1.论文 [1] Liu, J.; Yan, J.; Liu, W.; Kong, J.; Wu, Y.; Li, X.; Sun, L.; Design and multi-objective optimization of reactive-extractive dividing wall column with organic Rankine cycles considering safety, Separation and Purification Technology, 2022, 287(15): 120512. [2] Liu, J.; Liu, X.; Li, J.; Ren, J.; Wang, J.; Sun, L.; Design and control of side-stream extractive distillation to separate acetic acid and cyclohexanone from wastewater by varying pressure, Process Safety and Environmental Protection, 2022, 159:1127-1149. [3] Luo, F.; Liu, X.; Chen, S.; Song, Y.; Yi, X.; Xue, C.; Li, J.; Sun, L.; Comprehensive evaluation of a deep eutectic solvent based CO2 capture process through experiment and simulation, ACS Sustainable Chemistry & Engineering, 2021, 9(30): 10250-10265. [4] Liu, J.; Gao, L.; Ren, J.; Liu, W.; Liu, X.; Sun, L.; Dynamic process intensification of dimethyl ether reactive distillation based on output multiplicity, Industrial & Engineering Chemistry Research, 2020, 59(45): 20155-20167. [5] Ma, S.; Liu, J.; Xu, W.; Sun, F.; Jiang, J.; Sun, L.; Experiment and simulation for CO2 capture using low transition temperature mixtures as solvents, International Journal of Greenhouse Gas Control, 2020, 103: 103178. [6] Song, Y.; Chen, S.; Luo, F.; Sun, L.; Absorption of toluene using deep eutectic solvents: quantum chemical calculations and experimental investigation, Industrial & Engineering Chemistry Research, 2020, 59(52): 22605-22618. [7] Shang, X.; Ma, S.; Pan, Q.; Li, J.; Sun, Y.; Ji, K.; Sun, L.; Process analysis of extractive distillation for the separation of ethanol-water using deep eutectic solvent as entrainer, Chemical Engineering Research and Design, 2019, 148: 298-311. [8] Ma, S.; Shang, X.; Li, L.; Song, Y.; Pan, Q.; Sun, L.; Energy-saving thermally coupled ternary extractive distillation process using ionic liquids as entrainer for separating ethyl acetate-ethanol-water ternary mixture, Separation and Purification Technology, 2019, 226: 337-349. [9] Li, J.; Zhang, F.; Pan, Q.; Yang, Y.; Sun, L.; Performance enhancement of reactive dividing wall column based on self-heat recuperation technology, Industrial & Engineering Chemistry Research, 2019. [10] Pan, Q.; Li, J.; Shang, X.; Ma, S.; Liu, J.; Sun, M.; Sun, L.; Controllability, energy-efficiency and safety comparisons of different control schemes for producing n-butyl acetate in a reactive dividing wall column, Industrial & Engineering Chemistry Research, 2019, 58(22): 9675-9689. [11] Pan, Q.; Shang, X.; Li, J.; Ma, S.; Li, L.; Sun, L.; Energy-efficient separation process and control scheme for extractive distillation of ethanol-water using deep eutectic solvent, Separation and Purification Technology, 2019, 219: 113-126. [12] Sun, L.; Luo, F.; Liu, R.; Yang, H.; Huang, L.; Li, J.; Isobaric liquid–liquid equilibrium measurements and thermodynamics modeling for systems: Benzene+ cyclohexane+ DESs at 303.15 and 323.15 K. Journal of Chemical & Engineering Data, 2019, 64(3): 1113-1121. [13] Ma, S.; Shang, X.; Li, L.; Pan, Q.; Xue, C.; Ji, K.; Sun, L.; Optimization and control of CO2 capture using low transition temperature mixtures. International Journal of Greenhouse Gas Control, 2019, 81: 126-136. [14] Ma, S.; Shang, X.; Zhu, M.; Li, J.; Sun, L.; Design, optimization and control of extractive distillation for the separation of isopropanol-water using ionic liquids, Separation and Purification Technology, 2019, 209: 833-850. [15] Sun, Y.; Fu, D.; Ma, S.; Ma, Z.; Sun, L.; Isobaric vapor–liquid equilibrium data for two binary systems n-hexane+ 1, 2-dimethoxyethane and methylcyclopentane+ 1, 2-dimethoxyethane at 101.3 kPa, Journal of Chemical & Engineering Data, 2018, 63(2): 395-401. [16] Ma, S.; Shang, X.; Li, J.; Li, L.; Sun, Y.; Yang, Y.; Sun, L.; Liquid–liquid extraction of benzene using low transition temperature mixtures: COSMO-SAC predictions and experiments, Journal of Chemical & Engineering Data, 2018, 63(12): 4749-4760. [17] Ma, S.; Li, J.; Li, L.; Shang, X.; Liu, S.; Xue, C.; Sun, L.; Liquid–liquid extraction of benzene and cyclohexane using sulfolane-based low transition temperature mixtures as solvents: Experiments and simulation, Energy & Fuels, 2018, 32(7): 8006-8015. [18] Zhu, M.; Hou, Y.; Yu, N.; Chen, M.; Ma, Z.; Sun, L.; Design and control of a middle-vessel batch distillation for separating DMC–EMC–DEC mixture, Chinese Journal of Chemical Engineering, 2018, 26(9): 1837-1844. [19] Wang, J.; Yu, N.; Chen, M.; Cong, L.; Sun, L.; Composition control and temperature inferential control of dividing wall column based on model predictive control and PI strategies, Chinese Journal of Chemical Engineering, 2018, 26(5): 1087-1101. 2.专利 [1] 气液分配器及气液分配盘，201921503100.0 [2] 气液分配器及气液分配盘，201921449004.2 [3] 喷射旋流型气液分配器，201921234142.9 [4] 一种直链烷基苯的生产方法，201810079546.9 [5] 丙酮气相缩合制备异佛尔酮的设备及方法，201710766032.6 [6] 一种生产己二酸二甲酯的设备及方法，201610628645.9 [7] 一种生产己二酸二甲酯的设备及方法，201610634150.7 [8] 一种隔壁塔热泵精馏分离松节油的工艺及装置，201610452203.3 [9] 一种多产轻重芳烃产品的重油催化裂化工艺，201510493527.7 [10] 一种重油多产芳烃的方法，201510493528.1 [11] 一种异丁烷脱氢制异丁烯用催化剂及其制备方法与应用，201410841652.8 [12] 一种异丁烷脱氢制异丁烯用催化剂及其制备方法与应用，201410841699.4 [13] 一种差压热耦合萃取精馏分离甲基环己烷和甲苯的方法，201210051656.7 |
