WO2001068572A1 - Process for the preparation of 1-hexene - Google Patents

Process for the preparation of 1-hexene Download PDF

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Publication number
WO2001068572A1
WO2001068572A1 PCT/EP2001/002827 EP0102827W WO0168572A1 WO 2001068572 A1 WO2001068572 A1 WO 2001068572A1 EP 0102827 W EP0102827 W EP 0102827W WO 0168572 A1 WO0168572 A1 WO 0168572A1
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Prior art keywords
hexene
preparation
carried out
previous
reaction
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PCT/EP2001/002827
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French (fr)
Inventor
Roberto Santi
Anna Maria Romano
Manuela Grande
Anna Sommazzi
Francesco Masi
Antonio Proto
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Enichem S.P.A.
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Priority to EP01911764A priority Critical patent/EP1178949B1/en
Priority to US09/926,555 priority patent/US6459007B1/en
Priority to CA2373406A priority patent/CA2373406C/en
Priority to DE60100252T priority patent/DE60100252T2/en
Priority to AU40695/01A priority patent/AU4069501A/en
Priority to AT01911764T priority patent/ATE239682T1/en
Publication of WO2001068572A1 publication Critical patent/WO2001068572A1/en
Priority to HK02105939.1A priority patent/HK1045981B/en

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    • C—CHEMISTRY; METALLURGY
    • C07—ORGANIC CHEMISTRY
    • C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C2/00—Preparation of hydrocarbons from hydrocarbons containing a smaller number of carbon atoms
    • C07C2/02—Preparation of hydrocarbons from hydrocarbons containing a smaller number of carbon atoms by addition between unsaturated hydrocarbons
    • C07C2/04—Preparation of hydrocarbons from hydrocarbons containing a smaller number of carbon atoms by addition between unsaturated hydrocarbons by oligomerisation of well-defined unsaturated hydrocarbons without ring formation
    • C07C2/06—Preparation of hydrocarbons from hydrocarbons containing a smaller number of carbon atoms by addition between unsaturated hydrocarbons by oligomerisation of well-defined unsaturated hydrocarbons without ring formation of alkenes, i.e. acyclic hydrocarbons having only one carbon-to-carbon double bond
    • C07C2/08—Catalytic processes
    • C07C2/26—Catalytic processes with hydrides or organic compounds
    • C07C2/32—Catalytic processes with hydrides or organic compounds as complexes, e.g. acetyl-acetonates
    • C—CHEMISTRY; METALLURGY
    • C07—ORGANIC CHEMISTRY
    • C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C2531/00—Catalysts comprising hydrides, coordination complexes or organic compounds
    • C07C2531/16—Catalysts comprising hydrides, coordination complexes or organic compounds containing coordination complexes
    • C07C2531/22—Organic complexes

