Application of CAMD in separating hydrocarbons by extractive distillation

被引:55
作者
Chen, BH [1 ]
Lei, ZG [1 ]
Li, QS [1 ]
Li, CY [1 ]
机构
[1] Beijing Univ Chem Technol, Minit Educ, Key Lab Sci & Technol Controllable Chem React, Beijing 100029, Peoples R China
关键词
computer-aided molecular design (CAMD); extractive distillation; relative volatility; hydrocarbons; application;
D O I
10.1002/aic.10562
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
The solvent is the core of extractive distillation, and a suitable solvent plays an important role in the economical design of extractive distillation. Computer-aided molecular design (CAMD) has been applied to rapidly screen the solvents for separating hydrocarbons by extractive distillation. The systems of propane/propylene, n-butane/l-butene, and n-heptane/benzene, respectively, as the representatives of C3, C4, and C6 hydrocarbons were investigated, and the potential solvents were selected by means of CAMD. The designed results were further proven by experiments and process simulation. The mechanism for separating hydrocarbons by extractive distillation is based on the different fluidities of the electron cloud of C-C (no double bond), C=C (one double bond), and ACH (aromatic carbon ring) bonds and thus different interactions between solvent and hydrocarbon molecules. To improve the separation ability of the main solvent, one strategy is to add some additive that can form hydrogen bonding with the main solvent to make into a mixture. (c) 2005 American Institute of Chemical Engineers.
引用
收藏
页码:3114 / 3121
页数:8
相关论文
共 37 条
[2]  
Chen BH, 2003, J CHEM ENG JPN, V36, P20
[3]   Novel mathematical programming model for computer aided molecular design [J].
Churi, N ;
Achenie, LEK .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 1996, 35 (10) :3788-3794
[4]   PREDICTION OF HEAT AND FREE ENERGIES OF ORGANIC COMPOUNDS [J].
FRANKLIN, JL .
INDUSTRIAL AND ENGINEERING CHEMISTRY, 1949, 41 (05) :1070-1076
[5]   A GROUP CONTRIBUTION APPROACH TO COMPUTER-AIDED MOLECULAR DESIGN [J].
GANI, R ;
NIELSEN, B ;
FREDENSLUND, A .
AICHE JOURNAL, 1991, 37 (09) :1318-1332
[6]   MOLECULAR DESIGN OF SOLVENTS FOR LIQUID EXTRACTION BASED ON UNIFAC [J].
GANI, R ;
BRIGNOLE, EA .
FLUID PHASE EQUILIBRIA, 1983, 13 (OCT) :331-340
[7]   Requirements of thermodynamic data in the chemical industry [J].
Zeck, S. ;
Wolf, D. .
Fluid Phase Equilibria, 1993, 82 (pt 1) :27-38
[8]   A modified UNIFAC (Dortmund) model. 4. Revision and extension [J].
Gmehling, J ;
Wittig, R ;
Lohmann, J ;
Joh, R .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 2002, 41 (06) :1678-1688
[9]   VAPOR-LIQUID-EQUILIBRIA BY UNIFAC GROUP CONTRIBUTION - REVISION AND EXTENSION .2. [J].
GMEHLING, J ;
RASMUSSEN, P ;
FREDENSLUND, A .
INDUSTRIAL & ENGINEERING CHEMISTRY PROCESS DESIGN AND DEVELOPMENT, 1982, 21 (01) :118-127
[10]   A modified UNIFAC (Dortmund) model. 3. Revision and extension [J].
Gmehling, J ;
Lohmann, J ;
Jakob, A ;
Li, JD ;
Joh, R .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 1998, 37 (12) :4876-4882