Patent Application
20230331753
The present invention relates to a ligand compound, an organochromium compound, and a catalyst system comprising the same.
A linear alpha-olefin like 1-hexene and 1-octene is used as a detergent, a lubricant, a plasticizer, or the like, and particularly, used as a comonomer for adjusting the density of a polymer during preparing a linear low-density polyethylene.
In the preparation process of the conventional linear low-density polyethylene (LLDPE), in order to adjust the density by forming a branch on a polymer backbone, copolymerization with a comonomer like an alpha-olefin such as 1-hexene and 1-octene together with ethylene has been performed.
Accordingly, in order to prepare the LLDPE with the high comonomer content, there were defects of the cost of the comonomer accounted for a big part of the manufacturing cost, and to solve such defects, various attempts have been conducted.
Particularly, the LLDPE is mainly produced through a shell higher olefin process. However, according to the method, alpha-olefins with various lengths are synthesized simultaneously according to Schultz-Flory distribution, and a separate separation process is inconveniently required for obtaining a specific alpha-olefin.
To solve such defects, a method of selectively synthesizing 1-hexene through the trimerization reaction of ethylene, or selectively synthesizing 1-octene through the tetramerization reaction of ethylene has been suggested. In addition, more studies on a catalyst system capable of selectively oligomerizing ethylene have been conducted.
An object of the present invention is to provide an organochromium compound of a novel structure, which shows high catalyst activity and selectivity and may produce a linear alpha-olefin with excellent efficiency, and a catalyst system including the same.
In order to solve the above-described task, the present invention provides a ligand compound represented by Formula 1 below.
In Formula 1,
In addition, the present invention provides an organochromium compound including the ligand compound represented by Formula 1; and chromium (Cr) coordinated with the ligand compound.
In addition, the present invention provides a catalyst system including the ligand compound or the organochromium compound.
In addition, the present invention provides a method of preparing a linear alpha-olefin, including oligomerizing ethylene in the presence of the catalyst system.
The organochromium compound and the catalyst system using the same according to the present invention have excellent catalyst activity and shows high selectivity to an alpha-olefin such as 1-hexene and 1-octene, and accordingly, may be usefully used as catalysts for polymerization for preparing a linear alpha-olefin.
Hereinafter, the present invention will be explained in more detail to assist the understanding of the present invention.
It will be understood that words or terms used in the description and claims shall not be interpreted as the meaning defined in commonly used dictionaries. It will be further understood that the words or terms should be interpreted as having a meaning that is consistent with their meaning of the technical idea of the invention, based on the principle that an inventor may properly define the meaning of the words or terms to best explain the invention.
In the present invention, “oligomerization” means oligomerizing olefins. According to the number of olefins polymerized, the oligomerization is referred to as trimerization or tetramerization, and is collectively referred to as multimerization. Particularly, in the present disclosure, the oligomerization may mean selective preparation of 1-hexene and 1-octene, which are main comonomers of a LLDPE from ethylene.
In the present invention, a “catalyst system” means a state obtainable as a catalyst composition having activity by adding three components including a chromium source, a ligand compound and a cocatalyst, or two components of a transition metal compound and a cocatalyst in an arbitrary order. The three components or two components of the catalyst system may be added in the presence or absence of a solvent and a monomer, and may be used in a supported or unsupported state.
In the case of applying the ligand compound of the present invention to a catalyst system for polymerizing a linear alpha-olefin, excellent catalyst activity may be shown, and selectivity to linear alpha-olefin may be high, and when compared to the conventional PNP-based catalyst, the production amount of a solid polyethylene is small even under the same reaction conditions, and a linear alpha-olefin could be prepared more efficiently.
Particularly, the aniline-based PNP-based organochromium compound of the present invention is mainly utilized for the preparation of a linear alpha-olefin using ethylene, and oligomerization reaction is mainly performed by the reaction under ethylene conditions, to show high selectivity with respect to an alpha-olefin of a liquid type, particularly, 1-hexene or 1-octene of a liquid type. This is because selectivity to an alpha-olefin with a specific length increases through a transition state forming metallacycle in the oligomerization reaction of ethylene.
The ligand compound of the present invention includes a diphosphino aminyl moiety, and aryl having a specific substituent is connected with the terminal of the diphosphino aminyl moiety, and accordingly, the ligand compound may have a type which may play the role of a strong electron donating group.
Due to such structural features, the ligand compound may be applied to a catalyst system for oligomerizing ethylene to show high activity, particularly, high selectivity to 1-hexene, 1-octene, or the like. This is considered due to the interaction between adjacent chromium active points. Particularly, in the case where aryl substituted with a specific substituent is connected with the phosphor (P) atom of diphosphino aminyl, electron density may increase at the phosphor (P) atom and nitrogen (N) atom included in the diphosphino aminyl, and the electrical and three-dimensional properties of the whole ligand compound may change.
Accordingly, there may be changes of the bond between the ligand and the chromium atom, the structure of the catalyst may be stabilized even further, an alpha-olefin may be formed with higher activity and selectivity by changing the energy of a transition state (activation energy) when compared to the conventional metallacycloheptane or metallacyclononane type, and the amount of by-products such as a solid alpha-olefin having a large molecular weight like PE wax, may be reduced even further.
Particularly, the ligand compound of the present invention is characterized in that aryl positioned at the terminal of a diphosphino aminyl residue has a bulky substituent. The bulky substituent prevents the generation of an inactive species by the combination of two molecules of the ligand compound with the chromium atom, and reduces the rotatability of a nitrogen-phosphor bond to prevent the dissociation of the ligand compound in the catalyst, thereby producing a chromium catalyst having high stability and excellent activity and selectivity.
The bulky substituent is bonded at the para position of the aryl. If the substituent is bonded at a meta position or at both positions of meta and para, the steric hindrance of the catalyst may become too excessive, the approach of ethylene may become difficult, and the catalyst activity may be rather deteriorated. Since the ligand compound of the present invention is bonded at the para position, a suitable degree of steric hindrance may be induced, and ethylene may be oligomerized with high activity, while securing catalyst stability.
In addition, to the nitrogen atom bonded to two phosphor atoms, a bulky functional group such as cycloalkyl is bonded, and the bulky substituent bonded to the nitrogen may prevent the rotation of a nitrogen-phosphor bond to maximize the improvement of the catalyst stability and activity.
The ligand compound of the present invention is characterized in being represented by Formula 1 below.
In Formula 1,
In the present invention, “cycloalkyl” refers to a nonaromatic cyclic hydrocarbon radical composed of carbon atoms. Non-limiting examples of the cycloalkyl include cyclopropyl, cyclobutyl, cyclopentyl, cyclohexyl and cycloheptyl, without limitation. In the present disclosure, the cycloalkyl includes nonaromatic cyclic hydrocarbon such as bicyclic and tricyclic alkyls, in which two or more nonaromatic cyclic hydrocarbons are fused.
In the present invention, “alkyl” means a hydrocarbon residue of a linear chain, a cyclic or a branched type and includes methyl, ethyl, n-propyl, isopropyl, n-butyl, isobutyl, t-butyl, n-pentyl, isopentyl and hexyl, without limitation.
In the present invention, “alkoxyalkyl” means a substituent in which one or more hydrogen of alkyl are substituted with alkoxy. Particularly, methoxymethyl, ethoxymethyl, methoxyethyl, ethoxyethyl, butoxymethyl, butoxyethyl, butoxypropyl, butoxybutyl, butoxyheptyl, butoxyhexyl, or the like may be included, without limitation.
In the present invention, “arylalkoxyalkyl” means a substituent in which one or more hydrogen of alkyl are substituted with arylakoxy.
In the present invention, “trialkylsilyl” means a substituent represented by —SiR3 where each R is independently alkyl, and the carbon number of the trialkylsilyl may mean the sum of all the carbon number of R.