Definitions

  • the present invention relates to a process for the preparation of 1-hexene by the oligomeri- zation of ethylene in the presence of vanadium complexes with a low oxidation state.
  • the object of the invention therefore relates to a process for the preparation of 1-hexene which consists in subjecting ethylene to oli- gomerization in the presence of a catalyst comprising a vanadium complex with a low oxidation state selected from those included in the following formula: (arene) 2 VX wherein the term arene represents benzene or mono-, di-, or tri-alkylsubstituted benzene, V is a vanadium ion with a low oxidation state, and X is an anion such as Cl, Br, I, non-coordinated anions such as B(Ar) 4 ⁇ , A1C14-, carboxylates, sul- fonates.
  • Vanadium arenes are already known in the art and can be prepared for example according to the indications, which form an integral part of the present invention, contained in the articles of
  • these vanadium complexes can be used for the oligomerization of olefins other than ethylene, such as, for exam- pie, propylene, 1-butene, etc.: the reason the Applicant has decided to limit the description of the invention to the preparation of 1-hexene alone is simply because of the specific industrial interest in the production of this com- pound: any expert in the field will be able to understand from this description how to effect the oligomerization reaction starting from olefins other than ethylene, this process being included, however, in the scope of the invention according to the present patent application.
  • the oligomerization reaction of ethylene is carried out in the absence of co-catalysts, in the presence of the above vanadium compound alone or in the presence of the vanadium compound and a heterocyclic compound selected from pyrrole and derivatives .
  • heterocyclic compound When this heterocyclic compound is adopted, it is used in a ratio, with respect to the vana- dium complex, ranging from 1 to 20: heterocyclic compounds which can be advantageously used are pyrroles, pyrazoles, phenanthroline, pyridine and other mono and polynitrogenated derivatives .
  • the oligomerization reaction of ethylene is carried out in the presence of a solvent which is normally selected from aromatic hydrocarbons and cy- cloaliphatic hydrocarbons: of these, the use of toluene and cyclohexane has proved to be particu- larly advantageous.
  • the reaction is carried out at a temperature ranging from 0 to 150°C, preferably from 25 to 60°C, and at a pressure ranging from 1 to 100 atm. , preferably from 1 to 50 atmospheres.
  • the reaction time is normally less than 36 hours, preferably from 1 to 24 hours.
  • 1-hexene can be separated and recovered from the reaction mixture using techniques well known to experts in the field. Further details are evident from the following operative examples which are provided for a better illustration of the present invention without limiting its scope however in any way. Table I
  • the orange solution is charged into a Buchi 300 ml glass autoclave, put under 7 bars of ethylene and maintained at room temperature for 1 hour.
  • the autoclave is degassed and the contents discharged without diluting.
  • 1 ml of the solution is re- moved, 1 ml of a solution of Br 2 in CC1 is added and injected into GC: no olefins are present.
  • Activity 0 moles of ethylene/V mole Selectivity: 0% to 1-hexene OLIGOMERIZATION TESTS OF ETHYLENE CATALYZED BY V(I)

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  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
  • Low-Molecular Organic Synthesis Reactions Using Catalysts (AREA)
  • Catalysts (AREA)
  • Transition And Organic Metals Composition Catalysts For Addition Polymerization (AREA)
  • Encapsulation Of And Coatings For Semiconductor Or Solid State Devices (AREA)

Abstract

Process for the preparation of 1-hexene consisting in effecting the oligomerization of ethylene in the presence of a catalyst comprising a vanadium complex having the formula: (arene)2VX wherein the term arene represents benzene or mono-, di-, or tri-alkylsubstituted benzene, V is a vanadium ion with a low oxidation state, and X is an anion selected from Cl, Br and I halide ions, or from non-coordinated anions such as B(Ar)4-, AlCl¿4?-, carboxylates and sulfonates.

