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Catalytic system for ethylene selective oligomerization and ethylene selective oligomerization method

A catalytic system and selective technology, which is applied in the direction of chemical instruments and methods, catalysts, carbon compound catalysts, etc., can solve the problems of continuous production of products in production equipment, such as post-processing difficulties, and achieve the effects of low cost, high activity, and simple synthesis

Pending Publication Date: 2022-05-13
PETROCHINA CO LTD
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  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0003] The production of linear α-olefins has become an independent branch of the petrochemical industry. As a new type of ethylene oligomerization catalyst, chromium-based catalysts have excellent reaction selectivity. There are many reported patents. Ethylene trimerization (US5550305, US5198563) and ethylene tetramerization (WO2004 / 056478A1, US2006 / 0229480 and US 2006 / 0173226), etc., but the research results show that, in the process of using these chromium catalysts to carry out ethylene oligomerization, a small amount of polymer is always produced, which will cause serious damage to the production equipment. The continuous production and post-processing of the product bring difficulties

Method used

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  • Catalytic system for ethylene selective oligomerization and ethylene selective oligomerization method
  • Catalytic system for ethylene selective oligomerization and ethylene selective oligomerization method
  • Catalytic system for ethylene selective oligomerization and ethylene selective oligomerization method

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Experimental program
Comparison scheme
Effect test

Embodiment 1

[0054] 1. Synthesis of ligand L1 (2,6-dimethyl-(bis-2-pyridinemethanone)aniline)

[0055] Dissolve 0.50g (0.0027mol) dipyridine (L) in 20mL toluene, add 0.33g (0.0027mol) 2,6-dimethylaniline, add a drop of glacial acetic acid as catalyst, add appropriate amount of molecular sieve to remove water, heat to reflux After three days, it was filtered to obtain a yellow liquid, the solvent was evaporated under reduced pressure, and recrystallized with ethanol to obtain a yellow solid with a yield of 93%.

[0056] 1 H NMR (δ, ppm, CDCl 3 , TMS): 2.086 (s, 6H, CH 3 ), 6.789-6.901 (m, 3H, C 6 h 3 ), 7.014(d, 1H, CH), 7.146(m, 1H, CH), 7.356(m, 1H, CH), 7.492(m, 1H, CH), 7.836(m, 1H, CH), 8.297(d , 1H, CH), 8.583(d, 1H, CH), 8.631(d, 1H, CH). 13 C NMR (δ, ppm, CDCl 3 ): 17.39, 122.17, 122.38, 123.63, 126.55, 134.52, 135.59, 147.08, 147.97, 148.15, 153.57, 153.79, 164.85.

[0057] 2. Preparation of catalyst

[0058] All operations were carried out in an anhydrous and oxygen-free ...

Embodiment 2

[0062] 1. Synthesis of ligand L2 (3,5-dimethyl-(bis-2-pyridinemethanone) aniline)

[0063] In the same synthesis method as L1, a light yellow solid was obtained with a yield of 87%. 1 H NMR (δ, ppm, CDCl 3 , TMS): 2.181 (s, 6H, CH 3 ), 6.419(s, 2H, Ph), 6.633(s, 1H, Ph), 7.049(d, 1H, CH), 7.201(m, 1H, CH), 7.344(m, 1H, CH), 7.56(m , 1H, CH), 7.825(m, 1H, CH), 8.213(d, 1H, CH), 8.604(m, 2H, CH).

[0064] 2. Preparation of catalyst

[0065] With embodiment 1. Ligand L1 was exchanged for L2 (1.38 mg) (9.6 μmol).

[0066] 3. Ethylene oligomerization

[0067] Same as Example 1, 80°C is changed to 70°C. The catalyst activity is 9.75×10 5 g oligomer / mol Cr·h. The distribution of the oligomerization products is shown in Table 1.

Embodiment 3

[0069] 1. Synthesis of ligand L3 (3-methylthio-(bis-2-pyridinemethanone) propylamine)

[0070] Dissolve 0.50g (0.0027mol) dipyridinone (L) in 20mL toluene, add 0.28g (0.0027mol) 3-(methylthio)propylamine, add a drop of glacial acetic acid to catalyze, add molecular sieve to remove water, and reflux for three days. Precipitation occurred, filtered to obtain a light green liquid, and the solvent was evaporated under reduced pressure to obtain a dark green oily product. 1 H NMR (δ, ppm, CDCl 3 , TMS): 2.023 (m, 2H, CH 2 ), 2.083 (s, 3H, CH 3 ), 2.575 (m, 2H, CH 2 ), 3.515 (m, 2H, CH 2 ), 7.332(m, 3H, CH), 7.75(m, 1H, CH), 7.794(m, 1H, CH), 8.112(d, 1H, CH), 8.524(m, 1H, CH), 8.735(d , 1H, CH).

[0071] 2. Preparation of catalyst

[0072] With embodiment 1. Ligand L1 was exchanged for L3 (2.4 mg) (9.6 μmol).

[0073] 3. Ethylene oligomerization

[0074] With embodiment 1, catalyst activity is 3.42 * 105 g oligomer / mol Cr·h. The distribution of the oligomerization produc...

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Abstract

The present invention provides a catalytic system for ethylene selective oligomerization, the catalytic system comprises a heteroatom-containing ligand a, a transition metal compound b and an activator c, the heteroatom-containing ligand a is a compound conforming to a general formula (I), or a compound taking a structure conforming to the general formula (I) as a structural unit, and the structure of the general formula (I) is shown in the specification, r is straight-chain or branched-chain alkyl, straight-chain or branched-chain alkyl containing heteroatoms, monocyclic or polycyclic aryl and derivatives thereof. The invention also provides an ethylene selective oligomerization method. The catalytic system provided by the invention is used for selective oligomerization of ethylene, and has the characteristics of high catalytic activity, high selectivity of linear alpha-olefin in the product, no polyethylene by-product, simple catalyst synthesis, low cost, long catalyst life and the like.

Description

technical field [0001] The present invention relates to the field of selective oligomerization of ethylene, in particular to a catalytic system for selective oligomerization of ethylene and a method for selective oligomerization of ethylene, in particular to a method for highly selective oligomerization of ethylene to obtain linear A catalytic system for α-olefins, and a method for obtaining linear α-olefins by highly selective oligomerization of ethylene. Background technique [0002] Linear alpha-olefins refer to C with double bonds at the ends of the molecule 4 The above linear olefins are widely used in the fields of polyethylene comonomers, plasticizer alcohols, flavors and fragrances, synthetic lubricating oils and oil additives. In recent years, with the continuous development of the polyolefin industry, the worldwide demand for α-olefins has grown rapidly. The processes for producing linear α-olefins include fatty alcohol dehydration method, alkane dehydrogenation ...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): B01J31/22B01J31/26C07C2/32C07C11/02C07C11/08C07C11/107
CPCB01J31/1815B01J31/26C07C2/32C07C2531/22C07C2531/26C07C11/02C07C11/08C07C11/107
Inventor 褚洪岭姜涛王斯晗于部伟蒋岩王天成霍洪亮曹媛媛王力搏邵怀奇赵铁铠牟玉强佟铁鑫徐显明王亚丽黄付玲韩雪梅韩云光林如海张爱萍
Owner PETROCHINA CO LTD