Patent Application
20190322773
The present invention relates to a transition metal compound for an olefin polymerization catalyst, an olefin polymerization catalyst containing the transition metal compound, and a polyolefin prepared using the olefin polymerization catalyst for polymerization thereof.
A metallocene catalyst, which is a type of catalyst used for polymerizing olefins, is based on a compound in which a ligand such as a cyclopentadienyl group, an indenyl group, a cycloheptadienyl group, or the like is linked to a transition metal compound or a transition metal halide compound through a coordinate covalent bond, and the basic form thereof is a sandwich structure.
The metallocene catalyst is a single-site catalyst containing the above-described metallocene compound and a co-catalyst such as methylaluminoxane or the like. The use of the metallocene catalyst for polymerization results in a polymer having a narrow molecular weight distribution and a uniform comonomer distribution, and the metallocene catalyst exhibits higher copolymerization activity than a Ziegler-Natta catalyst.
However, since there are still many challenges in using the catalyst commercially, it is required to develop a catalyst having high activity and being highly capable of achieving copolymerization even at a high temperature of 100° C. or more and an economically feasible production technique.
One aspect of the present invention is to provide: a transition metal compound for an olefin polymerization catalyst; an olefin polymerization catalyst having high activity and being highly capable of achieving copolymerization even at a high temperature by containing the transition metal compound; and a polyolefin prepared using the olefin polymerization catalyst for polymerization thereof and thus having excellent physical properties such as low density, high molecular weight, and the like.
However, the technical scope of the present invention is not limited to the above-described objectives, and other unmentioned objectives can be clearly understood by those skilled in the art from the following description.
According to an embodiment of the present invention, a transition metal compound for an olefin polymerization catalyst, the transition metal compound represented by the following Chemical Formula 1:
(In Chemical Formula 1, M is titanium (Ti), zirconium (Zr), or hafnium (Hf), Q is silicon (Si), carbon (C), or germanium (Ge), Y is oxygen (O), sulfur (S), nitrogen (N), or phosphorus (P), X1 and X2 are each independently a halogen, a C1-20 alkyl, a C2-20 alkenyl, a C2-20 alkynyl, a C6-20 aryl, a C1-20 alkyl C6-20 aryl, a C6-20 aryl C1-20 alkyl, a C1-20 alkylamido, a C6-20 arylamido, or a C1-20 alkylidene, and R1 to R11 are each independently a hydrogen atom, a substituted or unsubstituted C1-20 alkyl, a substituted or unsubstituted C2-20 alkenyl, a substituted or unsubstituted C6-20 aryl, a substituted or unsubstituted C1-20 alkyl C6-20 aryl, a substituted or unsubstituted C6-20 aryl C1-20 alkyl, a substituted or unsubstituted C1-20 heteroalkyl, a substituted or unsubstituted C3-20 heteroaryl, or a substituted or unsubstituted C1-20 silyl.) A neighboring two among the R5 to R8 may be connected to each other, forming a substituted or unsubstituted C5-20 ring.
The Chemical Formula 1 may be one of the following Chemical Formulas 1-1 to 1-12:
(In each independent Chemical Formula 1-1 to Chemical Formula 1-2, M is Ti, Zr, or Hf, and X1 and X2 are each independently a halogen, a C1-20 alkyl, a C2-20 alkenyl, a C2-20 alkynyl, a C6-20 aryl, a C1-20 alkyl C6-20 aryl, a C6-20 aryl C1-20 alkyl, a C1-20 alkylamido, a C6-20 arylamido, or a C1-20 alkylidene.)
The R2 to R8 may be each a hydrogen atom.
The Chemical Formula 1 may be the following Chemical Formula 2:
According to another embodiment of the present invention, an olefin polymerization catalyst comprising: a transition metal compound represented by the following Chemical Formula 1; and a co-catalyst compound.
