Method for producing multimodal polyolefin using multistage continuous polymerization process
This invention relates to a method for producing multimodal polyolefin using multistage continuous polymerization process for producing multimodal polyolefin having superior melt-strength, moldability, mechanical strength, processability, and appearance. A method for producing multimodal polyolefin using multistage polymerization process, comprising the steps of: polymerizing a high molecular weight bimodal polymer by introducing a monomer in the presence of a catalyst composition including two or more different catalysts in a first reactor; and continuously introducing the high molecular weight bimodal polymer produced in the first reactor into a second reactor, and polymerizing a low molecular weight bimodal polymer by introducing a monomer in the presence of the catalyst composition, wherein the multimodal polyolefin includes the high molecular weight bimodal polymer and the low molecular weight bimodal polymer at the same time.
1. A method for producing multimodal polyolefin using multistage polymerization process, comprising the steps of:
polymerizing a high molecular weight bimodal polymer by introducing a monomer in the presence of a catalyst composition including two or more different catalysts in a first reactor; and
continuously introducing the high molecular weight bimodal polymer produced in the first reactor into a second reactor, and polymerizing a low molecular weight bimodal polymer by introducing a monomer in the presence of the catalyst composition,
wherein the multimodal polyolefin includes the high molecular weight bimodal polymer and the low molecular weight bimodal polymer at the same time,
and wherein the high molecular weight bimodal polymer has a weight average molecular weight (Mw) measured with Gel-permeation chromatography (GPC) of equal to or more than 200,000 g/mol, and the low molecular weight bimodal polymer has a weight average molecular weight (Mw) measured with Gel-permeation chromatography (GPC) of less than 200,000 g/mol.
2. The method for producing multimodal polyolefin according to claim 1 , wherein the high molecular weight bimodal polymer satisfies the following properties:
(1) Density(d): 0.930 to 0.965 g/cm 3
(2) Melt flow index (MIF, 190° C., 21.6 kg weight condition): 0.01 to 20 g/10 min
(3) Ratio of weight average molecular weight (Mw) to number average molecular weight (Mn) (Mw/Mn, Molecular weight distribution (MWD)) measured with Gel-permeation chromatography (GPC): 5 to 50
(4) Two or more peaks are shown when molecular weight is measured with Gel-permeation chromatography (GPC),
the low molecular weight bimodal polymer satisfies the following properties:
(5) Density(d): 0.910 to 0.965 g/cm 3
(6) Melt flow index (MIF, 190° C., 21.6 kg weight condition): 10 to 200 g/10 min
(7) Ratio of weight average molecular weight (Mw) to number average molecular weight (Mn) (Mw/Mn, Molecular weight distribution (MWD)) measured with Gel-permeation chromatography (GPC): 5 to 50
(8) Two or more peaks are shown when molecular weight is measured with Gel-permeation chromatography (GPC), and
the multimodal polyolefin satisfies the following properties:
(9) Density(d): 0.930 to 0.965 g/cm 3
(10) Melt flow index (MIF, 190° C., 21.6 kg weight condition): 0.1 to 50 g/10 min
(11) Weight average molecular weight (Mw) measured with Gel-permeation chromatography (GPC): 100,000 to 600,000 g/mol
(12) Ratio of weight average molecular weight (Mw) to number average molecular weight (Mn) (Mw/Mn, Molecular weight distribution (MWD)) measured with Gel-permeation chromatography (GPC): 10 to 60.
3. The method for producing multimodal polyolefin according to claim 1 , wherein a polymerization temperature of the first reactor is higher than that of the second reactor.
4. The method for producing multimodal polyolefin according to claim 1 , wherein a difference between polymerization temperatures of the first reactor and the second reactor is 1 to 20° C.
5. The method for producing multimodal polyolefin according to claim 1 , wherein a hydrogen (H 2 ) concentration in the first reactor is 0 to 300 g/ton C2, and the hydrogen (H 2 ) concentration in the second reactor is 300 to 2,000 g/ton C2.
6. The method for producing multimodal polyolefin according to claim 1 , wherein before polymerizing a high molecular weight bimodal polymer in the first reactor, the method further includes a step of undergoing a pre-polymerization process in one or more reactors.
7. The method for producing multimodal polyolefin according to claim 1 , wherein both of the first reactor and the second reactor are slurry phase reactors or gas phase reactors.
8. The method for producing multimodal polyolefin according to claim 1 , wherein the first reactor and the second reactor includes a slurry phase reactor and a gas phase reactor.
9. The method for producing multimodal polyolefin according to claim 1 , wherein the reactors are more than two reactors.
10. The method for producing multimodal polyolefin according to claim 1 , wherein the monomer is selected from the group consisting of ethylene, propylene and mixture thereof, and optionally further includes α-olefin of 4 to 10 carbon atoms, and the amount of the α-olefin is 0.01 to 10.0 weight % with respect to the total polyolefin of 100 weight %.
11. The method for producing multimodal polyolefin according to claim 1 , wherein in producing the low molecular weight bimodal polymer, one or more comonomer is introduced into the second reactor, and the amount of the comonomer is 0.01 to 30 weight % with respect to the total polyolefin of 100 weight %.
12. The method for producing multimodal polyolefin according to claim 1 , wherein the catalyst composition includes two or more metallocene catalysts for producing polymers of different molecular weights and one or more cocatalyst.
13. The method for producing multimodal polyolefin according to claim 12 , wherein the catalyst composition comprises:
(1) at least one first metallocene compound represented by Chemical formula 1 below;
(2) at least one second metallocene compound represented by Chemical formula 2 below; and
(3) One or more co-catalyst selected from the group of consisting of aluminoxane represented by Chemical formula 3, 4 and 5 below;
(L1)(L2)(X1)(X2)M1 [Chemical formula 1]
In Chemical formula 1, M1 is Titanium(Ti), Zirconium(Zr) or Hafnium(Hf); (L1) and (L2) are independently, a cyclopentadienyl group having hydrocarbyl substituents groups of 3 to 10 carbon atoms containing at least one secondary or tertiary carbon; (X1) and (X2) are independently F, Cl, Br, I or a hydrocarbyl group of 1 to 10 carbon atoms;
(L3-Q-L4)(X1)(X2)M2 [Chemical formula 2]
In Chemical formula 2, M2 is Titanium(Ti), Zirconium(Zr) or Hafnium(Hf); (L3) is fluorenyl group having two or more hydrocarbyl substituent groups of 4 to 10 carbon atoms containing the tertiary carbon; (L4) is a cyclopentadienyl group having at least one hydrocarbyl substituent groups of 4 to 10 carbon atoms; (Q) is a crosslinking functional group represented by Chemical formula Q1R1R2, Q1 is carbon atom(C), silicon atom(Si) or germanium atom(Ge), R1 and R2 are independently hydrogen or a hydrocarbyl group of 1 to 10 carbon atoms; (X1) and (X2) are independently F, Cl, Br, I or a hydrocarbyl group of 1 to 10 carbon atoms;
In Chemical formula 3, 4 and 5, R is hydrocarbyl group, x is an integer of 1 to 70, y is an integer of 3 to 50.
14. The method for producing multimodal polyolefin according to claim 12 , wherein the catalyst composition is supported on an organic or inorganic carrier.
15. The method for producing multimodal polyolefin according to claim 14 , wherein the amount of aluminum component in the catalyst composition is 5 to 30 weight part with respect to 100 weight part of the carrier, and the amount of the transition metal component in the catalyst is 0.01 to 2 weight part with respect to 100 weight part of the carrier.