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Catalyst for olefin multimerization and method for producing olefin multimer in presence of said catalyst

A technology for olefin multimers and production methods, applied to the field of olefin multimerization catalysts and the production of olefin multimers in the presence of the catalysts, to achieve excellent activity and high production efficiency

Pending Publication Date: 2020-03-06
MITSUI CHEM INC
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

Therefore, it is sometimes difficult to respond flexibly to changes in the market conditions of each component

Method used

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  • Catalyst for olefin multimerization and method for producing olefin multimer in presence of said catalyst
  • Catalyst for olefin multimerization and method for producing olefin multimer in presence of said catalyst
  • Catalyst for olefin multimerization and method for producing olefin multimer in presence of said catalyst

Examples

Experimental program
Comparison scheme
Effect test

Embodiment

[0244] Hereinafter, the present invention will be specifically described based on synthesis examples and examples, but the present invention is not limited to these examples.

[0245] The structure of the compound obtained by the synthesis example uses 270MHz 1 H NMR (manufactured by JEOL, device name GSH-270), ICP emission spectrometer (manufactured by Agilent Technologies, device name 720-ES type) and other devices.

[0246] The yield of the reaction product and the selectivity of 1-hexene and 1-octene were analyzed by gas chromatography (Shimadzu GC-14A, J&WScientific DB-5 column).

[0247] [catalytic activity]

[0248] The catalytic activity was obtained by dividing the mass of the reaction product obtained per unit time by the transition metal atomic weight (mmol) in the transition metal catalyst component used for the polymerization.

[0249] [Selectivity of 1-hexene or 1-octene]

[0250] The selectivity of 1-hexene or 1-octene was calculated|required according to the f...

Synthetic example 1

[0258] Into a well-dried 20 mL reactor, 2.1 mL (25.4 mmol) of pyrrolidine and 1.0 mL (13.3 mmol) of 37% aqueous formaldehyde were added, followed by stirring at room temperature. After 17 hours, diethyl ether was added to the reaction solution, the soluble fraction was extracted, and the obtained fraction was dried over anhydrous magnesium sulfate. After filtering magnesium sulfate, the filtrate was distilled off the solvent under reduced pressure. The obtained crude product was distilled under reduced pressure to obtain 1.32 g (64% yield) of an amine compound represented by the following formula (B-2) (hereinafter referred to as compound (1)).

[0259] 1 H-NMR (270MHz, CD 3 COCD 3 ):3.10(2H,s),2.52-2.43(8H,m),1.74-1.62(8H,m)ppm

[0260] [chemical 14]

[0261]

Synthetic example 2

[0263] Into a well-dried 20 mL reactor, 3.2 mL (27.0 mmol) of 3-methylpiperidine and 1.0 mL (13.3 mmol) of 37% aqueous formaldehyde were added at 0°C, followed by stirring at room temperature. After 18 hours, diethyl ether was added to the reaction solution, the soluble fraction was extracted, and the obtained fraction was dried over anhydrous magnesium sulfate. After filtering magnesium sulfate, the filtrate was distilled off the solvent under reduced pressure. The obtained crude product was distilled under reduced pressure to obtain 1.95 g (yield 70%) of an amine compound represented by the following formula (B-3) (hereinafter referred to as compound (2)).

[0264] 1 H-NMR (270MHz, CD 3 COCD 3 ):2.92-2.82(4H,m),2.74(2H,s),1.84-1.73(2H,m),1.71-1.37(10H,m),0.93-0.86(2H,m),0.85(3H,d ,J=1.6Hz),0.83(3H,d,J=1.6Hz)ppm

[0265] [chemical 15]

[0266]

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Abstract

Disclosed are: a production method for an olefin multimer, the method comprising conducting an olefin multimerization reaction in the presence of a catalyst for olefin multimerization which comprisesa chromium compound (A), an amine compound (B) of general formula (1), and a compound (C) such as an organometallic compound; and the catalyst for olefin multimerization. In general formula (1), R1 toR4 each represent a group, e.g., a hydrocarbon group; Y indicates a structure represented by -CR5R6-, where R5 and R6 each represent a hydrogen atom or a group; and Z is an integer of 1-10.

Description

technical field [0001] The present invention relates to an olefin multimerization catalyst having excellent activity and high selectivity and / or production efficiency of a specific olefin multimer, and production of an olefin multimer in the presence of the olefin multimerization catalyst method. Background technique [0002] α-Olefin is an important compound widely used industrially as a raw material of polyolefin, for example. For example, 1-hexene and 1-octene are in high demand as raw materials for polyolefins. Among the methods for producing α-olefins, there is a method using an organoaluminum or a transition metal compound as a catalyst, which has already been industrialized. However, in processes that have been industrialized, mixtures of various α-olefins are usually obtained. Therefore, it may be difficult to respond flexibly to changes in the market conditions of each component. Therefore, a method for producing a target α-olefin with high selectivity has been ...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C07C2/08B01J31/34C07C11/02C07B61/00
CPCC07B61/00C07C2/32C07C2531/18C07C2531/14B01J31/182B01J31/1805B01J31/143B01J2231/20B01J2531/62Y02P20/52C07C11/02C07C11/107B01J31/0244B01J31/34C07C2/08C07C11/04
Inventor 石井圣一市川真一郎藤田照典
Owner MITSUI CHEM INC