王英龙 - 青岛科技大学

研究领域

化工过程模拟、集成与节能；流体相平衡与热力学模拟化工过程强化与工艺改造；环境污染控制与废弃物资源化

近期论文

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Yinglong Wang,* Shisheng Liang, Guangle Bu, Wei Liu, Zhen Zhang, and Zhaoyou Zhu. Effect of Solvent Flow Rates on Controllability of Extractive Distillation for Separating Binary Azeotropic Mixture. Industrial & Engineering Chemistry Research, 2015, 54(51): 12908-12919 (SCI、EI收录， IF=2.587，中科院2区，top期刊) Yinglong Wang,* Zhen Zhang, Yujun Zhao, Shisheng Liang, and Guangle Bu, Control of Extractive Distillation and Partially Heat-Integrated Pressure-Swing Distillation for Separating Azeotropic Mixture of Ethanol and Tetrahydrofuran, Industrial & Engineering Chemistry Research, 2015, 54(34): 8533-8545 (SCI、EI收录， IF=2.587，中科院2区，top期刊) Yinglong Wang*, Zhen Zhang , Huan Zhang , and Qing Zhang, Control of Heat Integrated Pressure-Swing-Distillation Process for Separating Azeotropic Mixture of Tetrahydrofuran and Methanol, Industrial & Engineering Chemistry Research, 2015, 54(5) :1646-1655 (SCI、EI收录， IF=2.587，中科院2区，top期刊) Yinglong Wang*, Peizhe Cui, and Zhen Zhang, Heat-Integrated Pressure-swing Distillation Process for Separation of Tetrahydrofuran/Methanol with Different Feed Composition, Industrial & Engineering Chemistry Research, 2014, 53(17): 7186-7194 (SCI、EI收录， IF=2.587，中科院2区，top期刊) Yinglong Wang*, Peizhe Cui, Yuhong Ma and Zhen Zhang, Extractive Distillation and Pressure-swing Distillation for THF/Ethanol Separation, Journal of Chemical Technology & Biotechnology, 2015, 90: 1463-1472 ( SCI、EI收录， IF=2.037，中科院2区) Yinglong Wang*, Peizhe Cui , Qingxin Meng and Yuhong Ma, Liquid–Liquid Equilibrium for the Ternary System 2-Methyl-2-propanol + 1-Pentanol + Water at T = (303.15, 328.15, and 353.15) K, Journal of Chemical & Engineering Data, 2013, 58 (8): 2254?2259 (SCI、EI收录， IF=2.037) Yinglong Wang*, Ying Liu, Peizhe Cui, Measurement and Correlation of Liquid-Liquid Equilibrium Data for 2-methyl-1-propanol + 2-propanol + Water at Several Temperatures, Fluid Phase Equilibria, 2013,340: 37-41 (SCI、EI收录，IF=2.200, 中科院2区) Yinglong Wang*, Ying Liu, Liquid-Liquid Equilibrium for the Ternary System 2-Methyl-1-propanol + 3-Methyl-1-butanol + Water at (298.15, 323.15 and 348.15) K, Journal of Chemical & Engineering Data, 2012,57 (10): 2689-2695 (SCI、EI收录， IF=2.037)