Modelling of the quenching in cylindrical and annular reactors

被引:3
作者
Ferrer, M [1 ]
Lédé, J [1 ]
机构
[1] Ecole Natl Super Ind Chim, CNRS, Lab Sci Genie Chim, F-54001 Nancy, France
关键词
D O I
10.1016/S0038-092X(98)00111-X
中图分类号
TE [石油、天然气工业]; TK [能源与动力工程];
学科分类号
0807 ; 0820 ;
摘要
Many processes are carried out at high temperatures for the preparation of chemical species that must be recovered near room temperature. However, more or less important losses of the products occur during the cooling period because of undesired side reactions. in order to minimize these phenomena, it is necessary to design a quenching reactor just after the high temperature section. The purpose of the present paper is to propose a model representing the decay of the concentration and of the temperature of the species (produced by a high temperature solar reactor) inside a quenching reactor. The heat and mass balances an numerically solved with very simple assumptions and in the cases of cylindrical and annular reactors. The results are functions of couplings between chemical, heat transfer and flow phenomena. Thanks to the use of non dimensional numbers, the conclusions are valid inside very wide ranges of chemical and experimental conditions. The annular reactor in laminar flow confirms its high efficiency. The mean cooling rates can be much higher than 10(7) K s(-1). The proposed methodology would be also valid for other more complicated practical situations. (C) 1999 Elsevier Science Ltd. All rights reserved.
引用
收藏
页码:151 / 163
页数:13
相关论文
共 15 条
[1]   A NOVEL DEVICE FOR QUENCHING - THE CYLINDRICAL ANNULAR EXCHANGER IN LAMINAR-FLOW [J].
HOUZELOT, JL ;
VILLERMAUX, J .
CHEMICAL ENGINEERING SCIENCE, 1984, 39 (09) :1409-1413
[2]   MASS-TRANSFER IN ANNULAR CYLINDRICAL REACTORS IN LAMINAR-FLOW [J].
HOUZELOT, JL ;
VILLERMAUX, J .
CHEMICAL ENGINEERING SCIENCE, 1977, 32 (12) :1465-1470
[3]  
INCROPERA FP, 1996, INTRO HEAT TRANSFER, P407
[4]   A SOLAR REACTOR FOR HIGH-TEMPERATURE GAS-PHASE REACTIONS - (WATER AND CARBON-DIOXIDE THERMOLYSIS AND NITRIC-OXIDE SYNTHESIS) [J].
LAPICOUE, F ;
LEDE, J ;
TIRONNEAU, P ;
VILLERMAUX, J .
SOLAR ENERGY, 1985, 35 (02) :153-166
[5]   QUENCHING REACTORS IN HIGH-TEMPERATURE CHEMICAL PROCESSES - APPLICATION TO THE THERMOLYSIS OF WATER [J].
LAPICQUE, F ;
LEDE, J ;
VILLERMAUX, J .
CANADIAN JOURNAL OF CHEMICAL ENGINEERING, 1985, 63 (03) :470-480
[6]   DESIGN AND OPTIMIZATION OF A REACTOR FOR HIGH-TEMPERATURE DISSOCIATION OF WATER AND CARBON-DIOXIDE USING SOLAR-ENERGY [J].
LAPICQUE, F ;
LEDE, J ;
VILLERMAUX, J .
CHEMICAL ENGINEERING SCIENCE, 1986, 41 (04) :677-684
[7]  
LEDE J, 1993, CAN J CHEM ENG, V71, P209
[8]   PRODUCTION OF HYDROGEN BY DIRECT THERMAL-DECOMPOSITION OF WATER - PRELIMINARY INVESTIGATIONS [J].
LEDE, J ;
LAPICQUE, F ;
VILLERMAUX, J ;
CALES, B ;
OUNALLI, A ;
BAUMARD, JF ;
ANTHONY, AM .
INTERNATIONAL JOURNAL OF HYDROGEN ENERGY, 1982, 7 (12) :939-950
[9]  
LEDE J, 1996, P 8 INT S SOL THERM, P1143
[10]  
MIDOUX N, 1988, TECHNIQUE DOCUMENTAT, P469