KR20240004095A - Ethylene oligomerization catalyst including ligand compound, catalyst composition employing same, and method for preparing ethylene oligomer using same - Google Patents

Abstract

The present invention relates to an ethylene oligomerization catalyst containing a ligand compound, a catalyst composition employing the same, and a method for producing ethylene oligomer using the same. It exhibits excellent selectivity for oligomers and selectivity for 1-hexene, and is an industrially useful chemical raw material. Phosphorus 1-hexene can be mass-produced with high purity.

Description

Ethylene oligomerization catalyst including ligand compound, catalyst composition employing same, and method for preparing ethylene oligomer using same}

The present invention relates to an ethylene oligomerization catalyst containing a ligand compound, a catalyst composition employing the same, and a method for producing ethylene oligomer using the same.

Olefin oligomerization from ethylene is used as a raw material for a variety of useful chemical products. Specifically, olefin oligomers can be used as raw materials to provide higher olefins, and industrially important processes include the production of alpha olefins from ethylene. In particular, among alpha olefins produced from ethylene, the production of 1-hexene through trimerization of ethylene is very important.

However, the problem encountered in the above oligomerization is that the selectivity for single oligomers is low. That is, along with the desired oligomer, unwanted side products and byproducts such as other oligomers and polymers may also be formed. For example, when 1-hexene is produced by oligomerizing ethylene, not only other isomers of hexene, 2-hexene and 3-hexene, can be formed, but also octene, decene, and dodecene, which are higher oligomers of ethylene. And higher molecular weight polyethylene can also be formed.

By-products and by-products produced as described above may cause problems in the process or efficiency. The produced polymer may be deposited on the internal parts, pipelines, and/or other equipment of the oligomerization reactor, which may require a period of stopping the process equipment to remove it, and may require steam treatment or water treatment for removal. It may take time and cost for physical processing, etc. In addition, production efficiency may be very low due to additional processes and time required to separate the desired oligomer from the generated by-products and by-products.

Meanwhile, the olefin oligomerization reaction from ethylene can be performed in an aliphatic hydrocarbon solvent. For example, cyclohexane, methylcyclohexane, hexane, and heptane can be used in processes to produce 1-hexene, and while these solvents may have excellent solubility for organometallic catalysts, their Since they have similar boiling points, problems may arise in terms of cost and time, such as requiring a high distillation stage and consuming a lot of heat during separation.

To meet the demand for high single alpha olefin selectivity, especially high 1-hexene selectivity, new processes are being developed. Selective C6-commercialization process created by Chevron Phillips (see JTDixon, MJGreen, FMHess, DHMorgan, "Advances in selective ethylene trimerisation - a critical overview", Journal of Organometallic Chemistry 689 (2004) 3641-3668) This is known, and the patent application filed by Sasol (WO 03/053891 A1) describes a typical CrCl ₃ (bis-(2-diphenylphosphino-ethyl)amine) (CrCl ₃ (bis-(2-diphenylphosphino) -ethyl)amine)/MAO (methylaluminoxane) type chromium-based selective ethylene-trimerization catalyst systems are disclosed. However, all these catalyst systems are 1-hexene. In addition, significant amounts of by-products and by-products such as polyethylene and other alpha olefins are produced.

That is, there still remains a need for catalyst systems with increased selectivity of alpha olefins to the desired olefin isomers and high efficiency. Therefore, research is needed on catalysts and preparation methods that can achieve improved selectivity, reduced by-products and by-product formation, improved yield of the desired alpha olefin, improved economics, and improved efficiency.

Japanese published patent 2007-045837 A U.S. published patent 2017-0341998　A1

The purpose of the present invention is to provide an ethylene oligomerization catalyst containing a ligand compound and exhibiting excellent 1-hexene selectivity.

Another object of the present invention is to provide an ethylene oligomerization catalyst composition employing the above catalyst, which has excellent activity and improved selectivity even at high temperatures.

The present invention provides a method for producing ethylene oligomers using the above catalyst composition, which is easily commercially available.

The present invention provides an ethylene oligomerization catalyst comprising a chromium compound and a ligand compound represented by the following formula (1).

[Formula 1]

[In Formula 1 above,

L ₁ and L ₂ are independently (C2-C4)alkylene;

R ₁ to R ₄ are each independently hydrogen, (C1-C10)alkyl, (C3-C20)cycloalkyl, (C6-C20)aryl, (C6-C20)aryl(C1-C10)alkyl, or (C1-C10) ) alkoxy;

The aryl of R ₁ to R ₄ is one or more substituents selected from the group consisting of (C1-C10)alkyl, (C6-C20)aryl, tri(C1-C10)alkylsilyl, and (C1-C10)alkoxy. May be replaced.]

In detail, L ₁ and L ₂ of Formula 1 are independently (C2-C3)alkylene; R ₁ to R ₄ are each independently hydrogen, (C1-C7)alkyl, (C3-C12)cycloalkyl, (C6-C12)aryl, (C6-C12)aryl(C1-C7)alkyl, or (C1-C7) ) alkoxy; The aryl of R ₁ to R ₄ is one or more substituents selected from the group consisting of (C1-C7)alkyl, (C6-C12)aryl, tri(C1-C7)alkylsilyl, and (C1-C7)alkoxy. can be replaced.

In more detail, L ₁ and L ₂ of Formula 1 are independently (C2-C3) alkylene; R ₁ to R ₄ are independently hydrogen, (C1-C7)alkyl, (C6-C12)aryl, or (C6-C12)aryl(C1-C7)alkyl; The aryl of R ₁ to R ₄ is one or more substituents selected from the group consisting of (C1-C7)alkyl, (C6-C12)aryl, tri(C1-C7)alkylsilyl, and (C1-C7)alkoxy. can be replaced.

The ligand compound according to an embodiment of the present invention may be represented by the following formula (2).