In the present invention, “aryl” refers to an optionally substituted benzene ring, or refers to a ring system which may be formed by fusing one or more optional substituents, unless otherwise referred to. Examples of the optional substituent include optionally substituted C1-3 alkyl, optionally substituted C2-3 alkenyl, optionally substituted C2-3 alkynyl, heteroaryl, heterocyclic, aryl, alkoxy optionally having 1 to 3 fluorine substituents, aryloxy, aralkoxy, acyl, aroyl, heteroaroyl, acyloxy, aroyloxy, heteroaroyloxy, sulfanyl, sulfinyl, sulfonyl, aminosulfonyl, sulfonylamino, carboxyamide, aminocarbonyl, carboxy, oxo, hydroxyl, mercapto, amino, nitro, cyano, halogen or ureido. Such a ring or ring system may be optionally fused with an aryl ring (for example, benzene ring), carbocyclic ring or heterocyclic ring, having optionally one or more substituents. Non-limiting examples include phenyl, naphthyl, tetrahydronaphthyl, biphenyl, indanyl, anthracyl, phenanthryl and substituted derivatives thereof, without limitation.
Cy is cycloalkyl of 5 to 10 carbon atoms, or cycloalkyl of 5 to 10 carbon atoms, fused with aryl of 6 to 10 carbon atoms.
Here, each aryl fused with the cycloalkyl may be unsubstituted or substituted with alkyl of 1 to 8 carbon atoms, particularly, unsubstituted or substituted with alkyl of 1 to 6 carbon atoms, alkyl of 1 to 3 carbon atoms, or methyl.
Particularly, the cycloalkyl of 5 to 10 carbon atoms may be, for example, cyclopentyl, cyclohexyl, cycloheptyl, or cyclooctyl, and the cycloalkyl of 5 to 10 carbon atoms, fused with aryl of 6 to 10 carbon atoms may be fused with one or two aryl of 6 to 10 carbon atoms. For example, phenyl-fused cyclopentyl(dihydroindenyl), phenyl-fused cyclohexyl(tetrahydronaphthyl), phenyl-fused cycloheptyl(6,7,8,9-tetrahydrobenzo[7]annulenyl), phenyl-fused cyclooctyl(5,6,7,8,9,10-hexahydrobenzo[8]annulenyl), or two phenyl-fused cyclopentyl(9H-fluorenyl), may be included.
R1 to R4 may be each independently aryl of 6 to 20 carbon atoms, aryl of 6 to 10 carbon atoms, for example, phenyl or naphthyl, preferably, phenyl.
The substituent of R1 to R4 may be cycloalkyl of 5 to 20 carbon atoms, cycloalkyl of 6 to 10 carbon atoms, for example, cyclohexyl, cycloheptyl, cyclooctyl, cyclononyl, 1-adamantyl, 2-adamantyl, or the like; alkyl of 6 to 20 carbon atoms, alkyl of 8 to 15 carbon atoms, for example, octyl, nonan-5-yl, 5-methylnonan-5-yl, 5-ethylnonan-5-yl, 5-propylnonan-5-yl, 5-butylnonan-5-yl, or the like; alkoxyalkyl of 6 to 20 carbon atoms, alkoxyalkyl of 9 to 15 carbon atoms, for example, 5-methoxynonan-5-yl, 5-ethoxynonan-5-yl, 5-propoxynonan-5-yl, 5-butoxynonan-5-yl, or the like; arylalkoxyalkyl of 10 to 30 carbon atoms, arylalkoxyalkyl of 14 to 20 carbon atoms, for example, 5-phenylmethoxynonan-5-yl, 5-(2-phenylethoxy)nonan-5-yl, 5-(3-phenylpropoxy)nonan-5-yl, or the like; trialkylsilyl of 3 to 30 carbon atoms, trialkylsilyl of 3 to 15 carbon atoms, trialkylsilyl of 4 to 12 carbon atoms, or trialkylsilyl of 4 to 9 carbon atoms, for example, tributylsilyl, tripropylsilyl, or the like. The carbon number of the trialkylsilyl represents the total carbon number of the trialkylsilyl.
R1 to R4 may be the same or different.
The Cy may be any one selected from the group below, but is not limited thereto.
In addition, R1 to R4 may be each independently selected from the group below, but is not limited thereto.
The ligand compound according to the present invention may be accomplished by various combinations in a range satisfying the above-described conditions, in addition to the aforementioned particular embodiments, and all compounds may be applicable as the ligand compound of the present invention as long as they are represented by Formula 1.
In addition, the present invention provides an organochromium compound including the ligand compound represented by Formula 1; and chromium (Cr) coordinated with the ligand compound.
The organochromium compound is the chromium complex compound of the ligand compound and may have a type where the chromium of a chromium source makes coordination bonds with one or more unshared electron pairs of N and two P in the ligand compound represented by Formula 1. That is, in the structure, the phosphor atom or nitrogen atom of a diphosphino aminyl residue provides the chromium atom with an unshared electron pair, and particularly, a bidentated state in which two unshared electron pairs are shared, may be preferable. Such an organochromium compound may be applied to a catalyst system for the polymerization reaction of ethylene to show excellent catalyst activity and high selectivity to 1-hexene and 1-octene.
In addition, the present invention provides a catalyst system including chromium, the ligand compound represented by Formula 1 and a cocatalyst.
The ligand compound represented by Formula 1 may be coordinated with chromium to form an organochromium compound. That is, the catalyst system may be a three-component-based catalyst system including chromium, the ligand compound represented by Formula 1 and a cocatalyst, or a two-component-based catalyst system including the organochromium compound and a cocatalyst.
In the catalyst system, the chromium is derived from a chromium source, and the chromium source is an organic or inorganic chromium compound with an oxidation state of 0 to 6. The chromium source may be, for example, a chromium metal, or a compound in which an arbitrary organic or inorganic radical is bonded to chromium. Here, the organic radical may be alkyl, alkoxy, ester, ketone, amido, carboxylate radical, or the like having 1 to 20 carbon atoms, and the inorganic radical may be halide, sulfate, oxide, or the like.
The chromium source is a compound showing high activity for the oligomerization of an olefin and advantageously used and obtained, and may be one or more compounds selected from the group consisting of chromium(III) acetylacetonate, chromium(III) chloride tetrahydrofuran, chromium(III) 2-ethylhexanoate, chromium(III) acetate, chromium(III) butyrate, chromium(III) pentanoate, chromium(III) laurate, chromium(III) tris(2,2,6,6-tetramethyl-3,5-heptanedionate) and chromium(III) stearate.
In addition, preferably, the cocatalyst is an organometallic compound including a metal in group 13, and any one generally used for polymerizing an olefin in the presence of a transition metal compound may be applied, without specific limitation.
For example, the cocatalyst may be one or more compounds selected from the group consisting of Formulae 2 to 5 below.
—[Al(Ra)—O]a— [Formula 2]
In Formula 2, each Ra is independently a halogen radical, a hydrocarbyl radical of 1 to 20 carbon atoms, or a halogen-substituted hydrocarbyl radical of 1 to 20 carbon atoms, and
D(Rb)3 [Formula 3]
In Formula 3,
[L-H]+[Z(A)4]−or [L]+[Z(A)4]− [Formula 4]
In Formula 4,
[(Rc)nL′-H]+[B(Rd)4]− [Formula 5]
In Formula 5,
The [(Rc)nL′-H]+ is a cation, particularly, a Brønsted acid.
If L′ is N or P, the [(Rc)nL′-H]+ may be represented by [Rc1Rc2Rc3L1′-H]+, and if L′ is S, the [(Rc)nL′-H]+ may be represented by [(Rc1Rc2L2′)2-H]+.
Each Rc may be independently an aliphatic hydrocarbyl or aliphatic heterohydrocarbyl group, preferably, saturated aliphatic hydrocarbyl or saturated aliphatic heterohydrocarbyl, more preferably, substituted hydrocarbyl or substituted heterohydrocarbyl of which substituent is a nonpolar group, and the substituent of the nonpolar group may include, for example, butyl, pentyl, hexyl, sec-hexyl, cyclohexyl, 2-methylcyclohexyl, 2-ethylcyclohexyl, 2-isopropylcyclohexyl, cyclohexenyl, hexenyl, hexynyl, octyl, cyclo-octyl, cyclo-octenyl, 2-ethylhexyl, iso-octyl, decyl, benzyl, phenyl, tolyl, xylyl, o-methylphenyl, o-ethylphenyl, o-isopropylphenyl, o-t-butylphenyl, cumyl, mesityl, biphenyl, naphthyl, anthracenyl, or the like. In addition, Rc may include, for example, methyl, ethyl, ethylenyl, propyl, propenyl, propynyl, butyl, pentyl, hexyl, cyclohexyl, 2-methylcyclohexyl, 2-ethylcyclohexyl, octyl, 2-ethylhexyl, iso-octyl, decyl, dodecyl, tetradecyl, octadecyl, 2-isopropylcyclohexyl, benzyl, phenyl, tolyl, xylyl, o-methylphenyl, o-ethylphenyl, o-isopropylphenyl, o-t-butylphenyl, biphenyl, naphthyl, or the like.
