SCHOOL OF CHEMICAL ENGINEERING

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教授

秦英杰

现任职称/职务:教授,博士生导师
通讯地址:天津市津南区海河教育园区雅观路135号天津大学50楼C-511
电子邮箱:yjqin@tju.edu.cn
办公电话:15522500168

论著专利:


2009年归国任教后作为通讯作者发表的主要文章:

[1]  Q. Li, Y. J. Qin , Y.F. Liu, J.J. Liu, Q. Liu, P.L. Li, L. Q. Liu. Detoxification and Concentration of Corn Stover  Hydrolysate and Its Fermentation for Ethanol Production。 Frontiers of Chem. Sci. & Eng.,13(2019): 140-151.

[2]  Y. F. Liu, Y. J. Qin , Q. Li, Y. Wang, Y. Zhang, L.C. Zhang, L.Q. Liu. A reversible absorption-based supported gas membrane process for enriching bromine from brine by using thin PTFE hollow fibers, J. Membr. Sci. 543 (2017): 222–232.

[3]   J. J. Liu, Y. J. Qin, P. L. Li, K. M. Zhang, Q. Liu, L. Q. Liu. Separation of the Acidsugar Mixtures by Using Acid Retardation and further Concentration of the Eluents by Using CEMD, Journal of chemical technology and biotechnology, 2016, 91 (4) :1105-1112.

[4]   J. He, H. Q. Liu, P. F. Shan, K. M. Zhang, Y. J. Qin, L. Q. Liu. Supported-Gas-Membrane Process for Removal and Recovery of Aliphatic Amines from Aqueous Streams, Chemical Engineering Science, 141 (2016): 330-341.

[5]   J. He, L. L. Zhang; K. M. Zhang, Y. J. Qin,  L. Q. Liu. Concentrating aqueous urea solution by using continuous-effect membrane distillation, Chemical Engineering Research and Design, 104 (2016): 589-604.

[6]   K. M. Zhang, Y. J. Qin, F. He, J. J. Liu, Y. Zhang, L. Q. Liu. Concentration of aqueous glycerol solution by using continuous-effect membrane distillation,Separation and Purification Technology, 2015, 144:186-196.

[7]  K. Yao, Y. J. Qin, Y. J. Yuan, L. Q. Liu, F. He, Y. Wu. A Continuous-Effect Membrane Distillation Process Based on Hollow Fiber AGMD Module with Internal Latent-Heat Recovery, AIChE J., 2013,59(4):1278-1297.

[8]  X. J. Li, Y. J. Qin, R. L. Liu, Y. P. Zhang, K. Yao. Study on concentration of aqueous sulfuric acid solution by multiple-effect membrane distillation, Desalination, 2012,(307):34-41.

[9]   R. L. Liu, Y. J. Qin, X. J. Li, L. Q. Liu, Concentrating Aqueous Hydrochloric Acid by MultipleEffect Membrane Distillation, Front. Chem. Sci. Eng., 2012,6(3):311-321.  

[10]   R. Ban, M. M. Liu, Y. J. Qin, H. Wang, D. S. Cui. Enrichment of Semi-volatile Organic Acids from Aqueous Solutions by Multiple-Effect Membrane Distillation, Transactions of Tianjin University, 2012,18:320-329.

[11]  赵建敏, 秦英杰, 李旭超, 刘立强, 崔东胜, 张艳萍. 料液中盐对气态膜法脱氨

过程的影响[J].化工学报, 2012,63(4):1108-1115.

[12]  秦英杰,刘立强,何菲,张艳萍,吴茵,王世昌. 内部热能回收式多效膜蒸馏用于海水淡化及浓盐水深度浓缩[J].膜科学与技术, 2012,32(2):59-64.

[13]  秦英杰, 王焕, 刘立强, 崔东胜, 吴松松. 经反渗透处理后炼油废水浓水的多效 膜蒸馏技术[J].化工进展, 2011,30:844-848.

[14] 王焕, 秦英杰, 刘立强, 崔东胜. 多效膜蒸馏技术用于果汁浓缩[J].化学工业与工程, 2012,29(4):50-57.        

[15] 何杰, 张莉莉, 单鹏飞, 秦英杰. 多效膜蒸馏技术分离尿素水溶液的研究[J].水处理技术, 2012,38(7):75-78.

[16] 何杰, 单鹏飞, 张莉莉, 秦英杰. 气态膜吸收分离二甲胺水溶液的研究[J].环境科学学报, 2012,32(10):2360-2365.

[17] 李晓君, 秦英杰, 刘荣玲, 崔东胜, 刘立强. 利用多效膜蒸馏技术浓缩硫酸和磷酸水溶液[J]. 化学工业与工程, 2013, 30(4):55-62.

[18] 王奔, 秦英杰, 王彬, 靳军宝, 刘立强. 多效膜蒸馏过程用于海水和浓海水的深度浓缩[J]. 化工进展,32(9):2233-2241.

[19] 解利昕, 王元喜, 秦英杰, 郝兴阁, 李海庆, 刘立强. 盐酸作吸收剂用于气态膜法从废水中脱除/回收氨氮[J]. 化工进展,32(10):2507-2513.

[20] 刘晶, 王平, 秦英杰, 王奔, 刘立强, 崔东胜.钢铁废水经反渗透处理后浓水的多效膜蒸馏法深度浓缩[J].全国苦咸水淡化技术研讨会论文集, 2013, 128-132.

