李永紅

李永紅：男，天津大學化工學院教師。中國能源環境科技協會理事

研究方向:

綠色化學；石油化工；清潔燃料與能源

學術成就:

“蒸餾過程節能與強化關鍵技術及其應用研究”教育部創新團隊

“強化化工本科生實踐能力培養的改革與實”國家教學成果二等獎

科研項目:

低成本清潔油品生產技術研究開發與工業應用

重油臨界區水熱減粘過程研究

催化輕汽油醚化催化精餾新技術中試研究

煉油過程低碳產品高效分離與精製

煉廠尾氣低溫SCR脫硝催化劑的製備

論著專利: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

超臨界水改質重油的研究進展. 現代化工, 2014, 34(4): 17-22.

預硫化對異戊二烯選擇加氫鎳基催化劑性能的影響. 現代化工, 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 型催化劑低溫 NH3 選擇性催化還原 NO[J]. 化工進展, 2013, 32(10): 2403-2408.

Ni-Zn 複合氧化物用於反應吸附脫除噻吩[J]. 石油學報 (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.

一種汽油烷基化脫硫的催化蒸餾方法. 200810114387.8

重組烷基化催化蒸餾脫硫方法. 200810114386.3

一種汽油烷基化脫硫裝置. 200820109556.4

一種高效傳質的催化蒸餾塔內件. 200810052269.9

催化裂化汽油的烴重組烷基化脫硫方法. 200710060353.0

醚化用規整波紋填料支撐β分子篩膜催化劑的製備方法. 01110335.