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7篇 您的检索式:作者名="Mingfeng L"
    题名 作者 年代 出处 被引量
1Nanoparticle-filled capillary electrophoresis for the separation of long DNA molecules in the presence of hydrodynamic and electrokinetic forces 显示文摘TSENG W L HUANG Mingfeng HUANG Yufen 2005Electrophoresis2005,26,16:1
2Separation of dsDNA in the presence of electroosmotic flowunder discontinuous conditions显示文摘HUANG Mingfeng HSU C E TSENG W L 2001Electrophoresis2001,22,:1
3Comparative analysis of actuator concepts for active gear pair vibration control 显示文摘Yuan H G Mingfeng L Teik C L 2004Joumal of Sound and Vibration2004,269,12:1
4Effects of PPAR-y agonist treatment on lps-induced mastiffs in rats 显示文摘MINGFENG D XIAODONG M YUE L 2014Inflammation2014,37,6:1
5Effects of PPAR-γagonist treatment on LPS-induced mastitis in rats显示文摘Mingfeng D Xiaodong M Yue L 2014Inflammation2014,37,6:1
6Calculation of the surrounding rock pressure on a shallow buried tunnel using linear and nonlinear failure criteria显示文摘MINGFENG L LIMIN P CHENGHUA S 2014Automation in Construction2014,37,:1
7Hydrodearomatization Kinetics of Diesel Fraction and Catalyst Stacking Simulation显示文摘The kinetics of hydrodearomatization (HDA) is studied in an isothermal high-throughput reactor over three catalysts (CoMo, NiMo, and NiMoW) to produce clean diesel fuel according to China’s latest emission standards. The influences of reaction temperature, pressure, the ratio of H2 to oil, and space time were systematically investigated. By analyzing the reaction mechanism, a four-lump kinetic model considering the influence of competitive adsorption was proposed for the hydrodearomatization reaction, and the model parameters were optimized with good fitting. It was found that nitrogen compounds inhibited the hydrodearomatization reaction. The simulation of various catalyst stacking schemes based on the HDA kinetic model is close to the experimental data, proving the reliability of the model. The concentration of aromatic compounds of different loading sequences was predicted with the catalyst gradation model.Wei Ye Sun Xinge LüHailong Jiang Hongbo Chen Wenbin Qin Kang Li Mingfeng Nie Hong 2022China Petroleum Processing & Petrochemical Technology2022,24,3:0
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