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	Energy-saving nonequilibrium thermodynamic analysis for distillation - Mathematical model development
	Liu, QL ; Liu QL(刘庆林) ; Li, P ; Li P(李鹏) ; Zhang, ZB ; Zhang ZB(张志炳)
	2001
关键词	nonequilibrium thermodynamics mathematical model energy-saving analysis distillation
英文摘要	A general thermodynamic model was presented by analyzing distillation processes. The mass transfer in these processes was assumed in an irreversible thermodynamic state during the model development. The simulated results showed that this model could be applied not only to analyzing entropy generation in distillation processes, but also to compare the effects of the tray parameters on the entropy generation in a column, with which energy-saving distillation tower can thus be designed and the distillation operation can be controlled in an optimal mode.
语种	中文
出版者	HIGHER EDUCATION PRESS
内容类型	期刊论文
源URL	[http://dspace.xmu.edu.cn/handle/2288/12598]
专题	化学化工－已发表论文
推荐引用方式 GB/T 7714	Liu, QL,Liu QL,Li, P,et al. Energy-saving nonequilibrium thermodynamic analysis for distillation - Mathematical model development[J],2001.
APA	Liu, QL,刘庆林,Li, P,李鹏,Zhang, ZB,&张志炳.(2001).Energy-saving nonequilibrium thermodynamic analysis for distillation - Mathematical model development..
MLA	Liu, QL,et al."Energy-saving nonequilibrium thermodynamic analysis for distillation - Mathematical model development".(2001).

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