[Formula 2]

[In Formula 2 above,

R ₁₁ to R ₁₄ are independently hydrogen, (C1-C5)alkyl, (C6-C10)aryl, or (C6-C10)aryl(C1-C5)alkyl;

The aryl of R ₁₁ to R ₁₄ may be substituted with one or more substituents selected from the group consisting of (C1-C5)alkyl, tri(C1-C5)alkylsilyl, and (C1-C5)alkoxy.]

In addition, R ₁₁ to R ₁₃ in Formula 2 are independently (C1-C5)alkyl, (C6-C10)aryl, or (C6-C10)aryl(C1-C5)alkyl; R ₁₄ is hydrogen or (C1-C3)alkyl; The aryl of R ₁₁ to R ₁₃ may be substituted with one or more substituents selected from the group consisting of (C1-C5)alkyl, tri(C1-C5)alkylsilyl, and (C1-C5)alkoxy.

Specifically, the ligand compound according to an embodiment of the present invention may be selected from the following compounds.

The present invention provides an ethylene oligomerization catalyst composition including an ethylene oligomerization catalyst and an organic aluminum compound according to an embodiment.

The organic aluminum compounds include methylaluminoxane (MAO), modified methylaluminoxane (MMAO), ethyl aluminoxane (EAO), tetraisobutylaluminoxane (TIBAO), isobutylaluminoxane (IBAO), trimethylaluminum (TMA), Triethylaluminum (TEA), triisobutylaluminum (TIBA), tri-n-octylaluminum, methylaluminum dichloride, ethyl aluminum dichloride, dimethylaluminum chloride, diethylaluminum chloride, aluminum isopropoxide, ethyl aluminum ceth. It may be one or more than one selected from the group consisting of methylaluminum sesquichloride and methylaluminum sesquichloride.

Additionally, the present invention provides a method for producing ethylene oligomer using an ethylene oligomerization catalyst composition according to an embodiment.

The method for producing the ethylene oligomer may be characterized in that 60.0 to 99.999% by weight of 1-hexene is produced based on the total oligomer produced.

In addition, in one embodiment, the method for producing the ethylene oligomer includes benzene, glorobenzene, ethylbenzene, toluene, xylene, cumene, mesitylene, cyclohexane, methylcyclohexane, methylcyclopentane, hexane, heptane, octane, It may be performed in one or more solvents selected from the group consisting of nonane, decane, hexene, heptene, octene, nonene, decene, anisole, ethoxybenzene, and dimethoxybenzene.

The ethylene oligomerization catalyst containing the specific ligand compound of the present invention and the catalyst composition employing the catalyst may exhibit improved selectivity for 1-hexene.

The method for producing ethylene oligomer using the catalyst composition of the present invention exhibits surprisingly excellent selectivity for oligomers and selectivity for 1-hexene even at high temperatures, making it possible to mass-produce 1-hexene, an industrially useful chemical raw material, with high purity. there is.

Hereinafter, the ethylene oligomerization catalyst containing the ligand compound of the present invention, the catalyst composition employing the same, and the method for producing ethylene oligomer using the same will be described in detail.

As used herein, the singular forms “a,” “an,” and “the” are intended to also include the plural forms, unless the context clearly dictates otherwise.

As used in the present invention, “comprises” is an open description with the same meaning as expressions such as “comprises,” “contains,” “has,” or “features,” and includes elements and materials that are not additionally listed. or does not exclude the process.

As used herein, “alkyl” refers to a monovalent straight-chain or branched saturated hydrocarbon radical consisting only of carbon and hydrogen atoms. Examples of such alkyl radicals include methyl, ethyl, propyl, isopropyl, butyl, isobutyl, and t-butyl. , pentyl, hexyl, octyl, nonyl, etc., but is not limited thereto.

“Aryl” as described in the present invention is an organic radical derived from an aromatic hydrocarbon by removal of one hydrogen, and is a single or fused ring system containing suitably 4 to 7 ring atoms, preferably 5 or 6 ring atoms in each ring. It includes a form in which multiple aryls are connected by a single bond. The fused ring system may include an aliphatic ring, such as a saturated or partially saturated ring, and must include at least one aromatic ring. Additionally, the aliphatic ring may contain nitrogen, oxygen, sulfur, carbonyl, etc. in the ring. Specific examples of the aryl radical include phenyl, naphthyl, biphenyl, indenyl, fluorenyl, phenanthrenyl, anthracenyl, triphenylenyl, pyrenyl, chrysenyl, naphthacenyl, 9,10-dihydro. Including, but not limited to, anthracenyl and the like.

As used herein, “cycloalkyl” means a monovalent saturated carbocyclic radical consisting of one or more rings. Examples of cycloalkyl radicals include, but are not limited to, cyclopropyl, cyclobutyl, cyclopentyl, cyclohexyl, cycloheptyl, etc.

“Alkoxy” described in the present invention is -OCH ₃ , -OCH ₂ CH ₃ , -O(CH ₂ ) ₂ CH ₃ , -O(CH ₂ ) ₃ CH ₃ , -O(CH ₂ ) ₄ CH ₃ , -O means -O-(alkyl), including (CH ₂ ) ₅ CH ₃ and the like, where 'alkyl' is as defined above.

“Trialkylsilyl” described in the present invention may be an example of a group in which three hydrogens in a silyl group are each independently substituted with alkyl, where ‘alkyl’ is as defined above. Preferred alkyl to be substituted is alkyl having 1 to 5 carbon atoms, and specific examples include methyl, ethyl, propyl isopropyl, butyl, sce-butyl, tert-butyl, cyclobutyl, etc. More specifically, trialkylsilyl is It may be trimethylsilyl, triethylsilyl, t-butyldimethylsilyl, vinyldimethylsilyl, or propyldimethylsilyl, but is not limited thereto.

As used herein, “halogen” means a fluorine, chlorine, bromine or iodine atom.