(In Chemical Formula 1, M is Ti, Zr, or Hf, Q is Si, C, or Ge, Y is O, S, N, or P, X1 and X2 are each independently a halogen, a C1-20 alkyl, a C2-20 alkenyl, a C2-20 alkynyl, a C6-20 aryl, a C1-20 alkyl C6-20 aryl, a C6-20 aryl C1-20 alkyl, a C1-20 alkylamido, a C6-20 arylamido, or a C1-20 alkylidene, and R1 to R11 are each independently a hydrogen atom, a substituted or unsubstituted C1-20 alkyl, a substituted or unsubstituted C2-20 alkenyl, a substituted or unsubstituted C6-20 aryl, a substituted or unsubstituted C1-20 alkyl C6-20 aryl, a substituted or unsubstituted C6-20 aryl C1-20 alkyl, a substituted or unsubstituted C1-20 heteroalkyl, a substituted or unsubstituted C3-20 heteroaryl, or a substituted or unsubstituted C1-20 silyl.)
The Chemical Formula 1 may be one of the following Chemical Formulas 1-1 to 1-12:
(In each independent Chemical Formula 1-1 to Chemical Formula 1-2, M is Ti, Zr, or Hf, and X1 and X2 are each independently a halogen, a C1-20 alkyl, a C2-20 alkenyl, a C2-20 alkynyl, a C6-20 aryl, a C1-20 alkyl C6-20 aryl, a C6-20 aryl C1-20 alkyl, a C1-20 alkylamido, a C6-20 arylamido, or a C1-20 alkylidene.)
The Chemical Formula 1 may be the following Chemical Formula 2:
The co-catalyst compound may include one or more of a compound represented by the following Chemical Formula A, a compound represented by the following Chemical Formula B, and a compound represented by the following Chemical Formula C:
(In Chemical Formula A, n is an integer of 2 or more, and Ra is a halogen atom, a C1-20 hydrocarbon group, or a C1-20 hydrocarbon group substituted with a halogen.)
(In Chemical Formula B, D is aluminum (Al) or boron (B), and Rb, Rc, and Rd are each independently a halogen atom, a C1-20 hydrocarbon group, a C1-20 hydrocarbon group substituted with a halogen, or a C1-20 alkoxy group.)
[L-H]+[Z(A)4]− or [L]+[Z(A)4]− <Chemical Formula C>
(In Chemical Formula C, L is a neutral or cationic Lewis base, [L-H]+ and [L]+ are a Brønsted acid, Z is a Group 13 element, and A is each independently a substituted or unsubstituted C6-20 aryl group or a substituted or unsubstituted C1-20 alkyl group.)
According to the other embodiment of the present invention, A polyolefin prepared through the polymerization of olefin-based monomers in the presence of the olefin polymerization catalyst.
The olefin-based monomer may include one or more selected from the group consisting of a C2-20 α-olefin, a C1-20 diolefin, a C3-20 cycloolefin, and a C3-20 cyclodiolefin.
The polyolefin may have been prepared through the copolymerization of ethylene and 1-octene.
The polyolefin may have a molecular weight (Mw) of 210,000 or more.
The polyolefin may have a density of 0.900 g/cm3 or less.
Other details of the embodiments of the present invention are included in the detailed description and the accompanying drawings.
According to the embodiments of the present invention, at least the following effects are provided.
The transition metal compound of the present invention can be used for preparing an olefin polymerization catalyst having high activity and being highly capable of achieving copolymerization even at a high temperature, and a polyolefin prepared using the catalyst for polymerization thereof can exhibit excellent physical properties such as low density, high molecular weight, and the like.
In addition, an olefin polymerization catalyst containing the transition metal compound of the present invention is synthesized with high yield and can be easily prepared even by an economical method, and thus is highly practical in a commercial sense.
The effects of the present invention are not limited by the foregoing, and other various effects are included in the present specification.
Advantages and features of the present invention and methods of accomplishing the same may be understood more readily by reference to the following detailed description of preferred embodiments and the accompanying drawings. The present invention may, however, be embodied in many different forms and should not be construed as being limited to the embodiments set forth herein. Rather, these embodiments are provided so that this disclosure will be thorough and complete and will fully convey the scope of the invention to those skilled in the art, and the present invention will only be defined by the appended claims.
