ETHERS FROM ETHANOL .1. EQUILIBRIUM THERMODYNAMIC ANALYSIS OF THE LIQUID-PHASE ETHYL TERT-BUTYL ETHER REACTION

被引:67
作者
JENSEN, KL [1 ]
DATTA, R [1 ]
机构
[1] UNIV IOWA,DEPT CHEM & BIOCHEM ENGN,IOWA CITY,IA 52242
关键词
D O I
10.1021/ie00040a043
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
The equilibrium-limited liquid-phase synthesis of ethyl tert-butyl ether (ETBE) from the combination of ethanol and isobutylene over an ion-exchange resin catalyst, typically Amberlyst 15, is a reaction of considerable industrial importance now. An equilibrium constant relationship is developed here for the liquid-phase ETBE reaction by following three alternative thermodynamic pathways and critically evaluating the resulting expressions. The final theoretical expression is compared against experimental data obtained in this study from the decomposition of ETBE over Amberlyst 15, as well as that reported in the literature for ETBE synthesis. It can thus be used with reasonable confidence for the calculation of the equilibrium constant, despite a dearth of thermodynamic data yet available in the literature far ETBE. In addition, an expression is derived for the gas-phase equilibrium constant and compared to experimental data from the literature. The thermodynamic approach utilized here should also be useful for other liquid-phase reaction systems.
引用
收藏
页码:392 / 399
页数:8
相关论文
共 27 条
[1]  
[Anonymous], 1953, SELECTED VALUES PHYS
[2]  
[Anonymous], 1987, PROPERTIES GASES LIQ
[3]   EQUILIBRIUM-CONSTANT FOR THE METHYL TERT-BUTYL ETHER LIQUID-PHASE SYNTHESIS BY USE OF UNIFAC [J].
COLOMBO, F ;
CORI, L ;
DALLORO, L ;
DELOGU, P .
INDUSTRIAL & ENGINEERING CHEMISTRY FUNDAMENTALS, 1983, 22 (02) :219-223
[4]  
Denbigh K. G., 1981, PRINCIPLES CHEM EQUI, DOI 10.1017/CBO9781139167604
[5]   KINETICS AND MECHANISM OF ETHYL TERT-BUTYL ETHER LIQUID-PHASE SYNTHESIS [J].
FRANCOISSE, O ;
THYRION, FC .
CHEMICAL ENGINEERING AND PROCESSING-PROCESS INTENSIFICATION, 1991, 30 (03) :141-149
[6]  
GALLANT RW, 1968, PHYSICAL PROPERTIES, V1
[7]   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
[8]  
HUTCHINGS GJ, 1992, CATAL TODAY, V15, P23
[9]   EQUILIBRIUM-CONSTANT FOR ETHYL TERT-BUTYL ETHER VAPOR-PHASE SYNTHESIS [J].
IBORRA, M ;
IZQUIERDO, JF ;
TEJERO, J ;
CUNILL, F .
JOURNAL OF CHEMICAL AND ENGINEERING DATA, 1989, 34 (01) :1-5
[10]   EQUILIBRIUM-CONSTANTS FOR METHYL TERT-BUTYL ETHER LIQUID-PHASE SYNTHESIS [J].
IZQUIERDO, JF ;
CUNILL, F ;
VILA, M ;
TEJERO, J ;
IBORRA, M .
JOURNAL OF CHEMICAL AND ENGINEERING DATA, 1992, 37 (03) :339-343