“Ethylene oligomerization” described in the present invention is the polymerization of ethylene, and is called trimerization or tetramerization depending on the number of ethylene polymerized. In particular, the present invention refers to producing 1-hexene trimerized with ethylene, which is used as a comonomer of HDPE and LLDPE.

The present invention provides an ethylene oligomerization catalyst comprising a chromium compound and a ligand compound represented by the following formula (1).

[Formula 1]

[In Formula 1 above,

L ₁ and L ₂ are independently (C2-C4)alkylene;

R ₁ to R ₄ are each independently hydrogen, (C1-C10)alkyl, (C3-C20)cycloalkyl, (C6-C20)aryl, (C6-C20)aryl(C1-C10)alkyl, or (C1-C10) ) alkoxy;

The aryl of R ₁ to R ₄ is one or more substituents selected from the group consisting of (C1-C10)alkyl, (C6-C20)aryl, tri(C1-C10)alkylsilyl, and (C1-C10)alkoxy. May be replaced.]

The ethylene oligomerization catalyst of the present invention may be in the form of a complex in which the ligand compound of Formula 1 is coordinated with the chromium compound, which is a chromium source, or may be in the form of a composition containing the chromium compound and the ligand compound of Formula 1.

In one embodiment, the ethylene oligomerization catalyst is (L)CrX ₃ (where L is the ligand compound of Formula 1, and , acetylacetonate, pyrrolide, pyrazolide, imidazolide, 1,2,3-triazolide, tetrazolide or indolide).

The chromium compound may specifically be a chromium trivalent compound, for example, chromium (III) chloride (CrCl ₃ ), chromium (III) acetate (Cr(OAc) ₃ ), chromium (III) 2-ethylhexano. It may be one or more than one selected from the group consisting of ate (Cr(EH) ₃ ), chromium (III) acetylacetonate (Cr(acac) ₃ ), and chromium (III) pyrrolide, but is not limited thereto.

The ethylene oligomerization catalyst of the present invention contains a specific ligand showing the structure of P-N-S, exhibits high activity even at high temperatures, has excellent selectivity for oligomers compared to polymers, and the selectivity of oligomers for 1-hexene is also significantly improved. , 1-hexene can be produced with excellent yield and selectivity.

According to one embodiment, L ₁ and L ₂ of Formula 1 are independently (C2-C3)alkylene; R ₁ to R ₄ are each independently hydrogen, (C1-C7)alkyl, (C3-C12)cycloalkyl, (C6-C12)aryl, (C6-C12)aryl(C1-C7)alkyl, or (C1-C7) ) alkoxy; The aryl of R ₁ to R ₄ is one or more substituents selected from the group consisting of (C1-C7)alkyl, (C6-C12)aryl, tri(C1-C7)alkylsilyl, and (C1-C7)alkoxy. can be replaced.

In detail, L ₁ and L ₂ of Formula 1 are independently (C2-C3)alkylene; R ₁ to R ₄ are independently hydrogen, (C1-C7)alkyl, (C6-C12)aryl, or (C6-C12)aryl(C1-C7)alkyl; The aryl of R ₁ to R ₄ is one or more substituents selected from the group consisting of (C1-C7)alkyl, (C6-C12)aryl, tri(C1-C7)alkylsilyl, and (C1-C7)alkoxy. can be replaced.

In more detail, L ₁ and L ₂ of Formula 1 are independently (C2-C3)alkylene; R ₁ to R ₃ are each independently (C1-C5)alkyl, (C6-C10)aryl, or (C6-C10)aryl(C1-C5)alkyl; R ₁₄ is hydrogen or (C1-C5)alkyl; The aryl of R ₁ to R ₃ is one or more substituents selected from the group consisting of (C1-C5)alkyl, (C6-C10)aryl, tri(C1-C5)alkylsilyl, and (C1-C5)alkoxy. can be replaced.

The ligand compound according to an embodiment of the present invention may be represented by the following formula (2).

[Formula 2]

[In Formula 2 above,

R ₁₁ to R ₁₄ are independently hydrogen, (C1-C5)alkyl, (C6-C10)aryl, or (C6-C10)aryl(C1-C5)alkyl;

The aryl of R ₁₁ to R ₁₄ may be substituted with one or more substituents selected from the group consisting of (C1-C5)alkyl, tri(C1-C5)alkylsilyl, and (C1-C5)alkoxy.]

In addition, R ₁₁ to R ₁₃ in Formula 2 are independently (C1-C5)alkyl, (C6-C10)aryl, or (C6-C10)aryl(C1-C5)alkyl; R ₁₄ is hydrogen or (C1-C3)alkyl; The aryl of R ₁₁ to R ₁₃ may be substituted with one or more substituents selected from the group consisting of (C1-C5)alkyl, tri(C1-C5)alkylsilyl, and (C1-C5)alkoxy.

In Formula 2 according to an embodiment of the present invention, R ₁₁ to R ₁₃ are each independently (C1-C5)alkyl, phenyl, or benzyl; R ₁₄ is hydrogen or methyl; The phenyl and benzyl of R ₁₁ to R ₁₃ may be each independently substituted with one or more substituents selected from the group consisting of (C1-C5)alkyl, tri(C1-C5)alkylsilyl, and (C1-C3)alkoxy. can

The ligand compound according to an embodiment of the present invention may be represented by the following formula (3).

[Formula 3]

[In Formula 3 above,

R ₁₃ is independently (C1-C5) alkyl, phenyl or benzyl, and the phenyl of R ₁₃ is selected from the group consisting of (C1-C5) alkyl, tri (C1-C5) alkylsilyl and (C1-C3) alkoxy. may be substituted with one or two or more substituents selected;

R ₁₄ is hydrogen or methyl;

R ^a and R ^b are independently hydrogen, (C1-C5)alkyl, tri(C1-C5)alkylsilyl, or (C1-C3)alkoxy.]