Description

PROCESS FOR THE PREP7ARATION OF 1-HEXENE
The present invention relates to a process for the preparation of 1-hexene by the oligomeri- zation of ethylene in the presence of vanadium complexes with a low oxidation state.
The possibility of preparing olefins with a double terminal bond by means of the oligomerization of lower olefins, for example 1-hexene by the trimerization of ethylene, is already known: for example United States patent 4,668,838 describes a process involving the use of a catalyst which comprises the reaction product between a chromium compound, a hydrocarbon derivative of partially hydrolyzed aluminum and a ligand-donor compound; European patent application 416,304 involves, in the process in question, the use of a catalytic system comprising a pyrrolidic compound of chromium and a compound of aluminum; European patent application 537,609 relates to the process of interest which is carried out in the presence of a catalyst consisting of a complex of chromium with a polydentate ligand and an aluminoxane.
In addition to the above references, others can be cited relating to the use of catalytic systems based on compounds of chromium; preparation processes of 1-hexene by the oligomerization of ethylene in the presence of these catalytic systems, however, seem to have various drawbacks such as, for example, insufficient activity of the catalyst or difficulty in its preparation or the low selectivity with respect to the desired product .
The Applicant has now found that it is pos- sible to effect the synthesis of 1-hexene by the oligomerization of ethylene using a process which overcomes all the disadvantages which negatively characterize analogous processes described in the state of the art above, and which consequently seem to have all the necessary industrial requisites.
The object of the invention, according to the present patent application, therefore relates to a process for the preparation of 1-hexene which consists in subjecting ethylene to oli- gomerization in the presence of a catalyst comprising a vanadium complex with a low oxidation state selected from those included in the following formula: (arene) 2VX wherein the term arene represents benzene or mono-, di-, or tri-alkylsubstituted benzene, V is a vanadium ion with a low oxidation state, and X is an anion such as Cl, Br, I, non-coordinated anions such as B(Ar)4 ~, A1C14-, carboxylates, sul- fonates.
The following complexes have proved to be particularly advantageous: bis- (mesitylene) -vanadium trifluoroacetate bis- (mesitylene) -vanadium-tetraphenylborate bis- (mesitylene) -vanadium-iodide bis- (mesitylene) -vanadium-tetrachloroaluminate.
Vanadium arenes are already known in the art and can be prepared for example according to the indications, which form an integral part of the present invention, contained in the articles of
E.O. Fischer and U.S. Kogler, Chem. Ber. 90, 250
(1957), and F. Calderazzo, Inorg. Chem., _3, 810
(1964) : for example according to the schemes of Table 1. In accordance with a wider aspect of the process of the present invention, these vanadium complexes can be used for the oligomerization of olefins other than ethylene, such as, for exam- pie, propylene, 1-butene, etc.: the reason the Applicant has decided to limit the description of the invention to the preparation of 1-hexene alone is simply because of the specific industrial interest in the production of this com- pound: any expert in the field will be able to understand from this description how to effect the oligomerization reaction starting from olefins other than ethylene, this process being included, however, in the scope of the invention according to the present patent application.
The oligomerization reaction of ethylene, according to the process of the present invention is carried out in the absence of co-catalysts, in the presence of the above vanadium compound alone or in the presence of the vanadium compound and a heterocyclic compound selected from pyrrole and derivatives .
When this heterocyclic compound is adopted, it is used in a ratio, with respect to the vana- dium complex, ranging from 1 to 20: heterocyclic compounds which can be advantageously used are pyrroles, pyrazoles, phenanthroline, pyridine and other mono and polynitrogenated derivatives .
The oligomerization reaction of ethylene, according to the present invention, is carried out in the presence of a solvent which is normally selected from aromatic hydrocarbons and cy- cloaliphatic hydrocarbons: of these, the use of toluene and cyclohexane has proved to be particu- larly advantageous.
The reaction is carried out at a temperature ranging from 0 to 150°C, preferably from 25 to 60°C, and at a pressure ranging from 1 to 100 atm. , preferably from 1 to 50 atmospheres. The reaction time is normally less than 36 hours, preferably from 1 to 24 hours. At the end of the reaction, 1-hexene can be separated and recovered from the reaction mixture using techniques well known to experts in the field. Further details are evident from the following operative examples which are provided for a better illustration of the present invention without limiting its scope however in any way. Table I
VANADIUM COMPLEXES
OCOCF3
BAr4 X + Cp2Fe