In Formula 5, one or more Rc may include 6 to 40 carbon atoms and total 13 to 100 carbon atoms, and particularly, one Rc may include 6 to 40 carbon atoms and total 21 to 90 carbon atoms.
In Formula 5, Rd may be a halo-substituted aromatic residue having at least one halide substituent at an aromatic ring. The halo-substituted aromatic residue may particularly be pentafluorophenyl.
As a method for preparing the catalyst system, firstly, there is provided a preparation method including contacting the organochromium compound with the compound represented by Formula 2 or Formula 3 to prepare a mixture; and adding a compound represented by Formula 4 or 5 to the mixture. Secondly, there is provided a method for preparing a catalyst system by contacting the organochromium compound with the compound represented by Formula 4 or 5. Third, there is provided a preparation method including contacting the organochromium compound with the compound represented by Formula 4 or Formula 5 to prepare a mixture; and adding a compound represented by Formula 2 or 3 to the mixture.
Among the preparation methods of the catalyst system, in the case of the first method or third method, the molar ratio of the compound represented by Formula 2 or Formula 3 with respect to the organochromium compound may be 1:2 to 1:5,000, particularly, 1:100 to 1:3,000, more particularly, 1:300 to 1:1,500, each.
If the molar ratio of the compound represented by Formula 2 or Formula 3 with respect to the organochromium compound is less than 1:2, there may be defects of incompletely performing the alkylation of the organochromium compound, and if the molar ratio is greater than 1:5,000, the alkylation of the organochromium compound may be performed, but there are defects of incompletely performing the activation of the alkylated organochromium compound due to side reactions among the remaining excessive amount of the alkylating agent. In addition, if the molar ratio of the compound represented by Formula 4 or 5 with respect to the organochromium compound is less than 1:1, there are defects of incompletely performing the alkylation of the organochromium compound to deteriorate the activity of the catalyst system, and if the molar ratio is greater than 1:25, the alkylation of the metal compound may be completely performed, but due to the excessive amount of the activating agent remained, there are defects in that the unit cost of the catalyst system may not be economic, or the purity of a polymer produced may be degraded.
In the second method among the preparation methods of the catalyst system, the molar ratio of the compound represented by Formula 4 or 5 with respect to the organochromium compound may be 1:1 to 1:500, particularly, 1:1 to 1:50, more particularly, 1:1 to 1:25. If the molar ratio is less than 1:1, the amount of the activating agent is relatively small, and the activation of the metal compound may be incompletely performed, and there are defects of degrading the activity of the catalyst system. If the molar ratio is greater than 1;500, the activation of the metal compound may be completely performed, but there are defects in that the unit cost of the catalyst system may not be economic, or the purity of a polymer produced may be degraded due to the remaining excessive amount of the activating agent.
As the reaction solvent in preparing the composition, a hydrocarbon-based solvent such as pentane, hexane and heptane, or an aromatic solvent such as benzene and toluene may be used, but is not limited thereto, and all solvents used in this technical field may be used.
In addition, the organochromium compound and the cocatalyst may be used in supported types. As the support, silica or alumina may be used.
The compound represented by Formula 2 is not specifically limited as long as it is alkylaluminoxane. Particular examples may include methylaluminoxane, ethylaluminoxane, isobutylaluminoxane, butylaluminoxane, or the like, more particularly, methylaluminoxane.
The compound represented by Formula 3 is not specifically limited, and particular examples thereof may include trialkyl aluminum, dialkyl aluminum halide, alkyl aluminum dihalide, dialkyl aluminum hydride, alkyl aluminum dihydride, trialkylboron, or the like.
For example, trialkyl aluminum such as trimethylaluminum, triethylaluminum, triisobutylaluminum, tripropylaluminum, tributylaluminum, triisopropylaluminum, tri-s-butylaluminum, tricyclopentylaluminum, tripentylaluminum, triisopentylaluminum, trihexylaluminum, trioctylaluminum, ethyldimethylaluminum, methyldiethylaluminum, triphenylaluminum, and tri-p-tolylaluminum; dialkylaluminum halide such as diethylaluminum chloride; dialkyl aluminum hydride such as diethyl aluminum hydride, di-n-propyl aluminum hydride, diisopropyl aluminum hydride, di-n-butyl aluminum hydride, dibutyl aluminum hydride, diisobutyl aluminum hydride (DIBAH), di-n-octyl aluminum hydride, diphenyl aluminum hydride, di-p-tolyl aluminum hydride, dibenzyl aluminum hydride, phenylethyl aluminum hydride, phenyl-n-propyl aluminum hydride, phenylisopropyl aluminum hydride, phenyl-n-butyl aluminum hydride, phenylisobutyl aluminum hydride, phenyl-n-octyl aluminum hydride, p-tolylethyl aluminum hydride, p-tolyl-n-propyl aluminum hydride, p-tolylisopropyl aluminum hydride, p-tolyl-n-butyl aluminum hydride, p-tolylisobutyl aluminum hydride, p-tolyl-n-octyl aluminum hydride, benzylethyl aluminum hydride, benzyl-n-propyl aluminum hydride, benzylisopropyl aluminum hydride, benzyl-n-butyl aluminum hydride, benzylisobutyl aluminum hydride and benzyl-n-octyl aluminum hydride; alkyl aluminum dihydride such as n-propyl aluminum dihydride, isopropyl aluminum dihydride, n-butyl aluminum dihydride, isobutyl aluminum dihydride, and n-octylaluminum dihydride; and trialkylboron such as trimethylboron, triethylboron, triisobutylboron, tripropylboron and tributylboron, may be used without limitation.
Examples of the compound represented by Formula 4 may include trimethylammonium tetraphenylborate, triethylammonium tetraphenylborate, tripropylammonium tetraphenylborate, tributylammonium tetraphenylborate, N,N-diethylanilinium tetraphenylborate, trimethylammonium tetra(p-tolyl)borate, triethylammonium tetra(p-tolyl)borate, tripropylammonium tetra(p-tolyl)borate, tributylammonium tetra(p-tolyl)borate, N,N-diethylanilinium tetra(p-tolyl)borate, trimethylammonium tetra(o,p-dimethylphenyl)borate, triethylammonium tetra(o,p-dimethylphenyl)borate, tripropylammonium tetra(o,p-dimethylphenyl)borate, tributylammonium tetra(o,p-dimethylphenyl)borate, N,N-diethylanilinium tetra(o,p-dimethylphenyl)borate, trimethylammonium tetrakis(p-trifluoromethylphenyl)borate, triethylammonium tetrakis(p-trifluoromethylphenyl)borate, tripropylammonium tetrakis(p-trifluoromethylphenyl)borate, tributylammonium tetrakis(p-trifluoromethylphenyl)borate, N,N-diethylanilinium tetrakis(p-trifluoromethylphenyl)borate, trimethylammonium tetrakis(pentafluorophenyl)borate, triethylammonium tetrakis(pentafluorophenyl)borate, tripropylammonium tetrakis(pentafluorophenyl)borate, tributylammonium tetrakis(pentafluorophenyl)borate, N,N-diethylanilinium tetrais(pentafluorophenyl)borate, trimethylphosphonium tetraphenylborate, triethylphosphonium tetraphenylborate, tripropylphosphonium tetraphenylborate, tributylphosphonium tetraphenylborate, trimethylcarbonium tetraphenylborate, triethylcarbonium tetraphenylborate, tripropylcarbonium tetraphenylborate, tributylcarbonium tetraphenylborate, trimethylammonium tetraphenylaluminate, triethylammonium tetraphenylaluminate, tripropylammonium tetraphenylaluminate, tributylammonium tetraphenylaluminate, trimethylammonium tetra(p-tolyl)aluminate, triethylammonium tetra(p-tolyl)aluminate, tripropylammonium tetra(p-tolyl)aluminate, tributylammonium tetra(p-tolyl)aluminate, or the like, without limitation.