Specifically, the ligand compound according to an embodiment of the present invention may be selected from the following compounds.

The present invention provides a method for producing the specific ligand compound, and the ligand compound represented by the following formula (1) can be prepared by reacting the compound of the formula (11) and the compound of the formula (12).

[Formula 1]

[Formula 11]

[Formula 12]

[In Formulas 1, 11 and 12,

L ₁ and L ₂ are independently (C2-C4)alkylene;

R ₁ to R ₄ are each independently selected from (C1-C10)alkyl, (C3-C20)cycloalkyl, (C6-C20)aryl, (C6-C20)aryl (C1-C10)alkyl, or (C1-C10)alkoxy. and;

X ₁ is halogen;

The aryl of R ₁ to R ₄ is one or more substituents selected from the group consisting of (C1-C10)alkyl, (C6-C20)aryl, tri(C3-C10)alkylsilyl, and (C1-C10)alkoxy. May be replaced.]

Additionally, the compound represented by Formula 11 can be prepared by reacting the compound of Formula 13 and the compound of Formula 14 below.

[Formula 13]

[Formula 14]

[In Formulas 13 and 14, L ₁ , L ₂ , R ₁ , R ₂ and R ₃ are the same as defined in Formula 1.]

Additionally, the compound represented by Formula 13 can be prepared by reacting the compound of Formula 15 and the compound of Formula 16 below.

[Formula 15]

[Formula 16]

[In Formulas 15 and 16, L ₁ , L ₂ , R ₁ and R ₂ are the same as defined in Formula 1;

X ₂ is halogen.]

The method for producing a ligand compound according to an embodiment of the present invention can easily secure ligands with various substituents and different chemical properties by using raw material compounds whose substituents have been changed during the production process, thereby helping to control and support the activity of the catalyst. It can be advantageous.

The present invention provides an ethylene oligomerization catalyst composition including an ethylene oligomerization catalyst and an organic aluminum compound according to an embodiment.

The ethylene oligomerization catalyst composition employing the ethylene oligomerization catalyst of the present invention exhibits excellent catalytic activity and very high selectivity for 1-hexene even at high reaction temperatures, and can efficiently produce 1-hexene, which is industrially useful as a chemical raw material.

The organoaluminum compound is a compound of AlR ₃ (wherein R is each independently C1-C12 alkyl, C6-C20 aryl, C2-C10 alkenyl, C2-C10 alkynyl, C1-C12 alkoxy or halogen). You can. Specifically, the organic aluminum compounds include methylaluminoxane (MAO), modified methylaluminoxane (MMAO), ethyl aluminoxane (EAO), tetraisobutylaluminoxane (TIBAO), isobutylaluminoxane (IBAO), and trimethylaluminoxane (TMA). ), triethyl aluminum (TEA), triisobutyl aluminum (TIBA), tri-n-octyl aluminum, methyl aluminum dichloride, ethyl aluminum dichloride, dimethyl aluminum chloride, diethylaluminum chloride, aluminum isopropoxide, ethyl It may be one or more than one selected from the group consisting of aluminum sesquichloride and methylaluminum sesquichloride, but is not limited thereto.

In one embodiment of the present invention, the ratio of the ethylene oligomerization catalyst and the organoaluminum compound may be expressed as a molar ratio of chromium in the ethylene oligomerization catalyst to aluminum in the organoaluminum compound, and may be 1:1 to 10,000, preferably. It may be 1:1 to 2,000, and more preferably 1:1 to 1,000.

The individual components of the ethylene oligomerization catalyst composition may be blended simultaneously in the presence of a solvent or sequentially in any order. The mixing may be carried out at -20 to 250°C, preferably at 20 to 160°C.

The ethylene oligomerization catalyst composition according to an embodiment of the present invention has very high catalytic activity and selectivity for 1-hexene, the amount of catalyst input can be adjusted, and further, excellent activity is maintained even at high temperatures, eliminating problems in the olefin production process. It is very economical and efficient as it does not cause pipe clogging or fouling.

Additionally, the present invention provides a method for producing ethylene oligomer using an ethylene oligomerization catalyst composition according to an embodiment.

A method for producing ethylene oligomer according to an embodiment includes a homogeneous liquid phase reaction, a two-phase liquid/liquid reaction, and a bulk reaction in which the product acts as the main medium in the presence of an inert solvent using the oligomerization catalyst composition and conventional equipment and contact technology. It may be prepared by a phase reaction or a gas phase reaction, but is preferably a homogeneous liquid phase reaction in the presence of an inert solvent.

The polymer of the product prepared by the above ethylene oligomer production method may be 0.001% by weight or more, 0.01% by weight or more, or 0.1% by weight or more, 40.0% by weight or less, 30.0% by weight or less, or 20.0% by weight or less, e.g. For example, it may be 0.001 to 30.0% by weight, specifically 0.01 to 30.0% by weight, and more specifically 0.1 to 20.0% by weight.

The oligomer of the product prepared by the above ethylene oligomer production method may be 60.0% by weight or more, 70.0% by weight or more, 80.0% by weight or more, 99.999% by weight or less, 99.99% by weight or less, or 99.9% by weight or less, for example For example, it may be 70.0 to 99.999% by weight, specifically 70.0 to 99.99% by weight, and more specifically 80.0 to 99.9% by weight.

In addition, in the above production method, 1-hexene may be 60.0% by weight or more, 70.0% by weight, 80.0% by weight or more, 90.0% by weight or more, 99.999% by weight or less, 99.99% by weight or less, or 99.9% by weight or less, e.g. For example, it may be 60.0 to 99.999% by weight, specifically 65.0 to 99.99% by weight, more specifically 70.0 to 99.9% by weight, and even more specifically 80 to 99.9% by weight.

The method for producing ethylene oligomer using the catalyst composition of the present invention exhibits surprisingly excellent selectivity for oligomers and selectivity for 1-hexene even at high temperatures, enabling mass production of 1-hexene, an industrially useful chemical raw material, with high purity. .