Figure imgf000007_0001
Example 1: Synthesis of V(mes)2(OCOCF3)
1.723 g of N(mes)2 (5.9[mmoles) and 50 ml of anhydrous and degassed n-hexane are charged under argon into a 250 ml test-tube. 0.44 ml of anhy- drified trif luoroacetic acid CF3C00H (5.9 mmoles) are added to the brown solution. A brown precipitate is formed which, after 4 hours, is filtered and washed with hexane 6 times . The brown, pump- dried solid weighs 1.2 g (yield 52%). Example 2: Synthesis of ferrocene tetra- phenyl bor te Cp2Fe(BPh)
1.13 g of ferrocene Cp2Fe (MW = 186; 6.10 mmoles) are charged into a 100 ml flask and 10 ml of H2SO4 at 96% are slowly added dropwise. There is a substantial development of heat. 2.6 g of Νa(BPh4) (MW = 342; 7.63 mmoles) dissolved in 25 ml of water are slowly added dropwise to the blue solution, Cp2Fe(HS04) . A blue precipitate is formed, which is filtered and washed with ethanol (5 x 10 ml), followed by ethyl ether (5 x 10 ml) and finally dried for a whole night with a vacuum pump and subsequently on P2O5.
Example 3: Synthesis of Vanadium bis- (mesitylene) tetra phenyl borate V(mes)2(BPh ) 0.350 g of Cp2Fe(BPh4) (MW = 505; 0.7 mmoles) and 0.201 g of N (mes ) 2 (MW = 291; 0.7 mmoles) are charged under argon into a 100 ml test-tube containing 30 ml of anhydrous toluene. The mixture is left under stirring for about 4 hours; the dark solid product is filtered and dried. 0.410 g of product are obtained (yield: 96%) .
Example 4
36 mg of V(mes) 2 (OCOCF3) (MW = 404; 0.089 mmoles) are charged under argon into a 100 ml three-necked flask. 20 ml of anhydrous and degassed toluene are added. The resulting brown solution under ethylene becomes lighter. It is left at 45°C for 24 hours. The absorption buret regis- ters an ethylene consumption equal to 500 ml. 1 ml of the solution is removed, 1 ml of a solution of Br2 in CC14 is added and GC analysis is effected.
0.51/22.4 (1/mol) == 0.0223 moles of ethylene used up
Activity: 250.5 moles of ethylene/V moles Selectivity: 56% to 1-hexene Example 5
81 mg of V(mes) 2 (OCOCF3) (MW = 404; 2-10"4 mmoles) are charged under argon into a 250 ml three-necked flask. 30 ml of anhydrous and degassed toluene are added. The brown solution under ethylene becomes lighter. After 10 minutes an absorption equal to 67 ml of ethylene is ob- tained. After 1 hour, as there no longer seems to be any more absorption, 0.080 ml of 2, 5-dimethyl- pyrrole (0.787 mmoles) are added, which causes a further ethylene absorption equal to 33 ml. The green solution, after a night at room tempera- ture, becomes brown again and is analyzed via GC. 0.11/22.4 (1/mol) = 0.00446 moles of ethylene used up
Activity: 22.26 moles of ethylene/vanadium mole Selectivity: 55% to 1-hexene Example 6
56 mg of N ( es) 2 (OCOCF3) (MW = 404; 0.138 mmoles) are charged under argon into a 100 ml three-necked flask. 0.042 ml of 2,5- dimethylpyrrole (0.408 mmoles) are added to 20 ml of distilled and degassed cyclohexane. The orange solution under ethylene darkens. It is left at 50°C for 5 hours; after 3 hours the solution is green and has absorbed 70 ml of ethylene. GC analysis is effected. 0.071/22.4 (1/mol) = 0.003125 moles of ethylene used up
Activity: 22 . 54 moles of ethylene /vanadium mole
Selectivity: 46% to 1-hexene
Example 7 64 mg of N (mes) 2B (Ph) 4 (MW = 610; 1.04-10~4 moles) are charged under argon into a 100 ml three-necked flask. The mixture is dispersed in
30 ml of anhydrous toluene. The reddish-brown suspension under ethylene darkens. It is left at room temperature for 20 hours. After this period of time a black suspension is formed.
In 10 minutes, 70 ml of ethylene are absorbed. It is injected into GC.
0.071/22.4 (1/mol) = 0.00315 moles of ethylene used up
Activity: 29.8 moles of ethylene/vanadium mole
Selectivity: 66% to 1-hexene
Example 8
0.2 ml of V(mes)2 at 6% in hexane (MW = 291; 4.12-10"5 moles) in 20 ml of degassed and anhydrous toluene are charged under argon into a 100 ml test-tube. 21 mg of Cp2Fe(BPh4) (MW = 505;
4.12-10"5 moles) are added to the orange solution. The orange solution is diluted up to 100 ml with toluene, charged into a Buchi 300 ml glass auto- clave and is put under 7 bars of ethylene and maintained at room temperature for 1 hour. It is observed that as ethylene is absorbed, the solution becomes turbid. The autoclave is degassed and the contents discharged without diluting. 1 ml of the solution is removed, 1 ml of a solution of Br2 in CCl4 is added and injected into GC: only 1-hexene is present.
Activity: 605 moles of ethyl ene/N mole Selectivity: 99% to 1-hexene Example 9
30 mg of V(mes) I (MW = 418; 7.17-10~5 moles) in 100 ml of degassed and anhydrous toluene are charged under argon into a 100 ml test-tube. The orange solution is charged into a Buchi 300 ml glass autoclave, put under 7 bars of ethylene and maintained at room temperature for 1 hour. The autoclave is degassed and the contents discharged without diluting. 1 ml of the solution is re- moved, 1 ml of a solution of Br2 in CC1 is added and injected into GC: no olefins are present. Activity: 0 moles of ethylene/V mole Selectivity: 0% to 1-hexene OLIGOMERIZATION TESTS OF ETHYLENE CATALYZED BY V(I)
IN} I
10
Figure imgf000013_0001
Tests carried out at room temperature for 1 hour.
15

