CONTINUOUS OPERATION OF THE BERTY REACTOR FOR THE SOLVENT METHANOL PROCESS

被引:14
作者
KRISHNAN, C
ELLIOTT, JR
BERTY, JM
机构
[1] UNIV AKRON,DEPT CHEM ENGN,AKRON,OH 44325
[2] BERTY REACT ENGINEERS LTD,FOGELSVILLE,PA 18051
关键词
D O I
10.1021/ie00055a002
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
In the solvent methanol process (SMP), an inert and selective solvent removes methanol as soon as it is formed from syngas. Conversion in the conventional vapor-phase methanol synthesis is limited because of equilibrium limitations due to the reverse reaction, but data presented in this paper demonstrate that high conversions can be obtained in the SMP. Rate data have been collected for the SMP at operating conditions typical of the vapor-phase process (7.8-10 MPa, 493-513 K). Single-pass H-2 and CO conversions range from 30 to 80%. In some cases, conversions are higher than those predicted by vapor phase equilibrium calculations based on the feed composition, providing that SMP is able to overcome the equilibrium barrier. Rates are 2-3 times lower than those encountered in the vapor-phase process owing to pore diffusion limitations from the presence of the liquid.
引用
收藏
页码:1413 / 1418
页数:6
相关论文
共 18 条
[1]  
[Anonymous], 1987, PROPERTIES GASES LIQ
[2]  
BERTY JM, 1974, CHEM ENG PROG, V70, P78
[3]  
BERTY JM, 1990, CHEMTECH, V20, P624
[4]  
BERTY JM, 1981, I CHEM ENG S SER, P87
[5]   SYNTHESIS OF METHANOL .1. CATALYSTS AND KINETICS [J].
CHINCHEN, GC ;
DENNY, PJ ;
JENNINGS, JR ;
SPENCER, MS ;
WAUGH, KC .
APPLIED CATALYSIS, 1988, 36 (1-2) :1-65
[6]   EVALUATION OF AN EQUATION OF STATE METHOD FOR CALCULATING THE CRITICAL PROPERTIES OF MIXTURES [J].
ELLIOTT, JR ;
DAUBERT, TE .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 1987, 26 (08) :1686-1691
[7]  
Froment G.F., 1979, CHEM REACTOR ANAL DE
[8]  
GANDHI R, 1983, THESIS U AKRON
[9]  
HYMAN MH, 1968, HYDROCARB PROCESS, V47, P131
[10]   BINARY AND MULTICOMPONENT VAPOR-LIQUID-EQUILIBRIA OF SYNTHESIS GAS COMPONENTS, METHANOL AND WATER WITH TETRA ETHYLENE-GLYCOL DIMETHYL ETHER (TETRAGLYME) [J].
KHOSLA, P ;
KRISHNAN, C ;
ELLIOTT, JR ;
BERTY, JM .
CHEMICAL ENGINEERING COMMUNICATIONS, 1991, 102 :35-46