[1] SEADER J D, HENLEY E J. Separation process principles [M]. 2nd edition. New York: John Wiley & Sons. [2] WANG M, CHANG R, CHEU T. Analysis of absorption-stripping processes with split-flow cycles for energy saving[J]. Journal of the Chinese Institute of Chemical Engineers, 1985, 16(1): 1-9. [3] 刘练波,黄斌. 燃煤电站3 000-5 000 t/a CO 2 捕集示范装置工艺及关键设备[J]. 电力设备,2008,9(5):21-24. LIU Lian-bo, HUANG Bin. A pilot plant process and key equipment for capture CO 2 3 000~5 000 t/a in coal-fired power station [J]. Electrical Equipment, 2008, 9(5): 21-24. [4] 黄斌,刘练波,许世森. CO 2 的捕获和封存技术进展[J]. 中国电力,2007,40(3):14-17. HUANG Bin, LIU Lian-bo, XU Shi-sen. Evolution of CO 2 capture and sequestration technology[J]. Electric Power, 2007, 40(3): 14-17. [5] 时钧,汪家鼎,余国琮,等. 化学工程手册 上卷[M]. 2版. 北京:化学工业出版社,1996:12-38. [6] WANG M, WEI S. Energy conservation of absorption-stripping processes with split-flow cycles[J]. Journal of the Chinese Institute of Chemical Engineers, 1984, 15(1): 111-120. [7] DOUGLAS J M. Conceptual design of chemical processes [M]. New York: McGraw-Hill, 1988. [8] HUANG Bin, XU Shi-sen, GAO Shi-wang, et al . Preliminary results and operational cost analysis of CO 2 capture at the Huaneng Beijing coal-fired power plant [J]. Applied Energy, 2010, 87(11): 3347-3354. [9] DAVE N, DO T, PALFREYMAN D, et al . Post-combustion capture of CO 2 from coal-fired power plants in China and Australia: an experience based cost comparison[J]. Energy Procedia, 2011, 4: 1869-1877. |