The capillary-microreactor:: a new reactor concept for the intensification of heat and mass transfer in liquid-liquid reactions

被引:197
作者
Dummann, G
Quittmann, U
Gröschel, L
Agar, DW
Wörz, O
Morgenschweis, K
机构
[1] Univ Dortmund, Inst React Engn, Dept Chem Engn, D-44221 Dortmund, Germany
[2] BASF AG, D-67056 Ludwigshafen, Germany
[3] BASF Schwarzheide GmbH, D-01986 Schwarzheide, Germany
关键词
process intensification; microreactor; capillary flow; liquid-liquid flow; nitration;
D O I
10.1016/S0920-5861(03)00056-7
中图分类号
O69 [应用化学];
学科分类号
081704 ;
摘要
The capillary-microreactor was used for studying the nitration of a single ring aromatic in an exothermic liquid-liquid two-phase reaction. In the capillary-microreactor, isothermal behaviour can be assumed due to the high heat transfer rates. In addition. a liquid-liquid two-phase plug-flow with a well-defined flow pattern of alternating plugs of the two phases is formed, giving a constant, uniform specific surface area for mass transfer between the two phases. In the nitration reaction, not only the mononitrated main product is formed, but also various by-products via consecutive and parallel reactions. Mass transfer experiments with different flow velocities, but identical residence times, carried out in the capillary-microreactor, yielded differences in conversions and the amounts of by-products formed. Simulations using a mathematical model describing interphase mass transfer and homogeneous chemical reaction indicate increasing mass transfer coefficients at higher flow velocities, suggesting that the mass transfer between the two phases is enhanced by the flow velocity. The enhancement of the mass transfer can be interpreted in terms of an internal circulation flow within the plugs, a conclusion corroborated by CFD calculations. The capillary-microreactor has thus proved to be a useful instrument for the quantitative elucidation of the mechanisms of exothermic liquid-liquid two-phase reactions. (C) 2003 Elsevier Science B.V. All rights reserved.
引用
收藏
页码:433 / 439
页数:7
相关论文
共 6 条
[1]   Development of a microreactor for chemical production [J].
Burns, JR ;
Ramshaw, C .
CHEMICAL ENGINEERING RESEARCH & DESIGN, 1999, 77 (A3) :206-211
[2]  
BURNS JR, 2001, BETT PROC BETT PROD
[3]  
HANSON C, 1975, IND LAB NITRATIONS
[4]  
IRANDOUST S, 1998, STRUCTURED CATALYSTS
[5]   Aromatic nitrations by mixed acid. Fast liquid-liquid reaction regime [J].
Zaldivar, JM ;
Molga, E ;
Alos, MA ;
Hernandez, H ;
Westerterp, KR .
CHEMICAL ENGINEERING AND PROCESSING-PROCESS INTENSIFICATION, 1996, 35 (02) :91-105
[6]   Aromatic nitrations by mixed acid. Slow liquid-liquid reaction regime [J].
Zaldivar, JM ;
Molga, E ;
Alos, MA ;
Hernandez, H ;
Westerterp, KR .
CHEMICAL ENGINEERING AND PROCESSING-PROCESS INTENSIFICATION, 1995, 34 (06) :543-559