Predicting multiple steady states in equilibrium reactive distillation. 2. Analysis of hybrid systems

被引:44
作者
Guttinger, TE [1 ]
Morari, M [1 ]
机构
[1] Swiss Fed Inst Technol, Automat Control Lab, CH-8092 Zurich, Switzerland
关键词
D O I
10.1021/ie980328p
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
Guttinger and Morari (Ind. Eng. Chem. Res. 1998, 38, 1633-1648) developed graphical methods for the prediction of output multiplicities caused by the reactive vapor-liquid equilibrium in reactive distillation. These methods rest upon the limiting case of reactive columns of infinite length operated at infinite internal flows (infinity/infinity analysis) and are directly applicable to systems where the reactions take place in the entire column ("nonhybrid" columns). In this work, the reactive infinity/infinity analysis is extended to columns with a reactive core ("hybrid" columns) by introduction of two new procedures. First, necessary and sufficient feasibility conditions for hybrid column profiles are derived under the assumption that each of the reactive and nonreactive column sections has infinite length. Using these conditions, an "exact" method is formulated where all possible products of such an infinity/infinity hybrid column can be located in the composition space (by a continuation of solutions). The existence of multiple steady states and the feed region leading to output multiplicities can be predicted. Second, an "approximate" procedure is proposed to obtain an estimate of the product locations of a hybrid column with finite nonreactive sections. The exact method was applied to an "ideal" reactive system, and a new type of multiplicity, which is purely caused by the hybrid nature of the system, is shown. Moreover, the methyl tert-butyl ether (MTBE) reactive distillation process is analyzed using both methods, and the physical causes of the MTBE multiplicities are studied in detail. All analytical results are verified by simulation.
引用
收藏
页码:1649 / 1665
页数:17
相关论文
共 23 条
[1]  
ABUFARES AA, 1995, CHEM ENG RES DES, V73, P3
[2]  
*ASP PLUS, 1995, ASP PLUS REL 9 REF M
[3]   DESIGN AND MINIMUM-REFLUX CALCULATIONS FOR SINGLE-FEED MULTICOMPONENT REACTIVE DISTILLATION-COLUMNS [J].
BARBOSA, D ;
DOHERTY, MF .
CHEMICAL ENGINEERING SCIENCE, 1988, 43 (07) :1523-1537
[4]   Multiple steady states in heterogeneous azeotropic distillation [J].
Bekiaris, N ;
Meski, GA ;
Morari, M .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 1996, 35 (01) :207-227
[5]   MULTIPLE STEADY-STATES IN HOMOGENEOUS AZEOTROPIC DISTILLATION [J].
BEKIARIS, N ;
MESKI, GA ;
RADU, CM ;
MORARI, M .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 1993, 32 (09) :2023-2038
[6]   Some aspects in the design of multicomponent reactive distillation columns with a reacting core: Mixtures containing inerts [J].
Espinosa, J ;
Aguirre, P ;
Perez, G .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 1996, 35 (12) :4537-4549
[7]  
GUTTINGER T, 1998, THESIS ETH ZENTRUM Z
[8]   Predicting multiple steady states in equilibrium reactive distillation.: 1.: Analysis of nonhybrid systems [J].
Güttinger, TE ;
Morari, M .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 1999, 38 (04) :1633-1648
[9]  
Guttinger TE, 1997, COMPUT CHEM ENG, V21, pS995
[10]   WHY METHYL TERT-BUTYL ETHER PRODUCTION BY REACTIVE DISTILLATION MAY YIELD MULTIPLE SOLUTIONS [J].
HAUAN, S ;
HERTZBERG, T ;
LIEN, KM .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 1995, 34 (03) :987-991