Examples of the compound represented by Formula 5 may include dihexyl(methyl)ammonium tetrakis(pentafluorophenyl) borate, dioctyl(methyl)ammonium tetrakis(pentafluorophenyl) borate, methyldi(octyl)ammonium tetrakis(pentafluorophenyl) borate, methyldi (methyl) ammonium tetrakis(pentafluorophenyl) borate, dodecyldi(methyl)ammonium tetrakis(pentafluorophenyl) borate, tetradecyldi(methyl)ammonium tetrakis(pentafluorophenyl) borate, hexadecyldi(methyl)ammonium tetrakis(pentafluorophenyl) borate, octadecyldi(methyl)ammonium tetrakis(pentafluorophenyl) borate, eicosyldi(methyl)ammonium tetrakis(pentafluorophenyl) borate, methyldi(decyl)ammonium tetrakis(pentafluorophenyl) borate, methyldi(dodecyl)ammonium tetrakis(pentafluorophenyl) borate, methyldi(tetradecyl)ammonium tetrakis(pentafluorophenyl) borate, methyldi(hexadecyl)ammonium tetrakis(pentafluorophenyl) borate, methyldi(octadecyl)ammonium tetrakis(pentafluorophenyl) borate, methyldi(eicosyl)ammonium tetrakis(pentafluorophenyl) borate, trihexylammonium tetrakis(pentafluorophenyl) borate, trioctylammonium tetrakis(pentafluorophenyl) borate, tri(2-ethylhexyl)ammonium tetrakis(pentafluorophenyl) borate, tri(iso-octyl)ammonium tetrakis(pentafluorophenyl) borate, tridecylammonium tetrakis(pentafluorophenyl) borate, tridodecylammonium tetrakis(pentafluorophenyl) borate, tritetradecylammonium tetrakis(pentafluorophenyl) borate, trihexadecylammonium tetrakis(pentafluorophenyl) borate, trioctadecylammonium tetrakis(pentafluorophenyl) borate, trieicosylammonium tetrakis(pentafluorophenyl) borate, hexyldi (n-butyl) ammonium tetrakis(pentafluorophenyl) borate, octyldi (n-butyl) ammonium tetrakis(pentafluorophenyl) borate, decyldi (n-butyl) ammonium tetrakis(pentafluorophenyl) borate, dodecyldi(n-butyl)ammonium tetrakis(pentafluorophenyl) borate, octadecyldi(n-butyl)ammonium tetrakis(pentafluorophenyl) borate, N,N-dihexylanilinium tetrakis(pentafluorophenyl) borate, N,N-dioctylanilinium tetrakis(pentafluorophenyl) borate, N,N-didodecylanilinium tetrakis(pentafluorophenyl) borate, N-methyl-N-dodecylanilinium tetrakis(pentafluorophenyl) borate, N,N-di(octadecyl) (2,4,6-trimethylanilinium) tetrakis(pentafluorophenyl) borate, cyclohexyldi(dodecyl)ammonium tetrakis(pentafluorophenyl)borate, methyldi(dodecyl)ammonium tetrakis-(2,3,4,6-tetrafluorophenyl) borate, trioctylphosphonium tetrakis(pentafluorophenyl) borate, trihexylphosphonium tetrakis(pentafluorophenyl) borate, tributylphosphonium tetrakis(pentafluorophenyl) borate, dioctyl(methyl)phosphonium tetrakis(pentafluorophenyl) borate, dimethyl(octyl)phosphonium tetrakis(pentafluorophenyl) borate, bis(dihexylsulfide)onium tetrakis(pentafluorophenyl) borate, bis(dioctylsulfide)onium tetrakis(pentafluorophenyl) borate, bis(didecylsulfide)onium tetrakis(pentafluorophenyl) borate, and bis(didodecylsulfide)onium tetrakis(pentafluorophenyl) borate, or the like, without limitation.
Meanwhile, the amount ratio of the components constituting the catalyst system may be determined considering catalyst activity and selectivity to a linear alpha-olefin. According to an embodiment, in the case of the three-component-based catalyst system, the molar ratio of the diphosphino aminyl residue of the ligand compound: chromium source: cocatalyst may preferably be controlled to about 1:1:1 to 10:1:10,000, or about 1:1:100 to 5:1:3,000. In addition, in the case of the two-component-based catalyst system, the molar ratio of the diphosphino aminyl residue of the organochromium compound: cocatalyst may preferably be controlled to 1:1 to 1:10,000, or 1:1 to 1:5,000, or 1:1 to 1:3,000.
Also, the components constituting the catalyst system may be added simultaneously or in an arbitrary order, in the presence or absence of a suitable solvent and monomer, so as to act as a catalyst system having activity. In this case, the suitable solvent may use heptane, toluene, cyclohexane, methylcyclohexane, 1-hexene, 1-octene, diethyl ether, tetrahydrofuran, acetonitrile, dichloromethane, chloroform, chlorobenzene, methanol, acetone, or the like.
In addition, the catalyst system may further include a support. That is, the ligand compound represented by Formula 1 may be applied in a supported state to a support for the oligomerization of ethylene. The support may be a metal, a metal salt or a metal oxide, which may be applied to a general support catalyst. Non-limiting examples of the support may include silica, silica-alumina, silica-magnesia, or the like, and may include a metal oxide, metal carbonate, metal sulfate, or metal nitrate, such as Na2O, K2CO3, BaSO4, and Mg(NO3)2.
Such a catalyst system may preferably be used for the trimerization or tetramerization reaction of ethylene, and may produce 1-hexene or 1-octene with high selectivity by the above-description.
In addition, the present invention provides a method for preparing a linear alpha-olefin, including the step of oligomerizing ethylene in the presence of the catalyst system.
The oligomerization reaction of olefin may be the trimerization or tetramerization reaction of ethylene, and may form 1-hexene or 1-octene as a reaction result.
The method of oligomerizing ethylene according to the present invention may be performed by using ethylene as a raw material and applying the above-described catalyst system, a common apparatus and contacting technique. Non-limiting examples of the oligomerization reaction of ethylene may include homogeneous liquid phase reaction in the presence or absence of an inert solvent, slurry reaction by which a portion or whole of the catalyst system is not dissolved, bulk phase reaction in which an alpha-olefin product acts as a main medium, or gas phase reaction.
The oligomerization reaction of olefin may be performed under an inert solvent. Non-limiting examples of the inert solvent may include benzene, toluene, xylene, cumene, chlorobenzene, dichlorobenzene, heptane, cyclohexane, methylcyclohexane, methylcyclopentane, n-hexane, 1-hexene, 1-octene, or the like.
The polymerization of the olefin may be performed under a temperature of about 0 to about 200° C., or about 0 to about 150° C., or about 30 to about 100° C., or about 50 to about 100° C. In addition, the reaction may be performed under a pressure of about 15 to about 3000 psig, or about 15 to about 1500 psig, or about 15 to about 1000 psig.
Hereinafter, the present invention will be explained in more detail referring to the examples. However, the examples are for illustrating the present invention, and the scope of the present invention is not limited thereto.
[Synthesis of Ligand Compounds]
Ligand compounds of Synthetic Examples 1 to 17 were prepared according to the reaction below.
In the reaction, 1-bromo-4-cyclohexylbenzene (2 eq, 20 mmol) of which R is cyclohexyl was dissolved in THF (20 mL) and cooled to −78° C. While keeping the temperature, n-BuLi (2 eq, 20 mmol) was added thereto dropwisely, followed by stirring for 3 hours. Dichloro(diethylamino)phosphine (1 eq, 10 mmol) dissolved in THF (10 mL) was added thereto dropwisely, and the temperature was raised to room temperature, followed by stirring overnight. After removing the solvent in vacuum, the reaction product was dissolved in hexane (30 mL) without additional purification, and hydrochloric acid (2 eq) dissolved in ether was added thereto. After stirring for 15 minutes, filtering was performed, and the filtrate was dried in vacuum.
