SCHOOL OF CHEMICAL ENGINEERING

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教授

李永红

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论著专利:

Molybdenum modified CeAlOx catalyst for the selective catalytic reduction of NO with NH3 [J]. Journal of Molecular Catalysis A: Chemical, 2014, 386: 69-77.
Selective Catalytic Reduction of NO with NH3 over Ce-Mo-Ox Catalyst [J]. Catalysis Letters, 2014, 144:165-171.
Influence of the preparation method on the performance of CeO2-MoO3 catalyst for the selective catalytic reduction of NO with NH3 [J]. Reaction Kinetics, Mechanisms and Catalysis, 2014, DOI 10.1007/s11144-014-0688-0
超临界水改质重油的研究进展. 现代化工, 2014, 34(4): 17-22.
预硫化对异戊二烯选择加氢镍基催化剂性能的影响. 现代化工, 2014, 34(1): 111-116.
Isobaric vapor–liquid equilibrium for systems containing sulfur compounds [J]. Fluid Phase Equilibria, 2013, 353: 87-92.
Reactive adsorption desulfurization over a Ni/ZnO adsorbent prepared by homogeneous precipitation[J]. Frontiers of Chemical Science and Engineering, 2013, 7(2): 170-176.
A Ce-Sn-Ox catalyst for the selective catalytic reduction of NOx with NH3 [J]. Catalysis Communications, 2013, 40: 47-50.
MnOx-SnO2/TiO2 型催化剂低温 NH3 选择性催化还原 NO[J]. 化工进展, 2013, 32(10): 2403-2408.
Ni-Zn 复合氧化物用于反应吸附脱除噻吩[J]. 石油学报 (石油加工), 2013, 29(2): 214-222.
Isobaric vapor–liquid equilibrium for four binary systems of 3-methylthiophene [J]. Fluid Phase Equilibria, 2012, 320: 26-31.
Analysis and simulation of reactive distillation for gasoline alkylation desulfurization [J]. Chemical Engineering Science, 2012, 72: 115-125.
Effect of Methanol on Catalytic Performance of HY Zeolite for Desulfurization of FCC Gasoline by Alkylation [J]. Industrial & Engineering Chemistry Research, 2012, 51(18): 6320-6326.
Isothermal vapor–liquid equilibria for methanol and 2, 3-dimethyl-2-butene at 343.15 K, 353.15 K, 363.15 K, 373.15 K[J]. Fluid Phase Equilibria, 2011, 309(2): 201-205.
Isothermal Vapor− Liquid Equilibrium for Methanol and 2, 3-Dimethyl-1-butene at 343.06 K, 353.27 K, 363.19 K, and 372.90 K[J]. Journal of Chemical & Engineering Data, 2011, 56(5): 2386-2392.
Effect of metal–support interaction on the catalytic performance of Ni/Al2O3 for selective hydrogenation of isoprene [J]. Journal of Molecular Catalysis A: Chemical, 2011, 344(1): 122-127.
Catalytic mechanism of MCM-41 supported phosphoric acid catalyst for FCC gasoline desulfurization by alkylation: experimental and theoretical investigation [J]. Energy & Fuels, 2011, 25(9): 3940-3949.
Alkylation of Thiophenic Compounds with Olefins and Its Kinetics over MCM-41 Supported Phosphoric Acid in FCC Gasoline. Catalysis Letters, 2010, 139: 114-122.
The performance of solid phosphoric acid catalysts and macroporous sulfonic resins on gasoline alkylation desulfurization. Fuel Processing Technology, 2010, 91: 1731–1735. 
Preparation of MCM-41 supported phosphoric acid catalyst for thiophenic compounds alkylation in FCC gasoline. Catalysis Communications, 2010, 11(8): 705-709. 
一种汽油烷基化脱硫的催化蒸馏方法. 200810114387.8
重组烷基化催化蒸馏脱硫方法. 200810114386.3
一种汽油烷基化脱硫装置. 200820109556.4
一种高效传质的催化蒸馏塔内件. 200810052269.9
催化裂化汽油的烃重组烷基化脱硫方法. 200710060353.0
醚化用规整波纹填料支撑β分子筛膜催化剂的制备方法. 01110335.3