As used herein, the term “CA-B” means that “there are between A and B carbon atoms, inclusive,” and the term “A to B” means “between A and B, inclusive.” In addition, in the term “substituted or unsubstituted,” “substituted” means that “at least one hydrogen atom in the hydrocarbon compound or hydrocarbon derivative has been substituted with a halogen, a C1-20 alkyl, a C2-20 alkenyl, a C2-20 alkynyl, a C6-20 aryl, a C1-20 alkyl C6-20 aryl, a C6-20 aryl C1-20 alkyl, a C1-20 alkylamido, a C6-20 arylamido, or a C1-20 alkylidene” and “unsubstituted” means that “not even one hydrogen atom in the hydrocarbon compound or hydrocarbon derivative has been substituted with a halogen, a C1-20 alkyl, a C2-20 alkenyl, a C2-20 alkynyl, a C6-20 aryl, a C1-20 alkyl C6-20 aryl, a C6-20 aryl C1-20 alkyl, a C1-20 alkylamido, a C6-20 arylamido, or a C1-20 alkylidene.”
In one embodiment of the present invention, the transition metal compound for an olefin polymerization catalyst may be represented by the following Chemical Formula 1.
In Chemical Formula 1, M may be titanium (Ti), zirconium (Zr), or hafnium (Hf), Q may be silicon (Si), carbon (C), or germanium (Ge), Y may be a Group 15 element such as nitrogen (N), phosphorus (P), or the like, or when R11 is unsubstituted, a Group 16 element such as oxygen (O), sulfur (S), or the like, X1 and X2 are each independently a halogen, a C1-20 alkyl, a C2-20 alkenyl, a C2-20 alkynyl, a C6-20 aryl, a C1-20 alkyl C6-20 aryl, a C6-20 aryl C1-20 alkyl, a C1-20 alkylamido, a C6-20 arylamido, or a C1-20 alkylidene, and R1 to R11 may be each independently a hydrogen atom, a substituted or unsubstituted C1-20 alkyl, a substituted or unsubstituted C2-20 alkenyl, a substituted or unsubstituted C6-20 aryl, a substituted or unsubstituted C1-20 alkyl C6-20 aryl, a substituted or unsubstituted C6-20 aryl C1-20 alkyl, a substituted or unsubstituted C1-20 heteroalkyl, a substituted or unsubstituted C3-20 heteroaryl, or a substituted or unsubstituted C1-20 silyl.
In addition, a neighboring two among R5 to R8 may be connected to each other, forming a substituted or unsubstituted C5-20 ring.
Specifically, the transition metal compound may be at least one of the compounds represented by the following Chemical Formulas 1-1 to 1-12.
In each independent Chemical Formula 1-1 to Chemical Formula 1-2, M may be Ti, Zr, or Hf, and X1 and X2 may be each independently a halogen, a C1-20 alkyl, a C2-20 alkenyl, a C2-20 alkynyl, a C6-20 aryl, a C1-20 alkyl C6-20 aryl, a C6-20 aryl C1-20 alkyl, a C1-20 alkylamido, a C6-20 arylamido, or a C1-20 alkylidene.
Meanwhile in Chemical Formula 1, R2 to R8 may be each a hydrogen atom. In one exemplary embodiment, the transition metal compound may be represented by the following Chemical Formula 2, but the present invention is not limited thereto.
In one embodiment of the present invention, the olefin polymerization catalyst may contain: one or more of the above-exemplified transition metal compounds; and a co-catalyst compound.
The co-catalyst compound may include one or more of the compound represented by the following Chemical Formula A, the compound represented by the following Chemical Formula B, and the compound represented by the following Chemical Formula C.
In Chemical Formula A, n may be an integer of 2 or more, Ra may be a halogen atom, a C1-20 hydrocarbon group, or a C1-20 hydrocarbon group substituted with a halogen. Specifically, Ra may be methyl, ethyl, n-butyl, or isobutyl, but the present invention is not limited thereto.