Claims

1. A process for the preparation of 1-hexene consisting in effecting the oligomerization of ethylene in the presence of a catalyst comprising a vanadium complex having the formula:
(arene) 2 "VX wherein the term arene represents benzene or mono-, di-, or tri-alkylsubstituted benzene, V is a vanadium ion with a low oxidation state, and X is an anion selected from Cl, Br and I halide ions, or from non-coordinated anions such as B (Ar) 4 ~, A1C14 ", carboxylates and sul- fonates .
2. The process for the preparation of 1-hexene consisting in effecting the oligomerization of ethylene according to the previous claim, characterized in that the reaction is carried out in the presence of a vanadium complex preferably selected from bis- (mesitylene) -vanadium trifluoroacetate bis- (mesitylene) -vanadium-tetraphenylborate bis- (mesitylene) -vanadium-iodide bis- (mesitylene) -vanadium-tetrachloroaluminate.
3. The process for the preparation of 1-hexene consisting in effecting the oligomerization of ethylene according to the first claim, characterized in that the reaction is carried out with the additional presence of a hetero- cyclic compound.
4. The process for the preparation of 1-hexene consisting in effecting the oligomerization of ethylene according to the previous claim, characterized in that the reac- tion is carried out in the presence of a heterocyclic compound preferably selected from pyrroles, substituted pyrroles, phenanthroline, pyridine.
5. The process for the preparation of 1-hexene consisting in effecting the oligomerization of ethylene according to the previous two claims, characterized in that the reaction is carried out in the presence of a heterocyclic compound in a ratio, with respect to the vanadium complex, ranging from 1 to 20.
6. The process for the preparation of 1-hexene consisting in effecting the oligomerization of ethylene according to one or more of the previous claims, characterized in that the reaction is carried out in the presence of a solvent selected from aromatic hydrocarbons and aliphatic hydrocarbons .
7. The process for the preparation of 1-hexene according to the previous claim, characterized in that the reaction is preferably carried out in the presence of a solvent selected from toluene and cyclohexene.
8. The process for the preparation of 1-hexene consisting in effecting the oligomerization of ethylene according to one or more of the previous claims, characterized in that the reaction is carried out at a temperature less than or equal to 150°C.
9. The process for the preparation of 1-hexene according to the previous claim, characterized in that the reaction is preferably carried out at a temperature ranging from 25 to 60°C.
10. The process for the preparation of 1-hexene consisting in effecting the oligomerization of ethylene according to one or more of the previous claims, characterized in that the reaction is carried out at a pressure ranging from 1 to 100 atmospheres.
11. The process for the preparation of 1-hexene according to the previous claim, characterized in that the reac- tion is preferably carried out at a pressure ranging from 1 to 50 atmospheres.
12. The process for the preparation of 1-hexene consisting in effecting the oligomerization of ethylene according to one or more of the previous claims, characterized in that the reaction is carried out for times less than 36 hours .
13. The process for the preparation of 1-hexene according to the previous claim, characterized in that the reaction is preferably carried out for times ranging from 1 to 24 hours.
PCT/EP2001/002827 2000-03-17 2001-03-12 Process for the preparation of 1-hexene WO2001068572A1 (en)

