河北工业大学化工学院

李春利

2017/4/25 14:49:41 人评论 次浏览 分类:博士生导师

       李春利,男,1963年出生于唐山玉田,工学博士,教授,博士生导师,化学工程学科学术带头人;全国模范教师、国务院特殊津贴专家、河北省巨人团队领军人物、河北省高端人才(院士后备人才)、天津市创新创业人才。主要从事高效传质装备研发、分离与纯化技术、反应分离集成技术、化工过程系统工程及节能减排等方面的研究。

       作为课题负责人先后完成了国家重大科技攻关项目“大通量高效立体传质塔板技术与设备的开发”,国家西部大开发以及其他科研项目120多项。带领课题组研究开发了“新型立体传质塔板技术及其在化工行业的应用”、“化工过程集成及能量综合利用技术”等多项科研成果,申请发明专利近50多项,获得授权发明专利26项,发表论文150多篇,其中SCI/EI检索43篇。

       系列技术成果已经广泛应用于石化、化工、制药等行业的挖潜改造、节能、环保等项目中。二十多年来在国内30个省市及印度、古巴等国家的大中型企业应用已经超过3000套,有效地解决了生产中的瓶颈难题,对企业产品质量的升级换代具有极大的推动作用。同时,在降低原材料消耗、降低能耗、减少环境污染等方面的社会效益也十分显著。近几年为企业创造的经济效益已超过150亿元。

       作为优秀资源共享课程、河北省精品课程《化工原理》负责人,教学成果曾获得河北省教学成果一、二等奖,天津市教学成果二等奖等。个人先后获得“天津市课堂教学基本功竞赛一等奖”、“五一劳动奖章”、“八五立功奖章”、“教师楷模”等称号。


获奖:

1、 国家科技进步二等奖,2012年,第一完成人。

2、 河北省技术发明一等奖,2015年,第一完成人。

3、 河北省科学技术突出贡献奖,2006年,第一完成人。

4、 天津市科技进步一等奖,2004年,第一完成人。

5、 河北省科技进步一等奖,1999年,第一完成人。


代表性论文:

1. Fang, J., Y. Hu, and C. Li, Energy-Saving Mechanism in Heat Transfer Optimization of Dividing Wall Column. Industrial & Engineering Chemistry Research, 2013. 52(51): p. 18345-18355.

2. Fang, J., et al., A Quasi-steady-state Model for Numerical Simulation of Batch Extractive Distillation. Chinese Journal Of Chemical Engineering, 2010. 18(1): p. 43-47.

3. Fang, J., et al., Isobaric Vapor-Liquid Equilibrium for the Acetonitrile plus Water System Containing Different Ionic Liquids at Atmospheric Pressure. Journal Of Chemical And Engineering Data, 2013. 58(6): p. 1483-1489.

4. Fang, J., et al., Energy conserving effects of dividing wall column. Chinese Journal Of Chemical Engineering, 2015. 23(6): p. 934-940.

5. Fang, J., et al., Salting-out effect of ionic liquids on isobaric vapor-liquid equilibrium of acetonitrile-water system. Chinese Journal Of Chemical Engineering, 2015. 23(8): p. 1369-1373.

6. He, L., et al., Spray Characteristics Study of Combined Trapezoid Spray Tray. China Petroleum Processing & Petrochemical Technology, 2014. 16(3): p. 104-110.

7. He, L., S. Zhang, and C. Li, Experimental study of desulfurizaiton performance of spouted bed with porous draft tube, in Progress In Environmental Science And Engineering, H. Li, Q.J. Xu, and D. Zhang, Editors. 2012. p. 1050-1054.

8. Lu, J., et al., Kinetics of Forward Extraction of Boric Acid from Salt Lake Brine by 2-Ethyl-1,3-hexanediol in Toluene Using Single Drop Technique. Chinese Journal Of Chemical Engineering, 2014. 22(5): p. 496-502.

9. Wang, H., et al., Response surface optimization of the operating parameters for a complex distillation column based on process simulation. Energy Procedia, 2012. 16: p. 571-578.

10. Wang, H., C. Li, and C. Li, RSM optimization of the operating parameters for a butanol distillation column. Asia-Pacific Journal Of Chemical Engineering, 2012. 7(1): p. 117-123.

11. Zhang, W., et al., Measurement and Correlation of Vapor-Liquid Equilibria for Hexamethyl Disiloxane plus Vinyl Acetate System at 101.3 kPa. Chinese Journal Of Chemical Engineering, 2014. 22(2): p. 177-180.

12. Zhang, W., et al., Progress in adjustment of ionic liquids acidity based on the alkylation. Advanced Materials Research, 2013. 634-638(1): p. 581-586.

13. Zhang, W., et al., Progress in adjustment of ionic liquids acidity based on the alkylation, in Advances In Chemical, Material And Metallurgical Engineering, Pts 1-5, J.M. Zeng, H.X. Zhu, and J.Y. Kong, Editors. 2013. p. 581-586.

14. Zhang, W., et al., Determination and Correlation of Vapor-Liquid Equilibrium Data for the Ethyl Acetate plus Hexamethyl Disiloxane System at 101.3 kPa. Journal Of Chemical And Engineering Data, 2011. 56(12): p. 5078-5080.

15. Zhang, W., et al., Isobaric vapor-liquid equilibria of Hexamethyl Disiloxane plus Ethyl Acetate System at Normal Pressure, in Advances In Chemical Engineering, Pts 1-3, Y.X. Wen and F.H. Lei, Editors. 2012. p. 968-972.

16. Zhang, W., et al., Isobaric Vapor-Liquid Equilibrium for the Binary System of Hexamethyl Disiloxane plus Isopropyl Acetate at Atmospheric Pressure. Journal Of Chemical And Engineering Data, 2013. 58(9): p. 2425-2428.

17. Zhang, W., et al., Metal chlorides or sulfuric acid in ionic liquid solvents convert catechol to p-tert-Butylcatechol. Catalysis Communications, 2015. 65: p. 113-116.