天津大学化工学院教师 李永红

李永红(天津大学化工学院教师)基本介绍中文名:李永红
性别:男
职务:天津大学化工学院教师
研究方向: 绿色化学、石油化工
李永红:男,天津大学化工学院教师 。中国能源环境科技协会理事研究方向:绿色化学;石油化工;清洁燃料与能源学术成就:“蒸馏过程节能与强化关键技术及其套用研究”教育部创新团队“强化化工本科生实践能力培养的改革与实”国家教学成果二等奖科研项目:低成本清洁油品生产技术研究开发与工业套用重油临界区水热减粘过程研究催化轻汽油醚化催化精馏新技术中试研究炼油过程低碳产品高效分离与精製炼厂尾气低温SCR脱硝催化剂的製备论着专利: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 複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分子筛膜催化剂的製备方法. 01110335.