In Chemical Formula B, D may be aluminum (Al) or boron (B), and Rb, Rc, and Rd may be each independently a halogen atom, a C1-20 hydrocarbon group, a C1-20 hydrocarbon group substituted with a halogen, or a C1-20 alkoxy group. Specifically, when D is Al, Rb, Rc, and Rd may be each independently methyl or isobutyl, and when D is B, Rb, Rc, and Rd may be each pentafluorophenyl, but the present invention is not limited thereto.
[L-H]+[Z(A)4]− or [L]+[Z(A)4]− <Chemical Formula C>
In Chemical Formula C, L may be a neutral or cationic Lewis base, [L-H]+ or [L]+ may be a Brønsted acid, Z may be a Group 13 element, and A may be each independently a substituted or unsubstituted C6-20 aryl group or a substituted or unsubstituted C1-20 alkyl group. Specifically, [L-H]+ may be a dimethylanilinium cation, [Z(A)4]− may be [B(C6F5)4]−, and [L]+ may be [(C6H5)3C]+, but the present invention is not limited thereto.
The olefin polymerization catalyst may further contain a carrier.
There is no particular limitation on the carrier as long as it can support a transition metal compound for an olefin polymerization catalyst and a co-catalyst compound. In one exemplary embodiment, the carrier may be carbon, silica, alumina, zeolite, magnesium chloride, or the like.
As a method of supporting a transition metal compound for an olefin polymerization catalyst and a co-catalyst compound on the carrier, a physical adsorption method or a chemical adsorption method may be used.
In one exemplary embodiment, the physical adsorption method may be a method in which a carrier is brought into contact with a solution containing a transition metal compound for an olefin polymerization catalyst dissolved therein and then dried, a method in which a carrier is brought into contact with a solution containing both a transition metal compound for an olefin polymerization catalyst and a co-catalyst compound dissolved therein and then dried, or a method in which a carrier supporting a transition metal compound for an olefin polymerization catalyst and a carrier supporting a co-catalyst compound are prepared separately, respectively by bringing a carrier into contact with a solution containing the transition metal compound for an olefin polymerization catalyst dissolved therein and then drying the same and by bringing a carrier into contact with a solution containing the co-catalyst compound dissolved therein and then drying the same, and are subsequently mixed together.
In one exemplary embodiment, the chemical adsorption method may be a method in which a co-catalyst compound is first supported on the surface of a carrier and then a transition metal compound for an olefin polymerization catalyst is supported on the co-catalyst compound, or a method in which a functional group on the surface of a carrier (e.g., in the case of silica, a hydroxyl group (—OH) on the silica surface) is linked to a catalyst compound through a covalent bond.
The total amount of supported main catalyst compound, including the transition metal compound, may be 0.001 mmol to 1 mmol based on 1 g of the carrier, and the amount of supported co-catalyst compound may be 2 mmol to 15 mmol based on 1 g of the carrier.
However, the use of such a carrier is not essential, and the decision as to whether or not a carrier should be used may be appropriately made depending on necessity.
Meanwhile, a polyolefin may be prepared by polymerizing olefin-based monomers in the presence of the above-described olefin polymerization catalyst of the present invention.
The polyolefin may be, for example, a homopolymer or copolymer obtained by a polymerization reaction such as free-radical polymerization, cationic polymerization, coordination polymerization, condensation polymerization, addition polymerization, or the like, but the present invention is not limited thereto.
In one exemplary embodiment, the polyolefin may be produced by gas-phase polymerization, solution polymerization, slurry polymerization, or the like. Examples of the solvent that may be used for preparing the polyolefin by solution polymerization or slurry polymerization may include: C5-12 aliphatic hydrocarbon solvents such as pentane, hexane, heptane, nonane, decane, and isomers thereof; aromatic hydrocarbon solvents such as toluene and benzene; hydrocarbon solvents substituted with chlorine atoms, such as dichloromethane and chlorobenzene; mixtures thereof; and the like, but the present invention is not limited thereto.
The olefin-based monomer may be one or more selected from the group consisting of a C2-20 α-olefin, a C1-20 diolefin, a C3-20 cycloolefin, and a C3-20 cyclodiolefin.