Then, the compound thus obtained (2.1 eq, 2.1 mmol) was dissolved in DCM (3.8 mL), and TEA (3 eq, 3 mmol) was added thereto. Cyclohexylamine (1 eq, 1 mmol) dissolved in DCM (3.8 mL) was slowly added to a reaction system, followed by stirring at room temperature overnight. After removing the solvent in vacuum, the resultant product was dissolved in hexane (7.6 mL) and loaded on the top of silica. Silica filtration was performed using 1% TEA-added hexane/DCM or 1% TEA-added hexane, and the solution thus obtained was concentrated to obtain a ligand compound.
1H NMR (500 MHz, C6D6): δ 7.58 (br. s, 8H), δ 7.08 (d, 8H), δ 3.47 (pent, 1H), δ 2.35 (t, 4H), δ 2.21-2.11 (m, 2H), δ 1.80 (d, 8H), δ 1.71-1.56 (m, 16H), δ 1.44-1.11 (m, 24H)
The preparation was performed by the same method as in Synthetic Example 1 except for using a compound in which R is phenyl instead of 1-bromo-4-cyclohexylbenzene (R=cyclohexyl)
1H NMR (500 MHz, C6D6): δ 7.92-7.42 (m, 24H), δ 7.17 (t, 8H), δ 7.10 (t, 4H), δ 3.58 (pent, 1H), δ 2.28-2.17 (m, 2H), δ 1.84-1.77 (m, 2H), δ 1.67-1.60 (m, 2H), δ 1.48-1.42 (m, 1H), δ 1.18-1.07 (m, 3H)
The preparation was performed by the same method as in Synthetic Example 1 except for using a compound in which R is 1-adamantyl instead of 1-bromo-4-cyclohexylbenzene (R=cyclohexyl).
1H NMR (500 MHz, C6D6): δ 7.52 (br. s, 8H), δ 6.99 (d, 8H), δ 3.43 (pent, 1H), δ 2.43-2.36 (m, 24H), δ 2.26-2.10 (m, 14H), δ 1.85-1.74 (m, 26H), δ 1.65-1.58 (m, 2H), δ 1.46-1.40 (m, 1H), δ 1.16-1.05 (m, 3H)
The preparation was performed by the same method as in Synthetic Example 1 except for using a compound in which R is 2-adamantyl instead of 1-bromo-4-cyclohexylbenzene (R=cyclohexyl).
1H NMR (500 MHz, C6D6): δ 7.56 (br. s, 8H), δ 7.05 (d, 8H), δ 3.45 (pent, 1H), δ 3.18 (t, 4H), δ 2.38-2.32 (m, 8H), δ 2.30-2.17 (m, 10H), δ 1.85-1.72 (m, 42H), δ 1.67-1.60 (m, 2H), δ 1.48-1.42 (m, 1H), δ 1.18-1.07 (m, 3H)
The preparation was performed by the same method as in Synthetic Example 1 except for using a compound in which R is cycloheptyl instead of 1-bromo-4-cyclohexylbenzene (R=cyclohexyl).
1H NMR (500 MHz, C6D6): δ 7.57 (br. s, 8H), δ 7.07 (d, 8H), δ 3.46 (pent, 1H), δ 2.34 (t, 4H), δ 2.28-2.17 (m, 2H), S 1.86-1.76 (m, 10H), δ 1.69-1.58 (m, 34H), δ 1.50-1.41 (m, 9H), S 1.18-1.07 (m, 3H)
The preparation was performed by the same method as in Synthetic Example 1 except for using a compound in which R is cyclooctyl instead of 1-bromo-4-cyclohexylbenzene (R=cyclohexyl).
1H NMR (500 MHz, C6D6): δ 7.57 (br. s, 8H), δ 7.07 (d, 8H), δ 3.45 (pent, 1H), δ 2.34 (t, 4H), δ 2.27-2.16 (m, 2H), δ 1.85-1.75 (m, 10H), δ 1.70-1.56 (m, 42H), δ 1.51-1.41 (m, 9H), δ 1.19-1.06 (m, 3H)
The preparation was performed by the same method as in Synthetic Example 1 except for using a compound in which R is octyl instead of 1-bromo-4-cyclohexylbenzene (R=cyclohexyl).
1H NMR (500 MHz, C6D6): δ 7.62 (br. s, 8H), δ 7.10 (d, 8H), δ 3.50 (pent, 1H), δ 2.64 (t, 8H), δ 2.28-2.17 (m, 2H), δ 1.95-1.75 (m, 42H), δ 1.67-1.60 (m, 2H), δ 1.48-1.42 (m, 1H), δ 1.18-1.07 (m, 3H), δ 0.77 (t, 12H)
The preparation was performed by the same method as in Synthetic Example 1 except for using a compound in which R is nonan-5-yl instead of 1-bromo-4-cyclohexylbenzene (R=cyclohexyl).
1H NMR (500 MHz, C6D6): δ 7.58 (br. s, 8H), δ 7.09 (d, 8H), δ 3.57 (pent, 1H), δ 2.38 (pent, 4H), δ 2.28-2.17 (m, 2H), δ 1.84-1.77 (m, 2H), δ 1.73-1.64 (m, 8H), δ 1.67-1.60 (m, 2H), δ 1.57-1.49 (m, 8H), δ 1.48-1.42 (m, 1H), δ 1.19-1.02 (m, 27H), S 1.00-0.89 (m, 8H), δ 0.77 (t, 24H)
The preparation was performed by the same method as in Synthetic Example 1 except for using a compound in which R is 5-butyl-nonan-5-yl instead of 1-bromo-4-cyclohexylbenzene (R=cyclohexyl).
1H NMR (500 MHz, C6D6): δ 7.51 (br. s, 8H), δ 7.00 (d, 8H), δ 3.43 (pent, 1H), δ 2.28-2.17 (m, 2H), δ 1.84-1.77 (m, 2H), δ 1.73-1.64 (m, 12H), δ 1.67-1.60 (m, 2H), δ 1.57-1.49 (m, 12H), δ 1.48-1.42 (m, 1H), δ 1.19-1.02 (m, 31H), δ 1.00-0.89 (m, 8H), δ 0.77 (t, 36H)
The preparation was performed by the same method as in Synthetic Example 1 except for using a compound in which R is tributylsilyl instead of 1-bromo-4-cyclohexylbenzene (R=cyclohexyl).
1H NMR (500 MHz, C6D6): δ 8.07-7.38 (m, 16H), δ 3.40 (pent, 1H), δ 2.15-2.01 (m, 2H), δ 1.60-1.49 (m, 4H), δ 1.40-1.29 (m, 48H), δ 1.05-0.97 (m, 2H), δ 0.93-0.85 (m, 38H), δ 0.84-0.77 (m, 24H)
The preparation was performed by the same method as in Synthetic Example 1 except for using a compound in which R is tributylsilyl instead of 1-bromo-4-cyclohexylbenzene (R=cyclohexyl) and using 2-methylcyclohexaneamine instead of cyclohexaneamine.
1H NMR (500 MHz, C6D6): δ 8.05-7.36 (m, 16H), δ 3.30 (q, 1H), δ 2.13-2.00 (m, 2H), δ 1.59-1.50 (m, 3H), δ 1.41-1.28 (m, 48H), δ 1.04-0.96 (m, 2H), δ 0.94-0.84 (m, 41H), δ 0.83-0.75 (m, 24H)
The preparation was performed by the same method as in Synthetic Example 1 except for using a compound in which R is tributylsilyl instead of 1-bromo-4-cyclohexylbenzene (R=cyclohexyl) and using 3-methylcyclohexaneamine instead of cyclohexaneamine.
