尤新强
副教授，硕士生导师
最高学历：
法国图卢兹大学化学工程 博士
研究领域：
化工过程模拟与强化、分子热力学及状态方程的开发与应用
Tel:
17859191101
E-mail:
youxq@fzu.edu.cn
教育工作经历：
2019.7至今 我院石油化工学院 副教授
2015.12～2018.3 华东理工大学 化学工程与技术 博士后
2012.9～2015.9 图卢兹大学 化学工程与技术 博士
2009.9～2012.6 重庆大学 化学工程与技术 硕士
2005.9～2009.7 唐山学院 化学工程与工艺 学士
科研项目：
目前在研主持的科研项目：
1. 国家自然科学基金青年基金：受限流体分子热力学及其状态方程，项目批准号：
21706062，负责人。
近年来已完成的主要科研项目：
2. 中国博士后科学基金：精馏过程及其强化在醋酸脱水过程中的应用研究与评价，项
目批准号：2016M601528，负责人。
社会兼职：
担任applied energy，IECR , CES等期刊审稿人。
代表性论文：
1. You, Xinqiang et al. Design and optimization of sustainable pressure swing distillation for minimum-boiling azeotrope separation. Ind. Eng. Chem. Res. 2019.58,21659.
2. You, Xinqiang, et al. A joint model for calculating capillary pressure of confined fluid based on the SWCF-VR equation of state. Fluid Phase Equilibria 2019,498: 59-71.
3. Gu, J. You, Xinqiang et al. Analysis of heat integration, intermediate reboiler and vapor recompression for the extractive distillation of ternary mixture with two binary azeotropes. Chemical Engineering and Processing-Process Intensification 2019,142: 107546.
4. You, Xinqiang et al. Optimization of pre-concentration, entrainer recycle and pressure selection for the extractive distillation of acetonitrile-water with ethylene glycol. Chem. Eng. Sci. 2018. 177: 354.
5. Gu J, You, Xinqiang et al. Energy-saving reduced pressure extractive distillation with heat integration for separating biazeotropic ternary mixture tetrahydrofuran-methanol-water[J]. Ind. Eng. Chem. Res. 2018. 57:13498-13510.
6. Gu J, You, Xinqiang et al. Improved design and optimization for separating tetrahydrofuran–water azeotrope through extractive distillation with and without heat integration by varying pressure[J]. Chem. Eng. Res. Des. 2018, 133: 303-313.
7. You, Xinqiang et al. Improved design and optimization for separating azeotropes with heavy component as distillate through energy-saving extractive distillation by varying pressure. Ind. Eng. Chem. Res. 2017.56,9156.
8. You, Xinqiang et al. Optimal design of extractive distillation for acetic acid dehydration with N-methyl acetamide. Chem. Eng. Processing: Process Intensif. 2017, 120,301.
9. You, Xinqiang et al. Reducing process cost and CO2 emissions for extractive distillation by double-effect heat integration and mechanical heat pump. Applied Energy, 2016, 166, 128.
10. You, Xinqiang et al. Low pressure design for reducing energy cost of extractive distillation for separating diisopropyl ether and isopropyl alcohol. Chem. Eng. Res. Des. 2016, 109, 540.
11. You, Xinqiang et al. Improved Design and Efficiency of the Extractive Distillation Process for Acetone-Methanol with Water. Ind. Eng. Chem. Res. 2015, 54, 491.
12. You, Xinqiang et al. Investigation of separation efficiency indicator for the optimization of the acetone-methanol extractive distillation with water. Ind. Eng. Chem. Res. 2015, 54, 10863.
13. *** You, Xinqiang, ***. CAMD for entrainer screening of extractive distillation process based on new thermodynamic criteria." Chem. Eng. Res. Des. 2019, 147: 721-733.
14. *** You, Xinqiang, ***. Review of Extractive Distillation. Process design, operation, optimization and control[J]. Chemical Engineering Research and Design, 2018. 141:229-271.
15. *** You, Xinqiang et al. Systematic design of an extractive distillation for maximum‐boiling azeotropes with heavy entrainers. AIChE J. 2015, 61, 3898.
16. You, Xinqiang et al. Novel energy saving strategy for separating acetic acid–water in extractive distillation with N-methyl acetamide as entrainer. IOP Conf. Ser.: Mater. Sci. Eng. 2017, 231 012110.
