2022
DOI: 10.1039/d2nj01527g
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Tuning the Ni site location of bifunctional Ni-based catalysts for improving the performance in ethylene oligomerization

Abstract: The location of Ni sites in the catalyst is very important on the Ni-based catalyst for the ethylene oligomerization. In this work, a series of bifunctional Ni/Al-MCM-41 samples with carefully...

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Cited by 3 publications
(2 citation statements)
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“…This Ni loading is selected because previous studies have shown it to be most beneficial for the bifunctional oligomerization of ethylene. [47] The catalysts are characterized by N 2 adsorption-desorption isotherms, elemental analysis, temperature-programmed reduction, carbon monoxide (CO) pulse chemisorption, the temperature-programmed desorption of ammonia (NH 3 ), Fourier transform infrared (FTIR) spectroscopy with pyridine adsorption, and high-angle annular dark-field imaging transmission electron microscopy (HAADF-TEM), among others. The catalysts are tested during the continuous oligomerization of ethylene at 300 °C and pressures of 1-35 bar, the pulsed adsorption-desorption of ethylene at 40 °C and 1 bar, and the pulsed oligomerization of ethylene at 300 °C and 1 bar and 35 bar.…”
Section: Introductionmentioning
confidence: 99%
“…This Ni loading is selected because previous studies have shown it to be most beneficial for the bifunctional oligomerization of ethylene. [47] The catalysts are characterized by N 2 adsorption-desorption isotherms, elemental analysis, temperature-programmed reduction, carbon monoxide (CO) pulse chemisorption, the temperature-programmed desorption of ammonia (NH 3 ), Fourier transform infrared (FTIR) spectroscopy with pyridine adsorption, and high-angle annular dark-field imaging transmission electron microscopy (HAADF-TEM), among others. The catalysts are tested during the continuous oligomerization of ethylene at 300 °C and pressures of 1-35 bar, the pulsed adsorption-desorption of ethylene at 40 °C and 1 bar, and the pulsed oligomerization of ethylene at 300 °C and 1 bar and 35 bar.…”
Section: Introductionmentioning
confidence: 99%
“…Ni-containing catalysts, microporous and mesoporous catalysts, and solid acid catalysts have been extensively studied as heterogeneous catalysts for EO; examples of such catalysts include the following: nickel ion-exchanged zeolites (e.g., Y [6,9,10], beta [11][12][13][14], ZSM-5 [15,16], MCM-22 [17,18], MCM-36 [17,18]); nickel-loaded amorphous silica-alumina (ASA) [5,[19][20][21][22][23][24][25][26][27]; Ni-exchanged cationic clay [28]; Ni-containing ordered mesoporous silicaalumina (e.g., Al-MCM-41 [29][30][31][32], Al-SBA-15 [33][34][35][36], Al-KIT-6 [37,38]); nickel sulfate (NiSO 4 ) supported on Al 2 O 3 [39][40][41][42], ASA [43], ZrO 2 [44] or TiO 2 [44]; and nickel phosphide (Ni 2 P) supported on ASA [45] or SiO 2 [46]. These catalysts are easy to handle and recycle, and they do not need any promoters or solvents (except for Ni 2 P catalysts).…”
Section: Introductionmentioning
confidence: 99%