In one exemplary embodiment, the olefin-based monomer may be ethylene, propylene, 1-butene, 1-pentene, 4-methyl-1-pentene, 1-hexene, 1-heptene, 1-octene, 1-decene, 1-undecene, 1-dodecene, 1-tetradecene, 1-hexadecene, or the like, and the polyolefin may be a homopolymer containing only one type of the above-exemplified olefin-based monomer or a copolymer containing two or more types of the above-exemplified olefin-based monomer.
Preferably, the polyolefin is a copolymer of ethylene and 1-octene, but the present invention is not limited thereto.
The polyolefin obtained by polymerization in the presence of the olefin polymerization catalyst of the present invention may have a molecular weight (Mw) of 210,000 or more, and may specifically have a molecular weight (Mw) of 219,000 or more when the density is 0.900 g/cm3 or less. In addition, the polyolefin may have a density of 0.900 g/cm3 or less and a catalyst activity of 80 kg/mmol·h or more.
In regard to the obtained polyolefin, the molecular weight (Mw) of 210,000 or more is favorable in terms of the tensile strength of the polyolefin, the density of 0.900 g/cm3 or less is favorable in terms of the elastic modulus and transparency of the polyolefin, and the catalyst activity of 80 kg/mmol·h or more is favorable in terms of the reduction of polyolefin production costs because it leads to excellent polymerization reactivity with respect to the amount of catalyst used.
Hereinafter, details of preparation examples regarding, among the transition metal compounds for an olefin polymerization catalyst of the present invention, the above-described compound represented by Chemical Formula 2, and details of an experimental example for evaluating the physical properties of the polyolefins obtained by polymerization in the presence of an olefin polymerization catalyst containing the above-described transition metal compound will be described.
Methacryloyl chloride (2.8 g, 27 mmol) and a solution prepared by diluting dibenzothiophene (5.0 g, 27 mmol) in dichloromethane (50 mL) were added, at −78° C., to a solution prepared by dispersing AlCl3 (7.2 g, 54 mmol) in dichloromethane (150 mL). After completion of the addition, the mixture was stirred at room temperature for 12 hours, and then water was added at 0° C. to terminate the reaction. Afterward, the organic layer was extracted, the solvent was removed in vacuo, the resultant was subjected to column chromatography, and thereby 4.2 g (61%) of 1,2-dihydro-2-methyl-3H-benzo[b]indeno[4,5-d]thiophen-3-one having the following 1H-NMR spectrum was obtained.
1H-NMR (CDCl3, 300 MHz): 8.25 (m, 1H), 7.92 (m, 1H), 7.83 (m, 2H), 7.53 (m, 2H), 3.93 (m, 1H), 3.21 (m, 1H), 2.88 (m, 1H), 1.43 (d, 3H).
Sodium borohydride (NaBH4) (624 mg, 17 mmol) was added, at 0° C., to a solution prepared by dissolving the 1,2-dihydro-2-methyl-3H-benzo[b]indeno[4,5-d]thiophen-3-one (4.2 g, 17 mmol) obtained in Preparation Example 1-1 in a 1:9 (v/v) solvent mixture (50 mL) of THF and methanol. The temperature was gradually raised to room temperature, and thereafter the mixture was stirred for one hour. After completion of the reaction, all the solvent was removed in vacuo, and the organic layer was extracted with dichloromethane. Afterward, moisture was removed from the organic layer using magnesium sulfate, the solvent was subsequently removed in vacuo, and thereby 3.4 g (81%, diastereomeric alcohols) of 2,3-dihydro-2-methyl-1H-benzo[b]indeno[4,5-d]thiophen-3-ol having the following 1H-NMR spectrum was obtained.
1H-NMR (CDCl3, 300 MHz): 8.19 (m, 1H), 7.87 (m, 1H), 7.76 (d, 1H), 7.44-7.56(m, 3H), 4.91 and 5.17 (2s, 1H), 3.60 and 3.79 (2m, 1H), 2.96 and 3.17 (2m, 1H), 2.49 and 2.75 (2m, 1H), 1.86 and 1.66 (2s, 1H), 1.35 and 1.30 (2d, 3H).