1H NMR (500 MHz, C6D6): δ 8.06-7.38 (m, 16H), δ 3.38 (pent, 1H), δ 2.14-2.01 (m, 2H), δ 1.61-1.48 (m, 4H), δ 1.41-1.29 (m, 48H), δ 1.04-0.95 (m, 2H), δ 0.94-0.85 (m, 40H), δ 0.84-0.76 (m, 24H)
The preparation was performed by the same method as in Synthetic Example 1 except for using a compound in which R is tributylsilyl instead of 1-bromo-4-cyclohexylbenzene (R=cyclohexyl) and using 4-methylcyclohexaneamine instead of cyclohexaneamine.
1H NMR (500 MHz, C6D6): δ 8.07-7.38 (m, 16H), δ 3.39 (pent, 1H), δ 2.15-2.01 (m, 2H), δ 1.65-1.49 (m, 3H), δ 1.40-1.29 (m, 48H), δ 1.05-0.96 (m, 2H), δ 0.93-0.85 (m, 41H), δ 0.84-0.75 (m, 24H)
The preparation was performed by the same method as in Synthetic Example 1 except for using a compound in which R is tributylsilyl instead of 1-bromo-4-cyclohexylbenzene (R=cyclohexyl) and using cycloheptaneamine instead of cyclohexaneamine.
1H NMR (500 MHz, C6D6): δ 8.06-7.35 (m, 16H), δ 3.37 (pent, 1H), δ 2.15-2.01 (m, 2H), δ 1.62-1.47 (m, 6H), δ 1.40-1.29 (m, 48H), δ 1.05-0.97 (m, 2H), δ 0.93-0.85 (m, 38H), δ 0.84-0.77 (m, 24H)
The preparation was performed by the same method as in Synthetic Example 1 except for using a compound in which R is tributylsilyl instead of 1-bromo-4-cyclohexylbenzene (R=cyclohexyl) and using cyclooctaneamine instead of cyclohexaneamine.
1H NMR (500 MHz, C6D6): δ 8.07-7.34 (m, 16H), δ 3.37 (pent, 1H), δ 2.14-2.00 (m, 2H), δ 1.62-1.47 (m, 6H), δ 1.40-1.29 (m, 48H), δ 1.07-0.95 (m, 4H), δ 0.93-0.85 (m, 38H), δ 0.84-0.77 (m, 24H)
The preparation was performed by the same method as in Synthetic Example 1 except for using a compound in which R is tripropylsilyl instead of 1-bromo-4-cyclohexylbenzene (R=cyclohexyl).
1H NMR (500 MHz, C6D6): δ 8.09-7.39 (m, 16H), δ 3.42 (pent, 1H), δ 2.17-2.02 (m, 2H), δ 1.61-1.50 (m, 4H), δ 1.42-1.30 (m, 24H), δ 1.06-0.97 (m, 2H), δ 0.93-0.86 (m, 38H), δ 0.85-0.77 (m, 24H)
The preparation was performed by the same method as in Synthetic Example 1 except for using a compound in which R is tributylsilyl instead of 1-bromo-4-cyclohexylbenzene (R=cyclohexyl) and using 2,3-dihydro-1H-indene-ylamine instead of cyclohexaneamine.
1H NMR (500 MHz, C6D6): δ 8.07-7.38 (m, 18H), δ 7.13 (d, 2H), δ 3.53 (pent, 1H), δ 2.52-2.41 (m, 2H), δ 2.01-1.88 (m, 2H), δ 1.40-1.29 (m, 48H), δ 0.93-0.85 (m, 36H), δ 0.84-0.77 (m, 24H)
The preparation was performed by the same method as in Synthetic Example 1 except for using a compound in which R is tripropylsilyl instead of 1-bromo-4-cyclohexylbenzene (R=cyclohexyl) and using cycloheptaneamine instead of cyclohexaneamine.
1H NMR (500 MHz, C6D6): δ 8.20-7.65 (br, 4H), δ 7.60-7.15 (br, 4H), δ 7.45 (s, 8H), δ 3.69 (pent, 1H), δ 2.30 (m, 2H), 1.90-1.80 (m, 2H), δ 1.60-1.50 (m, 2H), δ 1.48-1.20 (m, 40H), δ 0.98 (t, 36H), δ 0.77 (m, 24H)
The preparation was performed by the same method as in Synthetic Example 1 except for using a compound in which R is tripropylsilyl instead of 1-bromo-4-cyclohexylbenzene (R=cyclohexyl) and using cyclooctaneamine instead of cyclohexaneamine.
1H NMR (500 MHz, C6D6): δ 8.15-7.70 (br, 4H), δ 7.45 (d, 8H), δ 7.70-7.45 (br, 4H), δ 3.81 (pent, 1H), δ 2.43-2.28 (m, 2H), δ 1.88-1.75 (m, 2H), δ 1.62-1.55 (m, 2H), δ 1.55-1.48 (m, 2H), δ 1.48-1.29 (m, 38H), δ 0.97 (t, 40H), δ 0.81-0.72 (m, 26H)
The preparation was performed by the same method as in Synthetic Example 1 except for using a compound in which R is tripropylsilyl instead of 1-bromo-4-cyclohexylbenzene (R=cyclohexyl) and using 2,3-dihydro-1H-indene-2-amine instead of cyclohexaneamine.
1H NMR (500 MHz, C6D6): δ 7.70-7.25 (m, 16H), δ 7.05-6.95 (m, 4H), δ 4.68-4.54 (m, 1H), δ 3.72-3.62 (m, 2H), δ 2.74-2.68 (m, 2H), δ 1.42-1.32 (m, 24H), δ 1.01-0.94 (m, 36H), δ 0.79-0.73 (m, 24H)
The preparation was performed by the same method as in Synthetic Example 20 except for using 2,3-dihydro-1H-indene-1-amine instead of 2,3-dihydro-1H-indene-2-amine.
1H NMR (500 MHz, C6D6): δ 7.92-7.62 (m, 4H), δ 7.50-6.35 (m, 12H), δ 7.09-7.35 (m, 12H), δ 7.09-7.06 (m, 2H), δ 7.00-6.95 (m, 1H), δ 6.48 (d, 1H), δ 5.40-5.28 (m, 1H), δ 2.53-2.40 (m, 2H), δ 2.11-2.03 (m, 1H), δ 1.42-1.30 (m, 25H), δ 1.00-0.92 (m, 36H), δ 0.80-0.70 (m, 24H)
The preparation was performed by the same method as in Synthetic Example 20 except for using 1,2,3,4-tetrahydronaphthalene-1-amine instead of 2,3-dihydro-1H-indene-2-amine.
1H NMR (500 MHz, C6D6): δ 8.00-7.30 (m, 18H), δ 7.03-6.91 (m, 3H), δ 5.02 (q, 1H), δ 2.76-2.66 (m, 1H), δ 2.53-2.45 (m, 1H), δ 2.33-2.20 (m, 1H), δ 1.62-1.53 (m, 1H), δ 1.50-1.20 (m, 24H), δ 1.05-0.85 (m, 36H), δ 0.83-0.73 (m, 14H), δ 0.73-0.68 (m, 12H)
The preparation was performed by the same method as in Synthetic Example 1 except for using a compound in which R is tributylsilyl instead of 1-bromo-4-cyclohexylbenzene (R=cyclohexyl) and using 2,3-dihydro-1H-indene-1-amine instead of cyclohexaneamine.
1H NMR (500 MHz, C6D6): δ 8.06-7.92 (m, 4H), δ 7.48-7.36 (m, 12H), δ 7.11-7.08 (m, 2H), δ 7.01-6.98 (m, 1H), δ 6.63 (d, 1H), δ 5.72-5.58 (m, 1H), δ 2.53-2.40 (m, 2H), δ 2.11-2.03 (m, 1H), δ 1.48-1.36 (m, 48H), δ 1.04-0.97 (m, 36H), δ 0.86-0.70 (m, 24H)
The preparation was performed by the same method as in Synthetic Example 23 except for using 1,2,3,4-tetrahydronaphthalene-1-amine instead of 2,3-dihydro-1H-indene-1-amine.
