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化学工业与工程 2014, Vol. 31 Issue (5) :65-69    DOI: doi: 10.13353/j.issn.1004.9533.2014.05.012
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丁酮-水共沸物系的萃取分离
田征,冯天扬,崔现宝,彭艳枚,薛乐星,包振宇
(天津大学化工学院 化学工程联合国家重点实验室,天津 300072)
Separation of Methyl Ethyl Ketone-Water Azeotropic System via Extraction
TIAN  Zheng, FENG  Tian-Yang, CUI  Xian-Bao, PENG  Yan-Mei, XUE  Le-Xing, BAO  Zhen-Yu
(State Key Laboratory of Chemical Engineering(Tianjin University), School of Chemical Engineering and Technology, Tianjin University, Tianjin 300072, China)

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摘要 采用液液萃取进行丁酮-水共沸物系的分离。测定了三元体系丁酮-水-(1-乙基-3-甲基咪唑醋酸盐)的液液平衡,采用NRTL活度系数方程对液液平衡数据进行回归得到组分间的二元交互作用参数。利用流程模拟软件ChemCAD进行了以离子液体为萃取剂的液液萃取过程的模拟,研究了理论板数、溶剂比(萃取剂摩尔流量和原料摩尔流量的比值)对萃取过程的影响,通过灵敏度分析,获得了优化的操作参数。在最适宜操作条件下,丁酮的摩尔分数可达0.999 4,离子液体经过回收能够直接循环使用。
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田征
冯天扬
崔现宝
彭艳枚
薛乐星
包振宇
关键词丁酮      离子液体   萃取   模拟   液液平衡     
Abstract: The azeotropic system of methyl ethyl ketone(MEK)-water was separated by extraction. The liquidliquid equilibrium of the ternary system of methyl ethyl ketone-water-(1-ethyl-3-methylimidazolium acetate) was measured. The liquid-liquid equilibrium data were correlated by NRTL activity coefficient model and the binary interaction parameters were obtained. The extraction process was simulated using ChemCAD simulation software with ionic liquid as solvent. The effects of the number of theoretical stages and solvent ratio(the ratio of the molar flow rate of solvent to feed) on the extraction process were investigated. The optimal operation parameters were obtained by the sensitivity analysis, and the purity of MEK could reach 0.999 4 in such conditions, and the ionic liquid was able to be recycled after recovery.
Keywordsmethyl ethyl ketone   water   ionic liquids;   extraction   simulation   ChemCAD     
Received 2013-05-24;
Corresponding Authors: 崔现宝,电话:(022)27404493,E-mail:cxb@tju.edu.cn。      Email: cxb@tju.edu.cn
About author: 田征(1989-),男,硕士研究生,现从事离子液体反应精馏研究。
引用本文:   
田征, 冯天扬, 崔现宝, 彭艳枚, 薛乐星, 包振宇.丁酮-水共沸物系的萃取分离[J].  化学工业与工程, 2014,31(5): 65-69
TIAN Zheng, FENG Tian-Yang, CUI Xian-Bao, PENG Yan-Mei, XUE Le-Xing, BAO Zhen-Yu.Separation of Methyl Ethyl Ketone-Water Azeotropic System via Extraction[J].  Chemcial Industry and Engineering, 2014,31(5): 65-69
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