temperature of 70-190° C.
4. The method of claim 1 , wherein the second reactor is operated at a temperature of 110-200° C.
5. The method of claim 1 , wherein the third reactor is operated at a temperature of 170-300° C.
6. The method of claim 1 , wherein the ethylene copolymer passed through the first and second reactors has a molecular weight distribution index of more than 3.
7. The method of claim 1 , wherein the alpha-olefin which is a comonomer for ethylene in each of the steps is 1-butene, 1-pentene, 1-hexene, 4-methyl-1-pentene, 1-heptene, 1-octene or 1-decene.