The 2,3-dihydro-2-methyl-1H-benzo[b]indeno[4,5-d]thiophen-3-ol (3.4 g, 13 mmol) obtained in Preparation Example 1-2 and p-toluenesulfonic acid (13 mg, 0.5 mol %) were added to toluene (30 mL), and the mixture was stirred for one hour while refluxing at 110° C. After completion of the reaction, the resultant was subjected to column chromatography, and thereby 2.2 g (69%) of 2-methyl-1H-benzo[b]indeno[4,5-d]thiophene having the following 1H-NMR spectrum was obtained.
1H-NMR (CDCl3, 300 MHz): 8.18 (m, 1H), 7.88 (m, 1H), 7.73 (d, 1H), 7.40-7.52 (m, 3H), 6.64 (s, 1H), 3.76 (s, 2H), 2.28 (s, 3H).
n-Butyllithium (4.3 g, 10 mmol, 1.6 M in hexane) was added slowly, at −78° C., to a solution prepared by diluting the 2-methyl-1H-benzo[b]indeno[4,5-d]thiophene (2.2 g, 9.3 mmol) obtained in Preparation Example 1-3 in diethyl ether (50 mL). The temperature was gradually raised to room temperature, and thereafter the mixture was stirred for 12 hours. After stirring, the resulting solid was isolated through filtration and then dried in vacuo, and thereby 2.2 g (99%) of a lithium salt compound was obtained.
A dispersion of the above-described lithium salt compound (2.2 g, 9.1 mmol) in diethyl ether (30 mL) was added slowly, at −78° C., to a solution prepared by diluting dichlorodimethylsilane (Me2SiCl2) (3.5 g, 27 mmol) in diethyl ether (70 mL). The temperature was gradually raised to room temperature, and thereafter the mixture was stirred for 12 hours. After completion of the reaction, the solvent was removed in vacuo, and the resultant was subjected to extraction with hexane and subsequent filtration. After removal of the solvent in vacuo, 2.8 g (95%) of (2-methyl-1H-benzo[b]indeno[4,5-d]thiophen-1-yl)chlorodimethylsilane was obtained.
1H-NMR (CDCl3, 300 MHz): 8.40 (d, 1H), 7.88 (d, 1H), 7.60 (m, 2H), 7.42-7.52 (m, 3H), 3.75 (s, 1H), 2.44 (s, 3H), 0.41 (s, 3H), 0.16 (s, 3H).
A solution prepared by diluting the (2-methyl-1H-benzo[b]indeno[4,5-d]thiophen-1-yl)chlorodimethylsilane (2.8 g, 8.5 mmol) obtained in Preparation Example 1-4 in THF (30 mL) was added slowly, at −78° C., to a solution prepared by diluting t-butylamine (t-BuNH2) (2.5 g, 34 mmol) in THF (30 mL). The temperature was gradually raised to room temperature, and thereafter the mixture was stirred for 12 hours. After completion of the reaction, all the solvent was removed in vacuo, and the resultant was subjected to extraction with hexane and subsequent filtration. After removal of the hexane in vacuo, 3.1 g (99%) of N-tert-butyl-1,1-dimethyl-1-(2-methyl-1H-benzo[b]indeno[4,5-d]thiophen-1-yl)silanamine, which is the compound represented by the following Chemical Formula 3, was obtained.
1H-NMR (CDCl3, 300 MHz): 8.40 (d, 1H), 7.86 (d, 1H), 7.55(m, 2H), 7.39-7.48 (m, 3H), 3.57 (s, 1H), 2.42 (s, 3H), 1.21 (s, 9H), 0.12 (s, 3H), −0.09 (s, 3H).