1H NMR (500 MHz, C6D6): δ 8.01-7.29 (m, 18H), δ 7.12-6.99 (m, 3H), δ 5.05 (q, 1H), δ 2.98-2.77 (m, 1H), δ 2.43-2.32 (m, 1H), δ 2.30-2.27 (m, 1H), δ 1.62-1.53 (m, 1H), δ 1.52-1.23 (m, 48H), δ 1.08-0.89 (m, 36H), δ 0.81-0.70 (m, 13H), δ 0.66-0.64 (m, 12H)
In addition, the ligand compounds of Synthetic Examples 25 to 27 were prepared according to the reaction below.
p-dibromobenzene (1 eq, 40 mmol) was dissolved in ether (100 mL) and cooled to −78° C. n-BuLi (1.05 eq, 42 mmol) was slowly injected, and the temperature of the reactants was raised to room temperature, followed by stirring for 2 hours. The reaction product was cooled to −78° C., and 5-nonanone (1 eq, 40 mmol) was slowly injected thereto. The temperature of the reaction product was raised to room temperature, and stirring was performed overnight. After quenching with a NH4Cl saturated aqueous solution, extraction with DCM was performed. Moisture was removed using MgSO4, filtering was performed to remove a solid, and the solvent was removed under a reduced pressure. Through purification by silica column chromatography, a liquid compound was obtained.
To a suspension in which NaH (1.2 eq, 12 mmol) was dispersed in THF (31 mL), a solution in which the above compound (1 eq, 10 mmol) was dissolved in THF (93 mL) was slowly added. The reactants were stirred and refluxed for 2 hours. After cooling to room temperature, CH3-X (1.2 eq, 12 mmol; X=I, Br, Cl, OTf, etc.) where R is methyl in the Reaction was injected thereto, followed by stirring overnight. The solvent was removed under a reduced pressure, and through purification by silica column chromatography, 1-bromo-4-(5-methoxynonan-5-yl)benzene was obtained.
1-bromo-4-(5-methoxynonan-5-yl)benzene (2 eq, 20 mmol) was dissolved in THF (20 mL) and cooled to −78° C. While maintaining the temperature, n-BuLi (2 eq, 20 mmol) was added thereto dropwisely, and stirring was performed for 3 hours. Dichloro(diethylamino)phosphine (1 eq, 10 mmol) dissolved in THF (10 mL) was added thereto dropwisely, the temperature was raised to room temperature, and stirring was performed overnight. After removing the solvent in vacuum, the resultant product was dissolved in hexane (30 mL) without purification, and hydrochloric acid (2 eq) dissolved in ether was added thereto. After stirring for 15 minutes, filtering was performed, and the filtrate was dried in vacuum.
Then, the compound thus obtained (2.1 eq, 2.1 mmol) was dissolved in DCM (3.8 mL), and TEA (3 eq, 3 mmol) was added thereto. Cyclohexylamine (1 eq, 1 mmol) dissolved in DCM (3.8 mL) was slowly added to a reaction system, followed by stirring at room temperature overnight. After removing the solvent in vacuum, the resultant product was dissolved in hexane (7.6 mL) and loaded on the top of silica. Silica filtration was performed using 1% TEA-added hexane/DCM (1:1), and the solution thus obtained was concentrated to obtain a ligand compound.
1H NMR (500 MHz, C6D6): δ 7.58 (br. s, 8H), δ 7.08 (d, 8H), δ 3.58 (pent, 1H), δ 2.90 (s, 12H), δ 2.28-2.17 (m, 2H), δ 1.84-1.77 (m, 2H), δ 1.73-1.68 (m, 8H), δ 1.67-1.60 (m, 2H), b 1.56-1.49 (m, 8H), δ 1.48-1.42 (m, 1H), δ 1.18-1.03 (m, 27H), S 1.00-0.91 (m, 8H), δ 0.77 (t, 24H)
The same method was performed as in Synthetic Example 25 except for using a compound where R is benzyl instead of CH3—X (R=methyl).
1H NMR (500 MHz, C6D6): δ 7.60-7.32 (m, 28H), δ 7.08 (d, 8H), δ 3.58 (pent, 1H), δ 3.20 (s, 8H), δ 2.28-2.17 (m, 2H), δ 1.84-1.77 (m, 2H), δ 1.73-1.68 (m, 8H), δ 1.67-1.60 (m, 2H), b 1.56-1.49 (m, 8H), δ 1.48-1.42 (m, 1H), δ 1.18-1.03 (m, 27H), δ 1.00-0.91 (m, 8H), δ 0.77 (t, 24H)
The same method was performed as in Synthetic Example 25 except for using a compound where R is butyl instead of CH3—X (R=methyl).
1H NMR (500 MHz, C6D6): δ 7.57 (br. s, 8H), δ 7.07 (d, 8H), δ 3.58 (pent, 1H), δ 3.02 (t, 8H), δ 2.28-2.17 (m, 2H), δ 1.85-1.78 (m, 10H), δ 1.74-1.59 (m, 18H), δ 1.56-1.49 (m, 8H), δ 1.48-1.42 (m, 1H), δ 1.18-1.03 (m, 27H), δ 1.00-0.91 (m, 8H), δ 0.80-0.75 (m, 36H)
Under argon, 2-isopropylcyclohexan-1-amine (10 mmol) and triethylamine (3 eq. to amine) were dissolved in dichloromethane (80 mL). In a state of immersing a flask into a water bath, chlorobis(3,4-dimethylphenyl)phosphine (20 mmol) was slowly added, and then, stirred overnight. After removing the solvent in vacuum, another solvent of diethyl ether, tetrahydrofuran or hexane was injected, stirring was sufficiently performed, and a triethylammonium chloride salt was removed using an air-free glass filter. The solvent was removed from the filtrate to obtain a product.
31P NMR(202 MHz, CDCl3): δ 54.5 (br s)
Chlorobis(3,5-dimethylphenyl)phosphine (2.1 eq, 2.1 mmol) was dissolved in DCM (3.8 mL), and TEA (3 eq, 3 mmol) was added. Cyclohexaneamine (1 eq, 1 mmol) dissolved in DCM (3.8 mL) was slowly added to a reaction system, followed by stirring at room temperature overnight. After removing the solvent in vacuum, the resultant product was dissolved in hexane (7.6 mL) and loaded on the top of silica. Silica filtration was performed using 1% TEA-added hexane/DCM (1:1), and the solution thus obtained was concentrated to obtain a ligand compound.
The same method was performed as in Synthetic Example 1 except for using a compound where R is phenyl instead of 1-bromo-4-cyclohexylbenzene (R=cyclohexyl) and using methenamine instead of cyclohexaneamine.
The same method was performed as in Synthetic Example 1 except for using a compound where R is tributylsilyl instead of 1-bromo-4-cyclohexylbenzene (R=cyclohexyl) and using isopropylamine instead of cyclohexaneamine.
Chlorodiphenylphosphine (2.1 eq, 2.1 mmol) was dissolved in DCM (3.8 mL), and TEA (3 eq, 3 mmol) was added. An amine compound below (1 eq, 1 mmol) dissolved in DCM (3.8 mL) was slowly added to a reaction system, followed by stirring at room temperature overnight. After removing the solvent in vacuum, the resultant product was dissolved in hexane (7.6 mL) and loaded on the top of silica. Silica filtration was performed using 1% TEA-added hexane/DCM (1:1), and the solution thus obtained was concentrated to obtain a ligand compound.
1H NMR (500 MHz, C6D6): δ 7.50-6.70 (br s, 2H), δ 3.03 (apparent quintet, J=6.3 Hz, 1H), δ 1.62-1.05 (m, 64H), δ 0.88 (t, J=6.6 Hz, 6H)
The same method was performed as in Synthetic Example 1 except for using a compound where R is triisopropylsilyl instead of 1-bromo-4-cyclohexylbenzene (R=cyclohexyl) and using isopropylamine instead of cyclohexaneamine.
1H NMR (500 MHz, C6D6): δ 8.12-7.26 (br, 8H), δ 7.45 (d, J=6.6 Hz, 8H), δ 3.83 (m, 1H, NCH), δ 1.32 (m, 12H, SiCH), δ 1.23 (d, J=6.6 Hz, 6H, NCHCH3), δ 1.10 ppm (t, J=7.8 Hz, 72H, CH3)
The same method was performed as in Synthetic Example 1 except for using chlorobis(3,4-dicyclohexylphenyl)phosphine instead of chlorobis(3,4-dimethylphenyl)phosphine.
