[1] 任海伦,安登超,朱桃月,等. 精馏技术研究进展与工业应用[J]. 化工进展,2016,35(6):1606-1626.
[2] Van De Bor D M, Infante Ferreira C A, Kiss A A. Low grade waste heat recovery using heat pumps and power cycles[J]. Energy, 2015, 89: 864-873.
[3] Annakou O, Mizsey P. Rigorous investigation of heat pump assisted distillation[J]. Heat Recovery Syst Chp, 2015, 15(3): 241-247.
[4] 李沐荣,许良华,辛春伟,等. 热泵精馏隔壁塔分离宽沸程物系的模拟[J]. 化工学报,2017,68(5):1906-1912.
[5] Felbab N, Patel B, El-Halwagi M M, et al. Vapor recompression for efficient distillation. A new synthesis perspective on standard configurations[J]. AIChE Journal, 2013, 59(8): 2977-2992.
[6] Kumar V, Kiran B, Jana A K. A novel multistage vapor recompression reactive distillation system with intermediate reboilers[J]. AIChE Journal, 2013, 59(3): 761-771.
[7] 丁良辉,刘从容,李乾军,等. 外部反应精馏强化的环氧乙烷制乙二醇工艺模拟及其热泵节能研究[J]. 石油学报(石油加工),2017,33(3):563-570.
[8] 唐超,胡存,陈亚中,等. 热泵精馏应用于异丁烷精馏过程的节能改造[J]. 化工进展,2015,34(2):581-585.
[9] Wentink A E, Kyipers N J M, Haan A B D, et al. Olefin isomer separation by reactive distillation: modeling of vapor-liquid equilibria and conceptual design for 1-hexene purification[J]. Chemical Engineering and Processing, 2007, 46(9): 800-809.
[10] 孙兰义.化工过程模拟实训—Aspen Plus教程[M]. 北京:化学工业出版社,2017,336-377.
[11] 肖汉. 从抽余碳四生产高纯度异丁烯流程模拟与优化[D]. 华东理工大学硕士学位论文,上海,2010.
[12] 叶庆国. 分离工程[M]. 北京:化学工业出版社,2008,187-208.
[13] Lujic ?, Sun L, De Rijke A, et al. Conceptual design of an internally heat integrated propylene-propane splitter[J]. Energy, 2006, 31(15): 3083-3096.
[14] Douglas J M. Conceptual design of chemical processes[M]. McGraw-Hill New York, 1988.
[15] 李萱. 热耦合精馏工艺设计与经济性分析[D]. 天津大学硕士学位论文,天津,2015.