In addition, in one embodiment, the method for producing the ethylene oligomer includes aromatic hydrocarbons such as benzene, glorobenzene, ethylbenzene, toluene, xylene, cumene, mesitylene, etc.; Cyclic aliphatic hydrocarbons such as cyclohexane, methylcyclohexane, methylcyclopentane, etc.; aliphatic hydrocarbons such as hexane, heptane, octane, nonane, decane, etc.; olefins such as hexene, heptene, octene, nonene, decene, etc.; and aromatic ethers such as anisole, ethoxybenzene, dimethoxybenzene, etc.; and may be performed in one or more solvents selected from the group consisting of. Specifically, it may be toluene, xylene, nonane, hexane, or a mixture thereof, and more specifically, it may be toluene, nonane, or a mixture thereof.

The oligomerization reaction according to an embodiment of the present invention may be performed at -20 to 250 °C, preferably 20 to 160 °C, and more preferably 60 to 120 °C.

Additionally, the oligomerization reaction may be performed at a pressure of 1 to 100 bar, preferably at a pressure of 5 to 70 bar, and more preferably at a pressure of 10 to 40 bar.

The method for producing ethylene oligomer according to one embodiment of the present invention can be performed in a plant including any type of reactor. The reactor may be, for example, a batch type, a semi-batch type, and a continuous type, but is not limited thereto. The plant may include a combination of a reactor, an olefin reactor inside the reactor and an inlet of the oligomerization catalyst composition, a line for discharging the oligomerization reaction product from the reactor, and one or more separators for separating the oligomerization reaction product. there is.

Hereinafter, the ethylene oligomerization catalyst containing the ligand compound according to the present invention, the catalyst composition employing the same, and the method for producing ethylene oligomer using the same will be described in more detail through specific examples.

[Preparation Example A] Preparation of Compound A

Add Compound A-2 (3.82 mL, 22 mmol) and 20 mL of dried THF to a flask dried under a nitrogen atmosphere, cool to 5°C, and then slowly add 2.5 M n-BuLi in Hex (8.8 ml, 22 mmol). Added. Stir at room temperature for 20 minutes and then cool to -78°C. Compound A-1 (3.0 g, 20 mmol) and 30 mL of dried THF were mixed at -78°C, and the mixed solution was slowly added over 1 hour. 100 mL of toluene and 25 mL of water were added at room temperature, and then distilled under reduced pressure. The organic layer was washed with water, moisture was removed with MgSO ₄ , recrystallized with 2-methyl-2-butanol, and dried in vacuum to obtain Compound A (yield 51%).

¹ H NMR (CDCl ₃ , 500 MHz) δ 7.50 - 7.28 (m, 10H), 4.23 - 4.19 (m, 2H), 3.56 - 3.43 (m, 4H), 2.39 - 2.35 (m, 2H)

[Preparation Example B] Preparation of Compound B

Compound B was obtained in the same manner as Preparation Example A, except that Compound B-1 was used instead of Compound A-2 (yield 54%).

^1H NMR (CDCl ₃ , 500 MHz) δ 7.38 - 7.34 (m, 4H), 6.88 (d, 4H, J = 7.8 Hz), 4.18 (t, 2H, J = 8.0 Hz), 3.79 (s, 6H) , 3.50 (t, 2H, J = 8.2 Hz), 3.41 - 3.36 (m, 2H), 2.26 (t, 2H, J = 7.6 Hz)

[Preparation Example C] Preparation of Compound C

Compound C was obtained in the same manner as Preparation Example A, except that Compound C-1 was used instead of Compound A-2 (yield 41%).

^1H NMR (CDCl ₃ , 500 MHz) δ 7.34 - 7.31 (m, 4H), 7.16 (d, 4H, J = 7.6 Hz), 4.18 (t, 2H, J = 8.1 Hz), 3.51 (t, 2H, J = 7.8 Hz), 3.43 - 3.38 (m, 2H), 2.34 (s, 6H), 2.30 (t, 2H, J = 7.4 Hz)

[Preparation Example 1] Preparation of Ligand Compound 1

Add Compound A (Preparation A (2.99 g, 10 mmol)), NaS-Me (0.70 g, 10 mmol), Et ₃ N (1.39 mL, 10 mmol), and 20 mL of 2-methyl-2-butanol to the flask. Refluxed for 3 hours. The reaction product was distilled under reduced pressure and purified by column to obtain Ligand Compound 1 (yield 67%).

¹ H NMR (CDCl ₃ , 500 MHz) δ 7.45 - 7.41 (m, 4H), 7.34 - 7.32 (m, 6H), 2.80 - 2.74 (m, 4H), 2.61 (t, 2H, J = 6.6 Hz), 2.28 (t, 2H, J = 7.5 Hz), 2.08 (s, 3H), 1.57 (br, 1H)

[Preparation Example 2] Ligand Compound 2

The Ligand Compound 2 was purchased and used from Strem.

[Preparation Example 3] Ligand Compound 3

The Ligand Compound 3 was purchased and used from Strem.

[Preparation Example 4] Ligand Compound 4

The ligand compound 4 was purchased and used from Strem.

[Preparation Example 5] Preparation of Ligand Compound 5

Ligand Compound 5 was obtained in the same manner as Preparation Example 1, except that Compound B (Preparation Example B) was used instead of Compound A (Preparation Example A) in Preparation Example 1 (yield 17%).

¹ H NMR (CDCl ₃ , 500 MHz) δ 7.37 - 7.34 (m, 4H), 6.87 (d, 4H, J = 8.9 Hz), 3.80 (s, 6H), 2.79 (t, 2H, J = 6.5 Hz) , 2.77-2.72 (m, 2H), 2.61 (t, 2H, 6.6 Hz), 2.21 (t, 2H, 7.2 Hz), 2.01 (s, 3H), 1.72 (br, 1H)

[Preparation Example 6] Preparation of Ligand Compound 6

Ligand Compound 6 was obtained in the same manner as Preparation Example 1, except that Compound C (Preparation Example C) was used instead of Compound A (Preparation Example A) in Preparation Example 1 (yield 32%).