Priority Applications (7)

Application Number Priority Date Filing Date Title
EP01911764A EP1178949B1 (en) 2000-03-17 2001-03-12 Process for the preparation of 1-hexene
US09/926,555 US6459007B1 (en) 2000-03-17 2001-03-12 Process for the preparation of 1-hexene
CA2373406A CA2373406C (en) 2000-03-17 2001-03-12 Process for the preparation of 1-hexene
DE60100252T DE60100252T2 (en) 2000-03-17 2001-03-12 METHOD FOR PRODUCING HEX-1-EN
AU40695/01A AU4069501A (en) 2000-03-17 2001-03-12 Process for the preparation of 1-hexene
AT01911764T ATE239682T1 (en) 2000-03-17 2001-03-12 METHOD FOR PRODUCING HEX-1-ENE
HK02105939.1A HK1045981B (en) 2000-03-17 2002-08-13 Process for the preparation of 1-hexene

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
ITMI2000A000546 2000-03-17
IT2000MI000546A IT1318394B1 (en) 2000-03-17 2000-03-17 PROCESS FOR THE PREPARATION OF 1-ESENE.

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EP (1) EP1178949B1 (en)
AT (1) ATE239682T1 (en)
AU (1) AU4069501A (en)
CA (1) CA2373406C (en)
CZ (1) CZ302831B6 (en)
DE (1) DE60100252T2 (en)
ES (1) ES2199210T3 (en)
HK (1) HK1045981B (en)
IT (1) IT1318394B1 (en)
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WO2006006433A1 (en) * 2004-07-12 2006-01-19 Sumitomo Chemical Company, Limited Catalyst for trimerization of olefin
US7820581B2 (en) 2004-02-20 2010-10-26 Chevron Phillips Chemical Company Lp Methods of preparation of an olefin oligomerization catalyst
US7902415B2 (en) 2007-12-21 2011-03-08 Chevron Phillips Chemical Company Lp Processes for dimerizing or isomerizing olefins
US7910670B2 (en) 2005-08-19 2011-03-22 Chevron Phillips Chemical Company Lp Methods of preparation of an olefin oligomerization catalyst
US7994376B2 (en) 2004-02-19 2011-08-09 Chevron Phillips Chemical Company Lp Olefin oligomerization
US8067609B2 (en) 2007-01-08 2011-11-29 Exxonmobil Chemical Patents Inc. Methods for oligomerizing olefins with chromium pyridine thioether catalysts
US8138348B2 (en) 2007-01-08 2012-03-20 Exxonmobil Chemical Patents Inc. Methods for oligomerizing olefins with chromium pyridine mono-oxazoline catalysts
US8258361B2 (en) 2007-07-04 2012-09-04 Mitsui Chemicals, Inc. Transition metal complex compounds, olefin oligomerization catalysts including the compounds, and processes for producing olefin oligomers using the catalysts
US8329608B2 (en) 2004-02-20 2012-12-11 Chevron Phillips Chemical Company Lp Methods of preparation of an olefin oligomerization catalyst
US8629280B2 (en) 2007-01-08 2014-01-14 Exxonmobil Chemical Patents Inc. Methods for oligomerizing olefins with chromium pyridine ether catalysts
WO2014133005A1 (en) 2013-02-27 2014-09-04 三井化学株式会社 Catalyst for olefin multimerization and method for producing olefin multimer in presence of catalyst for olefin multimerization
US9550841B2 (en) 2004-02-20 2017-01-24 Chevron Phillips Chemical Company Lp Methods of preparation of an olefin oligomerization catalyst
US9586872B2 (en) 2011-12-30 2017-03-07 Chevron Phillips Chemical Company Lp Olefin oligomerization methods
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US7994376B2 (en) 2004-02-19 2011-08-09 Chevron Phillips Chemical Company Lp Olefin oligomerization
