Extractive Distillation with Ionic Liquid Entrainers for the Separation of Acetonitrile and Water

被引:44
作者
Li, Jinlong [1 ,2 ]
Li, Tingting [3 ,4 ]
Peng, Changjun [3 ,4 ]
Liu, Honglai [3 ,4 ]
机构
[1] Changzhou Univ, Jiangsu Key Lab Adv Catalyt Mat & Technol, Changzhou 213164, Peoples R China
[2] Changzhou Univ, Sch Petrochem Engn, Changzhou 213164, Peoples R China
[3] East China Univ Sci & Technol, State Key Lab Chem Engn, 130 Meilong Rd, Shanghai 200237, Peoples R China
[4] East China Univ Sci & Technol, Dept Chem, 130 Meilong Rd, Shanghai 200237, Peoples R China
基金
中国国家自然科学基金;
关键词
DEEP EUTECTIC SOLVENTS; COSMO-RS; CONCEPTUAL DESIGN; EQUILIBRIUM DATA; MIXTURE; SYSTEM; ACETATE; TEMPERATURE; PREDICTION; RECOVERY;
D O I
10.1021/acs.iecr.8b05907
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
Ionic liquids (ILs) of 1-ethyl-3-methylimidazolium acetate ([EMIM][OAC]), 1-ethyl-3-methylimidazolium proline ([EMIM][PRO]), and N,N,N-dimethyl-butylethanol amine glycolic acid ([N1,1,4C2OH][GAC]) are selected as entrainers for the extractive distillation to separate the mixture of acetonitrile and water based on the COSMO-RS method. The isobaric vapor-liquid equilibrium of ternary mixtures containing ILs at atmospheric pressure is determined, verifying that the used ILs can break the azeotropy of acetonitrile and water. On the basis of the thermodynamic analysis, a typical extractive distillation process is designed with Aspen Plus to evaluate the competitiveness of IL entrainers in separation performance. Significant savings of entrainer and energy, in which the solvent ratios in moles reduce from 0.94 to 0.09, 0.12, and 0.12 and the overall heat duties on the reboiler decrease 24.9, 17.5, and 15.4% for [EMIM] [OAC], [EMIM] [PRO], and [N1,1,4C2OH] [GAG], respectively, can be achieved compared with those of ethylene glycol used as the entrainer.
引用
收藏
页码:5602 / 5612
页数:11
相关论文
共 80 条
[1]   Novel solvent properties of choline chloride/urea mixtures [J].
Abbott, AP ;
Capper, G ;
Davies, DL ;
Rasheed, RK ;
Tambyrajah, V .
CHEMICAL COMMUNICATIONS, 2003, (01) :70-71
[2]   Phase behavior in quaternary ammonium ionic liquid-propanol solutions: Hydrophobicity, molecular conformations, and isomer effects [J].
Abe, Hiroshi ;
Kohki, Erica ;
Nakada, Ayumu ;
Kishimura, Hiroaki .
CHEMICAL PHYSICS, 2017, 491 :136-142
[3]   A thermodynamic study on binary and ternary mixtures of acetonitrile, water and butyl acetate [J].
Acosta, J ;
Arce, A ;
Rodil, E ;
Soto, A .
FLUID PHASE EQUILIBRIA, 2002, 203 (1-2) :83-98
[4]   Recovery of acetonitrile from aqueous waste by a combined process:: Solvent extraction and batch distillation [J].
Acosta-Esquijarosa, Jhoany ;
Rodriguez-Donis, Ivonne ;
Jauregui-Haza, Ulises ;
Nuevas-Paz, Lauro ;
Pardillo-Fontdevila, Eladio .
SEPARATION AND PURIFICATION TECHNOLOGY, 2006, 52 (01) :95-101
[5]   A simple group contribution correlation for the prediction of ionic liquid heat capacities at different temperatures [J].
Ahmadi, Alireza ;
Haghbakhsh, Reza ;
Raeissi, Sona ;
Hemmati, Vahid .
FLUID PHASE EQUILIBRIA, 2015, 403 :95-103
[6]  
[Anonymous], 2010, COSMOTHERMX VERSION
[7]   Prediction of binary VLE for imidazolium based ionic liquid systems using COSMO-RS [J].
Banerjee, T ;
Singh, MK ;
Khanna, A .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 2006, 45 (09) :3207-3219
[8]   VAPOR-LIQUID EQUILIBRIA OF SYSTEM ACRYLONITRILE-ACETONITRILE-WATER [J].
BLACKFORD, DS ;
YORK, R .
JOURNAL OF CHEMICAL AND ENGINEERING DATA, 1965, 10 (04) :313-+
[9]   Ionic liquid 1-ethyl-3-methylimidazolium tetracyanoborate: An efficient entrainer to separate methanol dimethyl carbonate azeotropic mixture [J].
Blahut, Ales ;
Dohnal, Vladimir .
FLUID PHASE EQUILIBRIA, 2016, 423 :120-127
[10]   Sweet success: ionic liquids derived from non-nutritive sweeteners [J].
Carter, EB ;
Culver, SL ;
Fox, PA ;
Goode, RD ;
Ntai, I ;
Tickell, MD ;
Traylor, RK ;
Hoffman, NW ;
Davis, JH .
CHEMICAL COMMUNICATIONS, 2004, (06) :630-631