Hydrocracking of AATO on Ni/USY and Ni-Co/ USY Zeolite Catalysts

Zhao Xiang Yu; Shi Zhen Li; Qian Wu; Meng Zhi Chen; Zhi Rong Zhu

doi:10.4028/www.scientific.net/AMR.347-353.3699

Paper Titles

Dimethyl Ether Conversion to Olefins over the SAPO-34/ZrO₂ Catalysts: Effect of the ZrO₂ Supporter
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Preparation of a Styrenesulfonate Grafted MWCNT/Nafion® Nanocomposite Membrane for Direct Methanol Fuel Cell Applications
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Study of Cu-Fe-Co-M/SiO₂ (M = Unpromoted, Li, Na, K and Cs) Catalysts for Mixed Alcohols Synthesis from CO Hydrogenation
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The Preparation of Hybrid Solid Acids and its Catalytic Performance
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Hydrocracking of AATO on Ni/USY and Ni-Co/ USY Zeolite Catalysts
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Simulation of Reactive Distillation Process with ChemCAD Software
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Catalytic Hydrogenation and Hydrocracking of PRO Residual Oil over USY-Zeolite Catalyst
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Comparison Research between SMA with Activated Mineral Binder Stabilizer (AMBS) and SMA with Lignin Fiber
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Dithiocarbamate Derivative as an Efficient Inhibitor for Copper
p.3724

HomeAdvanced Materials ResearchAdvanced Materials Research Vols. 347-353Hydrocracking of AATO on Ni/USY and Ni-Co/ USY...

Hydrocracking of AATO on Ni/USY and Ni-Co/ USY Zeolite Catalysts

Abstract:

A series of Ni and Ni-Co were maintained on a mixed support of USY (ultrastable Y) zeolite and active aluminum oxide. The catalysts were characterized by means of element analysis, BET and XRD. The characterization results suggested that the active metal components were introduced without changing the microstructure. Then catalytic hydrocracking activity was studied using AATO (distillate of coal tar) in a tubular reactor. AATO conversion was 39.40% and 41.37% using the 10%Ni/USY catalyst and 10%Ni-6%Co/USY catalyst, the hightest total selectivity of benzene and xylol was 67.1% in 10%Ni-10%Co/USY catalyst than others under the reaction conditions studied [T=480°C, P=4.5MPa, LHSV=3.0h-1].