^1H NMR (CDCl ₃ , 500 MHz) δ 7.32 (t, 4H, J = 7.6 Hz), 7.14 (d, 4H, J = 7.6 Hz), 2.81-2.74 (m, 4H), 2.62 (t, 2H, J = 6.6 Hz), 2.33 (s, 6H), 2.26 (t, 2H, 7.4 Hz), 2.17 (br, 1H), 2.07 (s, 3H)

[Preparation Example 7] Preparation of Ligand Compound 7

Ligand Compound 1 (Preparation Example 1 (151 mg, 0.5 mmol)) and HCHO (30 mg, 1.0 mmol) were dissolved in 1.2 mL of dichloromethane in a flask and stirred for 15 minutes. NaBH(OAc) ₃ (212 mg, 1.0 mmol) was slowly added and refluxed for 24 hours. The reaction product was distilled under reduced pressure and purified by column to obtain Ligand Compound 7 (yield 48%).

¹ H NMR (CDCl ₃ , 500 MHz) δ 7.45 - 7.41 (m, 4H), 7.35 - 7.31 (m, 6H), 2.80 - 2.60 - 2.50 (m, 6H), 2.27 (s, 3H), 2.26-2.22 (m, 2H), 2.09 (s, 3H)

[Comparative Preparation Example 1] Preparation of Ligand Compound 8

The ligand compound 8 was prepared with reference to a known document (Organometallics 2001, 20, 4769-4771).

[Example 1] Preparation of oligomerization catalyst 1

Chromium (III) acetylacetonate (Cr(acac) ₃ ) (175 mg, 0.52 mmol) and 1.04 equiv. of Ligand Compound 1 (Preparation Example 1) were dissolved in 5 mL of Toluene and stirred for 20 minutes. The filtered liquid was vacuum dried using a 0.45 μm syringe filter, and then a solid was obtained, which was then vacuum dried to obtain a solid (yield 85%).

^1H NMR (C ₆ D ₆ , 500 MHz) δ 3.58 (br), 1.41 (br)

[Example 2] Preparation of oligomerization catalyst 2

Chromium (III) chloride tetrahydrofuran (CrCl ₃ (THF) ₃ ) (276 mg, 0.52 mmol) and 1.04 equiv. of Ligand Compound 1 (Preparation Example 1) were dissolved in 5 mL of Tetrahydrofuran and stirred for 20 minutes. The formed precipitate was filtered using a filter, and the solid was washed with diethyl ether and vacuum dried (yield 99%).

¹ H NMR (DMSO, 500 MHz) δ 8.84 (br), 5.06 (br), 3.97 (br), 2.07 (br)

[Example 3]

Chromium (III) acetylacetonate (Cr(acac) ₃ ) (6.99 mg, 20 μmol) and 1.2 equiv. of Ligand Compound 1 (Preparation Example 1) were dissolved in 4.12 mL of toluene and stirred for 10 minutes.

The stirred dispersion mixture in the glove box was introduced into a 20 mL autoclave reactor cleaned with nitrogen and vacuum. 0.86 mL (2 mmol, 100 equiv. of chromium catalyst) of MMAO-12 (10% in Toluene, Aldrich) and 20 μL of nonane were added and stirred at 800 rpm. The temperature in the autoclave reactor was raised to 50°C, and then ethylene was charged at 20 bar to perform an oligomerization reaction for 30 minutes. After completion of the reaction, excess ethylene in the reactor was discharged, the reactor was cooled to below 10°C, the reactant was discharged into a discharge container containing 2.5 mL of methanol, and a small amount of the organic layer sample was analyzed by GC-FID. The remaining organic layer was filtered to separate the solid wax and polymer product. The solid product was oven dried and its weight was measured. The product of Example 3 analyzed by GC is shown in Table 2.

[Examples 4 to 10]

Under the conditions shown in Table 1 below, the results of GC analysis of the products of Examples 4 to 10 were conducted in the same manner as Example 3, except that the temperature, pressure, number of moles of catalyst, and MMAO equivalent to the catalyst were different. It is shown in Table 2.

Cr(acac) ₃
(μmol) Ligand Compound 1 (Preparation Example 1) (equiv.) MMAO (equiv.) Pressure
(bar) Temperature
(℃) Example 3 20 1.2 100 20 (closed) 50 Example 4 20 1.2 100 20 (flow) 70 Example 5 20 1.2 100 20 (flow) 100 Example 6 10 1.2 100 20 (flow) 100 Example 7 2 1.2 100 20 (flow) 100 Example 8 0.1 1.2 100 20 (flow) 100 Example 9 2 1.2 100 30 (flow) 100 Example 10 2 1.2 300 20 (flow) 100

Activity(g/g-Cr/h)
for oligomers Selectivity(%) in Oligomer 1-Hexene 1-Octene etc Example 3 179.7 92.4 5.2 2.4 Example 4 525.4 96.6 0.5 2.9 Example 5 803.4 94.1 1.3 4.6 Example 6 2135.2 93.7 1.3 5.0 Example 7 10934.3 96.8 0.2 3.0 Example 8 1322.8 80.1 - 19.9 Example 9 5995.1 97.0 0.3 2.7 Example 10 11820.2 95.5 1.3 3.2

As shown in Table 2, it can be seen that the oligomerization of ethylene using Ligand Compound 1 (Preparation Example 1) shows excellent selectivity for 1-hexene, and the catalyst activity is very high even at a high temperature of 100 ° C. You can check it. Among Examples 3 to 10, the conditions of Example 7, in which the catalytic activity was very excellent even though a small amount of chromium compound was used, were adopted to determine the catalytic activity of oligomerization, selectivity to oligomers, and 1-hexene according to changes in the ligand compound. Selectivity was confirmed in the examples below.