US8329608B2 (en) 2004-02-20 2012-12-11 Chevron Phillips Chemical Company Lp Methods of preparation of an olefin oligomerization catalyst
US9550841B2 (en) 2004-02-20 2017-01-24 Chevron Phillips Chemical Company Lp Methods of preparation of an olefin oligomerization catalyst
US8993822B2 (en) 2004-02-20 2015-03-31 Chevron Phillips Chemical Company Lp Methods of preparation of an olefin oligomerization catalyst
US7820581B2 (en) 2004-02-20 2010-10-26 Chevron Phillips Chemical Company Lp Methods of preparation of an olefin oligomerization catalyst
WO2006006433A1 (en) * 2004-07-12 2006-01-19 Sumitomo Chemical Company, Limited Catalyst for trimerization of olefin
US7910670B2 (en) 2005-08-19 2011-03-22 Chevron Phillips Chemical Company Lp Methods of preparation of an olefin oligomerization catalyst
US8138348B2 (en) 2007-01-08 2012-03-20 Exxonmobil Chemical Patents Inc. Methods for oligomerizing olefins with chromium pyridine mono-oxazoline catalysts
US8067609B2 (en) 2007-01-08 2011-11-29 Exxonmobil Chemical Patents Inc. Methods for oligomerizing olefins with chromium pyridine thioether catalysts
US8629280B2 (en) 2007-01-08 2014-01-14 Exxonmobil Chemical Patents Inc. Methods for oligomerizing olefins with chromium pyridine ether catalysts
US8258361B2 (en) 2007-07-04 2012-09-04 Mitsui Chemicals, Inc. Transition metal complex compounds, olefin oligomerization catalysts including the compounds, and processes for producing olefin oligomers using the catalysts
US7902415B2 (en) 2007-12-21 2011-03-08 Chevron Phillips Chemical Company Lp Processes for dimerizing or isomerizing olefins
US9586872B2 (en) 2011-12-30 2017-03-07 Chevron Phillips Chemical Company Lp Olefin oligomerization methods
KR20150104178A (en) 2013-02-27 2015-09-14 미쓰이 가가쿠 가부시키가이샤 Catalyst for olefin multimerization and method for producing olefin multimer in presence of catalyst for olefin multimerization
WO2014133005A1 (en) 2013-02-27 2014-09-04 三井化学株式会社 Catalyst for olefin multimerization and method for producing olefin multimer in presence of catalyst for olefin multimerization
US9616421B2 (en) 2013-02-27 2017-04-11 Mitsui Chemicals, Inc. Catalyst for olefin multimerization and method for producing olefin multimer in presence of catalyst for olefin multimerization
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WO2018016712A1 (en) * 2016-07-18 2018-01-25 에스케이이노베이션 주식회사 Method for oligomerizing olefin
KR20180009179A (en) * 2016-07-18 2018-01-26 에스케이이노베이션 주식회사 Process For preparing oligomer Using olefin

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DE60100252D1 (en) 2003-06-12
CZ20014106A3 (en) 2002-08-14
ITMI20000546A1 (en) 2001-09-17
CZ302831B6 (en) 2011-11-30
CA2373406C (en) 2010-02-09
AU4069501A (en) 2001-09-24
HK1045981A1 (en) 2002-12-20
ITMI20000546A0 (en) 2000-03-17
EP1178949A1 (en) 2002-02-13
IT1318394B1 (en) 2003-08-25
CA2373406A1 (en) 2001-09-20
ES2199210T3 (en) 2004-02-16
EP1178949B1 (en) 2003-05-07
US6459007B1 (en) 2002-10-01
ATE239682T1 (en) 2003-05-15
DE60100252T2 (en) 2004-05-06

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