[21] 郝兴阁, 王元喜, 李海庆, 秦英杰, 刘立强, 崔东胜. 稀硝酸作吸收剂的气态膜法回收废水中氨氮的研究[J]. 化学工业与工程, 2015, 32(2):43-49.

[22] 李海庆, 秦英杰, 崔东胜, 蔡腾豪, 郝兴阁, 王元喜. 支撑气膜法脱除/回收垃圾渗滤液中氨氮[J]. 环境工程学报, 2014,8(2):612-618.

[23] 王彬, 秦英杰, 崔东胜, 刘立强, 王奔,  靳军宝. 多效膜蒸馏技术浓缩回收废水中的二甲基亚砜[J]. 环境工程学报, 2014,8(3):1091-1098.

[24] 靳军宝, 秦英杰, 王奔, 王彬, 崔东胜, 刘立强.多效膜蒸馏用于处理高盐溶液的实验研究[J]. 化学工业与工程, 2014,31(2):31-37.

[25] 王平, 秦英杰, 刘晶, 刘建军, 张昆明, 崔东胜. 多效膜蒸馏用于深度浓缩多种无机盐水[J]. 膜科学与技术, 2014, 34(4):39-44.

[26] 刘晶, 秦英杰, 王平, 王奔, 崔东胜. 刘立强.多效膜蒸馏技术用于氢氧化钠稀溶液的浓缩[J]. 工业水处理,2014, 34(11):73-76.

[27] 刘青,秦英杰,刘建军,张云,刘立强,崔东胜. 多效膜蒸馏法秸秆酸水解液脱毒及糖浓缩[J]. 膜科学与技术,2015, 35(6):99-105.

[28] 王云,秦英杰,郝兴阁,李海庆,崔东胜,刘立强,刘晶. 可逆气态膜-多效膜蒸馏-精馏过程脱除水相氨氮副产氨水[J]. 化工学报,2015, 66(9): 3588-3596.

[29] 张云, 秦英杰,刘青,刘晶,刘立强. 聚四氟乙烯中空纤维气态膜法浓海水提取溴素[J]. 化学工业与工程,2016, 33(6):56-63。


1991-2008国外期间发表的主要文章:

[1]  S. C. Wang, S. C. Xu, Y. J. Qin. Mass Transfer in Membrane Absorption-Desorption of Ammonia from Ammonia Water. Chinese J. Chem. Eng. (English Ed.), 1993, 1(3):160-170.

[2]  Y. J. Qin, J. M. S. Cabral. Kinetic studies of the urease-catalyzed hydrolysis of

urea in a buffer-free system. Appl. Biochem. Biotechnol., 1994, 49:217-240.

[3]  Y. J. Qin, J. M. S. Cabral, S. C. Wang. Hollow Fiber Gas-Membrane Process for Removal of NH3 from Solution of NH3 and CO2. AIChE J., 1996, 42(7):1945-1956.

[4]  Y. J. Qin, J. M. S. Cabral. Comparison Between SGM and SLM for the Separation of NH3 from Aqueous Solution of NH3 and CO2. J. Chem. Technol. Biotechnol., 1996, 67, 323-328.

[5]  Y. J. Qin, J. M. S. Cabral. Hollow Fiber SLM Separation for the Separation of NH3 from Aqueous Media Containing NH3 and CO2. J. Chem. Technol. Biotechnol., 1996, 65:137-148.

[6]  Y. J. Qin, J. M. S. Lumen Mass Transfer in Hollow Fiber Membrane Processes with Constant External Resistances. AIChE J., 1997, 43(8), 1975-1988.

[7]  Y. J. Qin, J. M. S. Cabral. Mass Transfer in Hollow-Fiber Membrane with Nonlinear Boundary Conditions. AIChE J., 1998, 44(4):836-848.

[8]  Y. J. Qin, J. M. S. Cabral. Influence of the Nernst-Planck Diffusion on Hollow Fiber Membrane Mass-Transfer Processes. AIChE J., 1998, 44(7):1529-1541.

[9]  Y. J. Qin, J. M. S. Cabral. Theoretical Analysis on the Design of Hollow Fiber Modules and Modules Cascades. Journal of Membrane Science, 1998, 143:197-205.

[10] Y. J. Qin, Sheth J. P., Sirkar. K. K.. Supported Liquid Membrane-Based Pervaporation for VOC Removal from Water. Ind. Eng. Chem. Res., 2002, 41:3413-3428.

[11] Y. J. Qin, J. M. S. Cabral. Review Properties and Applications of Urease. Biocatalysis and Biotransformation, 2002, 20(1):1-14.

[12] R. M. Cowan, J. J. Ge, Y. J. Qin, M. L. McGregor, M. C. Trachtenberg, CO2 capture by means of an enzyme-based reactor. Annals New York Academy Sci., 2003, 984:453-469.

[13] J. P. Sheth, Y. J. Qin, K. K. Sirkar, B. C. Baltzis. Nanofiltration-based diafiltration process for solvent exchange in pharmaceutical manufacturing. Journal of Membrane Science, 2003,211:251-261.

[14] Y. J. Qin, J. P. Sheth, K. K. Sirkar. Pervaporation Membranes That Are Highly Selective for Acetic Acid over Water. Ind. Eng. Chem. Res., 2003, 42, 582-595.