[Example 11]

Chromium (III) acetylacetonate (Cr(acac) ₃ ) (0.7 mg, 2 μmol) and 1.2 equiv. of Ligand Compound 1 (Preparation Example 1) were dissolved in 4.12 mL of toluene and stirred for 10 minutes.

The stirred dispersion mixture in the glove box was introduced into a 20 mL autoclave reactor cleaned with nitrogen and vacuum. 0.86 mL (2 mmol, 100 equiv. of chromium catalyst) of MMAO-12 (10% in Toluene, Aldrich) and 20 μL of nonane were added and stirred at 800 rpm. The temperature in the autoclave reactor was raised to 100°C, and then ethylene was charged at 20 bar to perform an oligomerization reaction for 30 minutes. After completion of the reaction, excess ethylene in the reactor was discharged, the reactor was cooled to below 10°C, the reactant was discharged into a discharge container containing 2.5 mL of methanol, and a small amount of the organic layer sample was analyzed by GC-FID. The remaining organic layer was filtered to separate the solid wax and polymer product. The solid product was oven dried and its weight was measured. The results of GC analysis of the product of Example 11 are shown in Table 3.

[Examples 12 to 17]

Examples 12 to 17 were carried out in the same manner as Example 11, except that Ligand Compounds 2 to 6 (Preparation Examples 2 to 6) were used instead of Ligand Compound 1 (Preparation Example 1). The results of GC analysis of the product are shown in Table 3.

[Example 18]

Example 1 (oligomerization catalyst 1) (1.2 mg, 2 μmol) was dissolved in 4.12 mL of toluene and stirred for 10 minutes.

The stirred dispersion mixture in the glove box was introduced into a 20 mL autoclave reactor cleaned with nitrogen and vacuum. 0.86 mL (2 mmol, 100 equiv. of chromium catalyst) of MMAO-12 (10% in Toluene, Aldrich) and 20 μL of nonane were added and stirred at 800 rpm. The temperature in the autoclave reactor was raised to 100°C, and then ethylene was charged at 20 bar to perform an oligomerization reaction for 30 minutes. After completion of the reaction, excess ethylene in the reactor was discharged, the reactor was cooled to below 10°C, the reactant was discharged into a discharge container containing 2.5 mL of methanol, and a small amount of the organic layer sample was analyzed by GC-FID. The remaining organic layer was filtered to separate the solid wax and polymer product. The solid product was oven dried and its weight was measured. The results of GC analysis of the product of Example 18 are shown in Table 3.

[Example 19]

Example 2 (oligomerization catalyst 2) (0.9 mg, 2 μmol) was dissolved in 4.12 mL of toluene and stirred for 10 minutes.

The stirred dispersion mixture in the glove box was introduced into a 20 mL autoclave reactor cleaned with nitrogen and vacuum. 0.86 mL (2 mmol, 100 equiv. of chromium catalyst) of MMAO-12 (10% in Toluene, Aldrich) and 20 μL of nonane were added and stirred at 800 rpm. The temperature in the autoclave reactor was raised to 100°C, and then ethylene was charged at 20 bar to perform an oligomerization reaction for 30 minutes. After completion of the reaction, excess ethylene in the reactor was discharged, the reactor was cooled to below 10°C, the reactant was discharged into a discharge container containing 2.5 mL of methanol, and a small amount of the organic layer sample was analyzed by GC-FID. The remaining organic layer was filtered to separate the solid wax and polymer product. The solid product was oven dried and its weight was measured. The results of GC analysis of the product of Example 19 are shown in Table 3.

[Comparative Example 1]

Table 3 shows the results of GC analysis of the product in the same manner as in Example 11, except that Ligand Compound 8 (Comparative Preparation Example 1) was used instead of Ligand Compound 1 (Preparation Example 1) in Example 11. shown in

chrome
compound Ligand
compound Activity
(g/g-Cr/h)
for oligomers Selectivity(%) Selectivity in Oligomer(%) Polymer Oligomer 1-Hexene 1-Octene etc Example 11 Cr(acac) ₃ One 10934.3 1.9 98.1 96.8 0.2 3.0 Example 12 Cr(acac) ₃ 2 786.1 11.3 88.7 91.0 4.0 5.0 Example 13 Cr(acac) ₃ 3 95.4 19.5 80.5 74.9 3.2 21.9 Example 14 Cr(acac) ₃ 4 55.7 29.0 71.0 74.5 - 25.5 Example 15 Cr(acac) ₃ 5 6060.0 5.4 94.6 96.2 0.5 3.3 Example 16 Cr(acac) ₃ 6 11130.5 1.2 98.8 96.2 0.3 3.5 Example 17 Cr(acac) ₃ 7 3471.9 7.7 92.3 95.1 0.7 4.2 Example 18 Example 1
(Oligomerization catalyst 1) 1376.0 18.6 81.4 63.0 7.9 29.1 Example 19 Example 2
(Oligomerization catalyst 2) 1924.0 2.9 97.1 98.6 0.2 1.2 Comparative Example 1 Cr(acac) ₃ 8 2910.5 85.2 14.8 71.2 2.9 25.9

As shown in Table 3, the selectivity for oligomers in Examples 11 to 17 using Ligand Compounds 1 to 7 of the present invention was more than 70%, and the oligomer selectivity of Comparative Example 1 using Ligand Compound 8, which was previously used, was 14.8%. Compared to , it can be seen that the examples of the present invention exhibit significantly superior selectivity, and in particular, examples 11 and 16 exhibit very excellent selectivity for oligomers of over 98%.