Methyllithium (15.9 g, 35 mmol, a 1.6 M solution in diethyl ether) was added, at −30° C., to a solution prepared by dissolving the N-tert-butyl-1,1-dimethyl-1-(2-methyl-1H-benzo[b]indeno[4,5-d]thiophen-1-yl)silanamine (3.1 g, 8.5 mmol) obtained in Preparation Example 1-5 in diethyl ether (30 ml). The temperature was gradually raised to room temperature, and thereafter the mixture was stirred for two hours. Afterward, TiCl4 (1.62 g, 8.5 mmol) diluted in pentane (10 ml) was added slowly at −30° C., and the mixture was stirred for two hours. After completion of the reaction, all the solvent was removed in vacuo, and the resultant was subjected to extraction with hexane and subsequent filtration. After removal of the hexane in vacuo, 786 mg (21%) of dimethylsilyl(t-butylamido)(2-methyl-1H-benzo[b]indeno[4,5-d]thiophen-1-yl)dimethyl titanium, which is the compound of Chemical Formula 2, was obtained.
1H-NMR (Benzene-d6, 300 MHz): 8.42 (d, 1H), 7.64 (m, 2H), 7.54 (d, 1H), 7.36 (m, 2H), 7.21 (s, 1H), 2.12 (s, 3H), 1.45 (s, 9H), 0.87 (s, 3H), 0.60 (s, 3H), 0.53 (s, 3H), −0.36 (s, 3H).
Ethylene and 1-octene were copolymerized as follows, using an olefin polymerization catalyst containing the above-described compound of Chemical Formula 2.
First, a hexane solvent (1 L) and 1-octene (45 g) were added to a 2-L autoclave reactor, and then the reactor was preheated to a temperature of 70° C. Next, the transition metal compound (4×10−6 M) of Chemical Formula 2 obtained in Preparation Example 1 and having been treated with a triisobutylaluminum compound was added to a catalyst storage tank and was subsequently introduced into the reactor by applying high-pressure argon thereto. A 2.4×10−5 M dimethylanilinium tetrakis(pentafluorophenyl)borate co-catalyst was introduced into the reactor by applying high-pressure argon thereto.
Ethylene gas was injected while controlling the ethylene pressure so that the overall pressure in the reactor was maintained at 30 bar, and afterward the polymerization reaction was carried out for five minutes. During the polymerization reaction, the polymerization temperature was maintained as constant as possible at 90° C. by removing the heat of reaction using a cooling coil inside the reactor.
After the polymerization reaction, the remaining gas was discharged, and the polymer solution was discharged through the lower part of the reactor and then cooled by adding an excessive amount of ethanol thereto to induce precipitation. The obtained polymer was washed two to three times with each of ethanol and acetone and then dried in a 80° C. vacuum oven for at least 12 hours, and thereby an ethylene/1-octene copolymer was obtained.
An ethylene/1-octene copolymer was obtained in the same manner as in Preparation Example 2, except that 67 g of 1-octene was used.
An ethylene/1-octene copolymer was obtained in the same manner as in Preparation Example 2, except that dimethylsilylene(t-butylamido)(indenyl)titanium dimethyl represented by the following Chemical Formula 4 was used as the transition metal compound.
The physical properties of the ethylene/1-octene copolymers prepared according to Preparation Examples 2 and 3 and the Comparative Example were measured, and the results are shown in Table 1 below.
As shown in Table 1, it can be seen that, when used for preparing an olefin polymer, an olefin polymerization catalyst containing a compound of the present invention is more capable of producing an olefin polymer having a high molecular weight and a low density with high activity than the olefin polymerization catalyst of the Comparative Example.
While the embodiments within the scope of the inventive concept have been described in detail with reference to the above-exemplified chemical structural formulas, preparation examples, and the like, it should be understood that the inventive concept is not limited by, but can be variously modified based on, the exemplified chemical structural formulas, preparation examples, and the like. The exemplified chemical structural formulas, preparation examples, and the like have been provided to fully convey the scope of the inventive concept to those skilled in the art, and the scope of the inventive concept will only be defined by the scope of the claims. Therefore, it is to be understood that the above-described embodiments are illustrative in all aspects and are not restrictive.
| Number | Date | Country | Kind |
|---|---|---|---|
| 10-2016-0164939 | Dec 2016 | KR | national |
| Filing Document | Filing Date | Country | Kind |
|---|---|---|---|
| PCT/KR2017/014259 | 12/6/2017 | WO | 00 |
