| 1 |
Highly Efficient Production of 5-Hydroxymethylfurfural from Fructose via a Bromine-Functionalized Porous Catalyst under Mild Conditions
Zhao J, Si ZH, Shan HC, Cai D, Li SF, Li GZ, Lin HF, Baeyens J, Wang GR, Zhao HN, Qin PY
Industrial & Engineering Chemistry Research, 59(33), 14569, 2020 |
| 2 |
Study on the Catalytic Properties of Ru/TiO2 Catalysts for the Catalytic Oxidation of (Chloro)-Aromatics
Wang J, Zhao HN, Liu XL, Xu WQ, Guo YY, Song JF, Zhu TY
Catalysis Letters, 149(7), 2004, 2019 |
| 3 |
A magnetically recyclable chitosan composite adsorbent functionalized with EDTA for simultaneous capture of anionic dye and heavy metals in complex wastewater
Chen B, Zhao HN, Chen SJ, Long FX, Huang B, Yang BQ, Pan XJ
Chemical Engineering Journal, 356, 69, 2019 |
| 4 |
Modeling vapor-liquid phase equilibria of hydrogen sulfide and water system using a cubic EOS-G(EX) model
Zhao HN, Fang ZB, Jing HB, Liu JQ
Fluid Phase Equilibria, 484, 60, 2019 |
| 5 |
Chiral Bidentate Boryl Ligand Enabled Iridium-Catalyzed Asymmetric C(sp(2))-H Borylation of Diarylmethylamines
Zou XL, Zhao HN, Li YW, Gao Q, Ke ZF, Xu SM
Journal of the American Chemical Society, 141(13), 5334, 2019 |
| 6 |
Opioid prescribing decreases after learning of a patient's fatal overdose
Doctor JN, Nguyen A, Lev R, Lucas J, Knight T, Zhao HN, Menchine M
Science, 361(6402), 588, 2018 |
| 7 |
Modeling vapor-liquid phase equilibria of methane-water and methane-carbon dioxide-water systems at 274K to 573K and 0.1 to 150 MPa using PRSV equation of state and Wong-Sandler mixing rule
Zhao HN
Fluid Phase Equilibria, 447, 12, 2017 |
| 8 |
Preparation and evaluation of 1-deoxynojirimycin sustained-release pellets vs conventional immediate-release tablets
Sun ZY, Yuan SJ, Zhao HN, Wang ZY, Liu ZM
Journal of Microencapsulation, 34(3), 293, 2017 |
| 9 |
Theoretical insight into a series of cyclometalated platinum(II) complexes with the substituted 2-phenylimidazole ligand
Han DM, Wang HL, Lv SH, Zhao HN, Zhao LH
Molecular Crystals and Liquid Crystals, 656(1), 185, 2017 |
| 10 |
Phase behavior of the CO2-H2O system at temperatures of 273-623 K and pressures of 0.1-200 MPa using Peng-Robinson-Stryjek-Vera equation of state with a modified Wong -Sandler mixing rule: An extension to the CO2-CH4-H2O system
Zhao HN, Lvov SN
Fluid Phase Equilibria, 417, 96, 2016 |