In addition, the examples of the present invention had excellent selectivity for 1-hexene, and in particular, Examples 11, 12, 15, 16, 17, and 19 were confirmed to have surprisingly improved selectivity for 1-hexene of more than 90%. It can be confirmed that the oligomerization catalyst and catalyst composition containing the ligand compound of the invention are very efficient in producing 1-hexene.

The oligomerization catalyst of the present invention maintains catalytic activity and selectivity even at high temperatures, has no problems with tube clogging and fouling due to low production of by-products, and is very economical because it does not require interruption of the polymerization process to remove them. Furthermore, the oligomerization catalyst of the present invention has excellent catalytic activity even at high temperatures, allowing oligomers to be produced with only a small amount of catalyst and a small amount of organoaluminum compounds. The activity does not decrease even at high temperatures and the selectivity is excellent, so that 1 -Hexene can be produced with surprisingly excellent selectivity.

As described above, the present invention has been described with specific details and limited examples and comparative examples, but these are provided only to facilitate a more general understanding of the present invention, and the present invention is not limited to the above examples. Those skilled in the art can make various modifications and variations from this description.

Accordingly, the spirit of the present invention should not be limited to the described embodiments, and the scope of the patent claims described below as well as all modifications that are equivalent or equivalent to the scope of this patent claim shall fall within the scope of the spirit of the present invention. .

Claims (11)

An ethylene oligomerization catalyst comprising a chromium compound and a ligand compound represented by the following formula (1).
[Formula 1]

[In Formula 1 above,
L ₁ and L ₂ are independently (C2-C4)alkylene;
R ₁ to R ₄ are each independently hydrogen, (C1-C10)alkyl, (C3-C20)cycloalkyl, (C6-C20)aryl, (C6-C20)aryl(C1-C10)alkyl, or (C1-C10) ) alkoxy;
The aryl of R ₁ to R ₄ is one or more substituents selected from the group consisting of (C1-C10)alkyl, (C6-C20)aryl, tri(C1-C10)alkylsilyl, and (C1-C10)alkoxy. May be replaced.] According to paragraph 1,
In Formula 1, L ₁ and L ₂ are independently (C2-C3)alkylene;
R ₁ to R ₄ are each independently hydrogen, (C1-C7)alkyl, (C3-C12)cycloalkyl, (C6-C12)aryl, (C6-C12)aryl(C1-C7)alkyl, or (C1-C7) ) alkoxy;
The aryl of R ₁ to R ₄ is one or more substituents selected from the group consisting of (C1-C7)alkyl, (C6-C12)aryl, tri(C1-C7)alkylsilyl, and (C1-C7)alkoxy. Ethylene oligomerization catalyst, which may be substituted. According to paragraph 1,
In Formula 1, L ₁ and L ₂ are independently (C2-C3)alkylene;
R ₁ to R ₄ are independently hydrogen, (C1-C7)alkyl, (C6-C12)aryl, or (C6-C12)aryl(C1-C7)alkyl;
The aryl of R ₁ to R ₄ is one or more substituents selected from the group consisting of (C1-C7)alkyl, (C6-C12)aryl, tri(C1-C7)alkylsilyl, and (C1-C7)alkoxy. Ethylene oligomerization catalyst, which may be substituted. According to paragraph 1,
An ethylene oligomerization catalyst wherein the ligand compound is represented by the following formula (2).
[Formula 2]

[In Formula 2 above,
R ₁₁ to R ₁₄ are independently hydrogen, (C1-C5)alkyl, (C6-C10)aryl, or (C6-C10)aryl(C1-C5)alkyl;
The aryl of R ₁₁ to R ₁₄ may be substituted with one or more substituents selected from the group consisting of (C1-C5)alkyl, tri(C1-C5)alkylsilyl, and (C1-C5)alkoxy.] According to paragraph 4,
R ₁₁ to R ₁₃ in Formula 2 are independently (C1-C5)alkyl, (C6-C10)aryl, or (C6-C10)aryl(C1-C5)alkyl;
R ₁₄ is hydrogen or (C1-C3)alkyl;
The aryl of R ₁₁ to R ₁₃ is an ethylene oligomer that may be substituted with one or more substituents selected from the group consisting of (C1-C5) alkyl, tri(C1-C5) alkylsilyl, and (C1-C5) alkoxy. fire catalyst. According to paragraph 1,
The ethylene oligomerization catalyst wherein the ligand compound is selected from the following compounds.

An ethylene oligomerization catalyst composition comprising the ethylene oligomerization catalyst according to any one of claims 1 to 6 and an organic aluminum compound. In clause 7,
The organic aluminum compounds include methylaluminoxane (MAO), modified methylaluminoxane (MMAO), ethyl aluminoxane (EAO), tetraisobutylaluminoxane (TIBAO), isobutylaluminoxane (IBAO), trimethylaluminum (TMA), Triethylaluminum (TEA), triisobutylaluminum (TIBA), tri-n-octylaluminum, methylaluminum dichloride, ethyl aluminum dichloride, dimethylaluminum chloride, diethylaluminum chloride, aluminum isopropoxide, ethyl aluminum ceth. An ethylene oligomerization catalyst composition comprising one or more selected from the group consisting of methylaluminum sesquichloride and methylaluminum sesquichloride. A method for producing ethylene oligomers using the ethylene oligomerization catalyst composition according to claim 7. According to clause 9,
The method for producing an ethylene oligomer is characterized in that 60.0 to 99.999% by weight of 1-hexene is produced based on the total oligomer. According to clause 9,
The method for producing the ethylene oligomer is benzene, glorobenzene, ethylbenzene, toluene, xylene, cumene, mesitylene, cyclohexane, methylcyclohexane, methylcyclopentane, hexane, heptane, octane, nonane, decane, hexene, and heptene. A method for producing an ethylene oligomer, which is carried out under one or two or more solvents selected from the group consisting of octene, nonene, decene, anisole, ethoxybenzene, and dimethoxybenzene.