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Alpha-olefin oligomer and production method thereof

A technology of olefin oligomer and manufacturing method, which is applied in chemical instruments and methods, hydrocarbons, hydrocarbons, etc., and can solve the problems of insufficient amount of dimer components and reduced product yield, etc.

Inactive Publication Date: 2014-04-09
IDEMITSU KOSAN CO LTD
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

For example, when used as a paraffin component or a lubricating oil component, it is necessary to remove unnecessary ultra-low molecular weight components by distillation, and the yield of the product decreases, and the α-olefin oligomers obtained by the methods described in Patent Documents 1 to 5 are decreasing. The amount of dimer components is still insufficient, and performance is expected to be further improved

Method used

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  • Alpha-olefin oligomer and production method thereof
  • Alpha-olefin oligomer and production method thereof
  • Alpha-olefin oligomer and production method thereof

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0223] Example 1 (reaction carried out by preactivation under 50°C and hydrogen pressure of 0.15MPa)

[0224] Into a 50 ml Schlenk bottle equipped with a stir bar, toluene (13 ml) and 1-decene (2 ml, 1.5 g) which had been well bubbled with nitrogen were added under a nitrogen stream. Then, triisobutylaluminum (0.4 mmol: 0.2 ml of a solution diluted to 2 mmol / liter with toluene), dimethylanilinium tetrakis(pentafluorophenyl) borate (60 μmol: after vacuum drying) were added in turn while stirring. Dissolve 3 mL of a solution of 20 μmol / ml in toluene), (1,1'-ethylene)(2,2'-dimethylsilylene)-bis(indenyl)zirconium dichloride (40 μmol: Dissolve 2 mL of 20 μmol / ml solution with heptane). By performing stirring for 6 hours, a solution-like preactivated catalyst (preactivated catalyst concentration: 2 μmol / ml) was obtained.

[0225] Into a heat-dried 1-liter autoclave, 400 ml of 1-decene, 1 mmol of triisobutylaluminum, and the above preactivated catalyst (1 ml, Zr: 2 μmol) were charg...

Embodiment 2(50

[0226] Example 2 (progressive reaction at 50°C and hydrogen pressure of 0.15MPa)

[0227] In a 1-liter autoclave that has been heated and dried, add 400 ml of 1-decene, 1 mmol of triisobutylaluminum, (1,1'-ethylene)(2,2'-dimethylmethylene Silyl)-bis(indenyl)zirconium dichloride 2 micromoles, dimethylanilinium tetrakis(pentafluorophenyl)borate 8 micromoles, and then introduce hydrogen 0.15MPa. After polymerization was carried out at a temperature of 50° C. for 5 hours while stirring, an α-olefin oligomer was obtained. After the obtained reaction solution was treated as described in Example 1, physical properties were measured.

Embodiment 3(90

[0228] Example 3 (progressive reaction at 90°C, hydrogen pressure 0.15MPa)

[0229] In a 1-liter autoclave that has been heated and dried, add 400 ml of 1-decene, 1 mmol of triisobutylaluminum, (1,1'-ethylene)(2,2'-dimethylmethylene Silyl)-bis(indenyl)zirconium dichloride 2 micromoles, dimethylanilinium tetrakis(pentafluorophenyl)borate 8 micromoles, and then introduce hydrogen 0.15MPa. After polymerization was carried out at a temperature of 90° C. for 5 hours while stirring, an α-olefin oligomer was obtained. After the obtained reaction solution was treated as described in Example 1, physical properties were measured.

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Abstract

Provided are: an alpha -olefin oligomer fulfilling (1)-(6) below; an alpha-olefin oligomer which is produced with an alpha-olefin oligomer production method using a specific double-cross-linked meso-type complex and which has a low amount of dimer components while having a low viscosity without following the Schulz-Flory distribution; and a production method of said a-olefin oligomers. (1) The trimer component proportion C3 (mass%) is higher than the theoretical value found by means of the S-F distribution. (2) The hexamer component proportion C6 (mass%) is lower than the theoretical value found by means of the S-F distribution. (3) 100 DEG C kinematic viscosity is 20mm2 / s or less. (4) The mesotriad fraction [mm] measured by 13C-NMR is 40 mol% or less. (5) There are 0.2-1.0 vinylidene groups per 1 molecule. (6) The average carbon number of monomer units is 6-30. Here, the aforementioned S-F distribution is computed on the basis of chain growth probability a calculated from the dimer component proportion C2 (mass%).

Description

technical field [0001] The present invention relates to an α-olefin oligomer and a method for producing the same. More specifically, it relates to an α-olefin oligomer useful as a paraffin wax component and a lubricating oil component, and a method for producing the same. Background technique [0002] In recent years, α-olefin oligomers have been produced using metallocene-based catalysts and used as paraffin wax components or lubricating oil components. For example, Patent Document 1 discloses a polymer obtained by polymerizing a higher α-olefin having 10 or more carbon atoms using a metallocene catalyst, and a catalyst using a racemic dicrosslinked compound is used in Examples. Patent Document 2 discloses a method for producing an α-olefin polymer in which an α-olefin having 4 or more carbon atoms is polymerized using a metallocene-based catalyst. In an example, a syndiotactic type dioxocarbon having two different crosslinking groups was used. Catalyst for crosslinking co...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C08F10/14C07C2/24C07C11/02C07F17/00C08F4/6592
CPCC07C2/24C08F110/14C08F4/6592C08F4/65908C07C11/21C07F7/082C08F4/65927C07C2/32C07C2531/22C07C11/02C08F10/14C07C2/34C07C2531/14C07C2531/38C08F4/65912B01J31/143B01J31/146B01J31/2295B01J2231/20B01J2531/48C07F7/0803
Inventor 辻深奈子冈本卓治藤村刚经南裕
Owner IDEMITSU KOSAN CO LTD