化工过程系统工程团队
日期：2017-04-13 | 访问量：
一、团队名称：化工过程系统工程团队
二、团队成员：刘伯潭、盖晓龙、王红星
三、实验室位置：8号楼B501-B505
四、研究方向：
化工过程建模与优化
反应精馏过程开发
计算传质学
化工过程智能控制
能源资源系统优化
隔板精馏、热泵精馏、内部能量热集成技术开发
五、研究成果
主持完成国家及省部级基金项目10余项，至今发表高水平SCI论文20余篇，授权发明专利10余项，承担研究生与本科生专业核心课程教学。
1. 将复杂多相剩余曲线应用于反应精馏设计，成功开发了第三代催化填料，成功研发高转化率、高选择性、低能耗、低物耗反应精馏技术并实现工业化。
2. 针对隔板精馏塔、热泵精馏塔、内部能量热集成塔进行了系统研究，发展了先进精馏技术优化设计的系统工程方法，针对复杂精馏强非线性系统，发展了其控制结构的方案框架，实现了过程集成与过程强化。
3. 建立了化工计算传质学体系与模型，提出了传质理论的双方程模型与雷诺质流模型，将介尺度理论应用于化工过程研究，实现化工过程传质系数的理论求取。
六、在研项目（自2016年1月起）
国家自然科学基金重点基金培育项目：蛋氨酸气-液-固三相连续反应结晶过程中介尺度机制及调控，91634117，刘伯潭，16.75万
齐鲁安替丙酮/乙醇尾气VOC处理新工艺开发，刘伯潭，40万
盐穴储气库水溶造腔模拟软件开发，刘伯潭，11万
低成本低能耗燃煤电厂烟气CO2捕集技术开发，刘伯潭，60万
国家重点实验室开放基金：多产品隔板精馏塔动态行为规律研究，盖晓龙，10万
企业委托项目-先进精馏技术开发，盖晓龙，150万
山东鸿达生物科技有限公司2万吨/年杂醇油处理工艺开发，王红星，50万
年产10000吨电子级碳酸甲乙酯/碳酸二乙酯联产新工艺开发，18万
高纯碳酸酯工艺节能优化技术支持项目，40万
七、 论文发表(第一作者/通讯作者)
(1)Liu Botan, Wen Yantong, Liu Chunjiang, Sun Bo, Yuan Xigang, Multiscale Calculation on Perforated Sheet Structured Packing To Predict the Liquid Distribution Based on Computational Fluid Dynamics Simulation. Industrial & Engineering Chemistry Research, 2016, 55(28): 7810-7818.
(2) Botan liu, Yantong Wen, Xuegang Zhang, Development of CAMD based on the hybrid gene algorithm and simulated annealing algorithm and the application on solvent selection, The Canadian journal of Chemical Engineeing, 2016, DOI:10.1002/cjce.22724
(3)Liu Botan and Liu Chunjiang, Three Dimensional Simulation of Liquid Flow on Distillation Tray, Chinese Journal of Chemcial Engineering, 2002, 10(5): 517~521
(4)胡威，陈淑勇，刘伯潭*，HNO自由基与O2反应机理的理论研究，无机化学学报，2016,32(10):1757-1762
（5）Kai Guo; Chunjiang Liu; Botan Liu*;Shuyong Chen, Modeling with statistical hydrodynamic quantity of mass transfer across gas-liquid interface with Rayleigh convection, Chemical Engineering Science, 2015, 135:33-44
（6）Li Wenbin, Liu Botan*, A Reynolds Mass Flux Model for the Simulation of Chemical Absorption of CO2 into 2-Amino-2-methyl-1-propanol in a Packed Column, Industrial & Engineering Chemistry Research, 2015, 54(4):1385-1396
（7）Guo Kai, Liu Chunjiang, Chen Shuyong, Fu Bo, Liu Botan*, Spatial Scale Effects on Rayleigh Convection and Interfacial Mass Transfer Characteristics in CO2 Absorption, Chemical Engineering Technology, 2015, 38(1):23-32
(8) Li Wenbin, Zhao Xingjian, Liu Botan*, Tang Zhongli,Mass Transfer Coefficients for CO2 Absorption into Aqueous Ammonia Using Structured Packing, Industrial & Engineering Chemistry Research, 2014,53(14):6185-6196
(9) Sun B., He L., Liu B. T.*, Gu F., Liu C. J.,A new multi-scale model based on CFD and macroscopic calculation for corrugated structured packing column, AIChE Journal, 2013, 59(8):3119-3130
(10) Li W. B., Liu B. T.*, Yu K. T., Yuan X. G.,Rigorous Model for the Simulation of Gas Adsorption and Its Verification, Industrial & Engineering Chemistry Research, 2011, 50(13):8361-8370
(11)Xiaolong Ge, Xigang Yuan*, Chen Ao, Kuo-Ksong Yu, Simulation based approach to optimal design of dividing wall column using random search method. Computers & Chemical Engineering 2014, 68, 38-46.
(12)Xiaolong Ge, Chen Ao, Xigang Yuan*, Yiqing Luo, Investigation of the Effect of the Vapor Split Ratio Decision in Design on Operability for DWC by Numerical Simulation. Industrial & Engineering Chemistry Research. 2014, 53, 13383-13390.
(13)Liu botong, Liu botan*, Ge Xiaolong*, Yuan Xigang ,Validation of Simulation and Mass Transfer Coefficient Prediction with Interfacial Convection. Chemical Engineering & Technology ,2017, accepted.
(14)Ge Xiaolong, Liu Botong, Yuan Xigang*, Luo Yiqing,Yu Kuo-Ksong, Application of the dividing wall column to olefin separation in fluidization methanol to propylene (FMTP) process. Chinese Journal of Chemical Engineering, accepted.
(15) Wang H.X., Wu C. M., Bu X. W., Tang W. L., Li L., Qiu T., A benign preparation of sec-butanol via transesterification from sec-butyl acetate using the acidic Imidazolium ionic liquids as catalysts. Chemical Engineering Journal, 2014, 246: 366-372.
(16) Wang H. X., Bu X.W., Huang Z.X., Yang J.B., Qiu T., Synthesis of methacrylic anhydride by batch reactive distillation: reaction kinetics and process. Industrial & Engineering chemistry Research, 2014, 53(44): 17317-17324.
(17) Wang H. X., Li L., Ye C. S., Isobaric vapor-liquid equilibria of the binary system acetone + acetone oxime methyl ether at 101.3 kPa, Fluid Phase Equilibria, 2013, 342(1): 42-46.
(18) Wang H. X., Xiao J. J., Shen Y. Y., Ye C. S., Li L., Qiu T., Experimental measurements of vapor - liquid equilibrium data for the binary systems of methanol + 2-butyl acetate, 2-butyl alcohol + 2-butyl acetate and methyl acetate + 2-butyl acetate at 101.33 kPa, Journal of Chemical Engineering Data, 2013, 58(6): 1827-1832.
(19) Wang H. X., Li L., Ye, C. S., Isobaric vapor–liquid equilibria of the binary system acetone+ acetone oxime methyl ether at 101.3 kPa, Fluid Phase Equilibria, 2013, 342: 42-46.