The same method was performed as in Synthetic Example 1 except for using a compound where R is tripropylsilyl instead of 1-bromo-4-cyclohexylbenzene (R=cyclohexyl) and using tripropylamine instead of cyclohexaneamine.
1H NMR (500 MHz, C6D6): δ 8.16-7.20 (br, 8H), δ 7.46 (d, J=6.8 Hz, 8H), δ 3.87 (m, 1H, NCH), δ 1.42-1.33 (br, 48H), δ 1.27 (d, J=6.0 Hz, 6H, NCHCH3), δ 0.98 (t, J=7.8 Hz, 36H, CH3), δ 0.74 ppm (q, J=7.2 Hz, 48H, SiCH2)
[Manufacture of Catalyst System and Process of Ethylene Oligomerization Reaction]
Under an argon gas atmosphere, chromium(III) acetylacetonate (Cr(acac)3, 17.5 mg, 0.05 mmol) and the ligand compound (0.010 mmol) according to Synthetic Example 1 were put in a flask, and methylcyclohexane (100 mL) was added and stirred to prepare a catalyst solution of 5 mM (based on Cr).
A Parr reactor with a volume of 600 mL was prepared, vacuum was applied at 120° C. for 2 hours, the inside was replaced with argon, and the temperature was reduced to 80° C. Then, cyclohexane (180 mL) and 2 mL of MMAO (isoheptane solution, Al/Cr=600) were injected, and the catalyst solution (2 mL, 1.0 μmol Cr) was injected thereto. After stirring at 500 rpm for 2 minutes, the valve of an ethylene line adjusted to 30 bar was opened to fill the inside of the reactor with ethylene, and then, stirring was performed at 500 rpm for 15 minutes. The ethylene line valve was closed, the reactor was cooled to 0° C. using a dry ice/acetone bath, unreacted ethylene was slowly ventilated, and 0.5 mL of nonane (GC internal standard) was injected. After stirring for 10 seconds, 2 mL of a liquid part of the reactor was taken and quenched with water, and an organic part thus obtained was filtered using a PTFE syringe filter to manufacture a GC-FID sample.
Then, the distribution of a liquid product was analyzed by GC (Agilent Co., 6890N, Alltech AT-5 (30 m×0.32 mm ID×0.25 μm; series no. 12446)). To a remaining solution, 400 mL of ethanol/HCl (10 vol % of aqueous 12 M HCl solution) was added, stirring and filtering were performed, and the amount of a solid product was analyzed. The polymer thus obtained was dried in a vacuum oven of 65° C. overnight.
The same method as in Example 1a was performed except for changing the type of the catalyst as in Table 1 below.
Under an argon gas atmosphere, chromium(III) chloride tetrahydrofuran (Cr (THF)3Cl3, 0.05 mmol), the ligand compound (0.5 mmol) according to Synthetic Example 1, and N,N-dimethylanilinium tetrakis(pentafluorophenyl)borate (AB, 0.5 mmol) were put in a flask, dichloromethane (30 mL) was added and stirred for 1 hour, the solvent was removed in vacuum, and the resultant product was dissolved in methylcyclohexane to prepare a catalyst solution of 5 mM (based on Cr).
A Parr reactor with a volume of 600 mL was prepared, vacuum was applied at 120° C. for 2 hours, the inside was replaced with argon, and the temperature was reduced to 80° C. Then, methylcyclohexane (180 mL) and TIBAL (300 μmol) were injected, and the catalyst solution (2 mL, 1.0 μmol Cr) was injected thereto. The valve of an ethylene line adjusted to 30 bar was opened to fill the inside of the reactor with ethylene, and then, stirring was performed at 500 rpm for 15 minutes. The ethylene line valve was closed, the reactor was cooled to 0° C. using a dry ice/acetone bath, unreacted ethylene was slowly ventilated, and 0.5 mL of nonane (GC internal standard) was injected thereto. After stirring for 10 seconds, 2 mL of a liquid part of the reactor was taken and quenched with water, and an organic part thus obtained was filtered using a PTFE syringe filter to manufacture a GC-FID sample. Then, the distribution of a liquid product was analyzed by GC. To a remaining solution, 400 mL of ethanol/HCl (10 vol % of aqueous 12 M HCl solution) was added, stirring and filtering were performed, and the amount of a solid product was analyzed. The polymer thus obtained was dried in a vacuum oven of 65° C. overnight.
The same method as in Example 1b was performed except for changing the type of the catalyst as in Table 2 below.
The ethylene oligomerization reaction results according to the Examples and Comparative Examples are summarized in Table 3 and Table 4 below.
(1) Catalyst Activity (Ton/Mol·Cr/Hr)
From the total weight (ton) value of the product obtained by combining the weights (ton) of the liquid product and solid product obtained, the catalyst activity was calculated.
(2) 1-C6 or 1-C8 Selectivity
From the GC analysis results of the distribution of a liquid product, the 1-hexene (1-C6) and 1-octene (1-C8) contents were calculated, and the wt % of 1-hexene or 1-octene based on the total weight of the product was calculated.
(3) Solid (wt %)
The wt % of the solid product based on the total weight of the product was calculated. The solid means insoluble solid which is not dissolved in a solvent, and represents the degree of production of polyethylene with a carbon number of about 40 or more.
As confirmed in Table 1 and Table 2, the catalyst system including an organochromium compound of the present invention has excellent catalyst activity and shows high selectivity to 1-hexene and 1-octene during polymerizing an olefin-based monomer, thereby enabling more efficient preparation of an alpha-olefin. As shown in Table 3, the catalyst activity was excellent in all of the Examples, and the amount of by-products such as a solid alpha-olefin was reduced when compared to Comparative Examples 1a and 2a, which used ligand compounds in which a methyl substituent having a small size was bonded to phenyl, and Comparative Example 3a which used a ligand compound in which not cycloalkyl but alkyl was bonded to nitrogen. It was found that the selectivity to an alpha-olefin (1-hexene and 1-octene) was even higher. In addition, in the case of using a compound (Comparative Synthetic Example 7) in which bulky substituents were bonded to both meta and para of phenyl, it could be found that the catalyst activity was rather reduced, because the approach of a monomer was difficult due to the excessively bulky catalyst structure like in Comparative Example 7a.
In the results of Table 4, using different types of cocatalysts and chromium sources, the Examples showed improved catalyst activity and alpha-olefin selectivity, and reduced production amount of a solid type alpha-olefin by-products when compared to Comparative Examples 1b and 2b, in which ligand compounds in which a methyl substituent was bonded to a phenyl group were used, and Comparative Examples 3b to 6b, in which ligand compounds in which alkyl was bonded to nitrogen were used.
As described above, in the catalyst of the present invention, cycloalkyl or aryl-fused cycloalkyl is bonded to N, and a bulky substituent is positioned at a para position of phenyl bonded to P, and it could be found that catalyst activity is high, and the production amounts of by-products could be reduced in ethylene oligomerization reaction, and an alpha-olefin could be prepared with high selectivity. In addition, it was confirmed that such effects are intrinsic effects shown by the structure of a ligand compound irrespective of the type of the cocatalyst or chromium source.
| Number | Date | Country | Kind |
|---|---|---|---|
| 10-2020-0118561 | Sep 2020 | KR | national |
| 10-2021-0070100 | May 2021 | KR | national |
| 10-2021-0123295 | Sep 2021 | KR | national |
| 10-2021-0123296 | Sep 2021 | KR | national |
| 10-2021-0123303 | Sep 2021 | KR | national |
The present application is a national stage entry under U.S.C. § 371 of International Application No. PCT/KR2021/012636 filed on Sep. 15, 2021, which claims priority to Korean Patent Application Nos. 10-2020-0118561 filed on Sep. 15, 2020, 10-2021-0070100 filed on May 31, 2021, and 10-2021-0123295, 10-2021-0123296 and 10-2021-0123303 filed on Sep. 15, 2021, all the disclosures of which are incorporated herein by reference.
| Filing Document | Filing Date | Country | Kind |
|---|---|---|---|
| PCT/KR2021/012636 | 9/15/2021 | WO |
