Catalyst components and catalysts for selective oligomerization of ethylene
A catalyst and selective technology, applied in physical/chemical process catalysts, organic compound/hydride/coordination complex catalysts, compounds of Group 5/15 elements of the periodic table, etc., can solve huge equipment investment and process routes complex and other issues, to achieve the effect of long catalyst life, simple synthesis and high activity
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Embodiment 1
[0027] 1. Preparation of N-diphenylphosphino-2,6-diisopropylanilino (diphenylphosphino) dimethylsilane (C 38 h 43 NP 2 Si)
[0028] (1) Preparation of diphenylphosphinolithium
[0029] in the N 2 Add dehydrated THF (200 mL) and diphenylphosphine (18.62 g, 0.1 mol) into a fully replaced stirred 500 mL reactor, stir well and cool to -80° C. with liquid nitrogen. Draw n-butyllithium hexane solution (41.6mL, 2.4mol / L) with a 100mL syringe, slowly add it dropwise to the above solution while stirring, keep stirring at -80°C for 1h, then rise to room temperature and continue stirring for 1 hour, and then vacuum The solvent was removed, n-hexane (100 mL) was added, stirred thoroughly and then filtered, and the obtained filtrate was vacuum-extracted at room temperature to obtain 18.82 g (0.098 mol, 98.6%) of the product.
[0030] (2) prepare diphenylphosphinodimethylsilyl chloride (C 14 h 16 ClPSi)
[0031] in N 2 In an atmosphere glove box, dimethyldichlorosilane (6.45g, 0.05...
Embodiment 2
[0041] With embodiment 1. The difference is that Ph 1 ~Ph 4 Both are dimethylphenyl. Obtain 50.2g of oligomerization product, catalyst activity is 3.04×10 6 g oligomer / mol Cr·h. The distribution of the oligomerization products is shown in Table 1.
Embodiment 3
[0043] With embodiment 1. The difference is that Ph 1 ~Ph 4 Both are naphthyl. Obtain 51.3g of oligomerization product, catalyst activity is 3.11×10 6 g oligomer / mol Cr·h. The distribution of the oligomerization products is shown in Table 1.
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