Stoichio-kinetic modeling and optimization of chemical synthesis: Application to the aldolic condensation of furfural on acetone

被引:48
作者
Fakhfakh, Nadim [1 ]
Cognet, Patrick [1 ]
Cabassud, Michel [1 ]
Lucchese, Yolande [1 ]
Rios, Manuel Dias De Los [2 ]
机构
[1] CNRS, INPT, UMR 5503, Lab Genie Chim, F-31106 Toulouse, France
[2] Cuban Res Inst Sugar Cane Byproducts, Havana, Cuba
关键词
furfural; acetone; chromatography; aldolic condensation; batch reactor; stoichio-kinetic modeling;
D O I
10.1016/j.cep.2007.01.015
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
The condensation reaction of furfural (F) on acetone (Ac) gives a high added value product, the 4-(2-furyl)-3-buten-2-one (FAc), used as aroma in alcohol free drinks, ice, candies, gelatines and other products of current life. This synthesis valorises the residues of sugar cane treatment since furfural is obtained by hydrolysis of sugar cane bagasse followed by vapor training extraction. In the face of numerous and complex reactions involved in this synthesis, it is very complicated to define the kinetic laws from exact stoichiometry. A solution allowing to cope the problem consists in identifying an appropriate stoichiometric model. It does not attempt to represent exactly all the reaction mechanisms, but proposes a mathematical support to integrate available knowledge on the transformation. The aim of this work is the determination of stoichiometric and kinetic models of the condensation reaction of furfural on acetone. Concentrations of reagents and products are determined by gas and liquid chromatography. Concentration profiles obtained at different temperatures are used to identify kinetic parameters. The model is then used for the optimization of the production of FAc. The interest of such tool is also shown for the scale up of laboratory reactor to a large scale. The anticipation of the reaction behaviour in large scale is crucial especially when the reactor presents important limitations of thermal exchange capacity. (c) 2007 Elsevier B.V. All rights reserved.
引用
收藏
页码:349 / 362
页数:14
相关论文
共 38 条
[1]   Productivity optimization of an industrial semi-batch polymerization reactor under safety constraints [J].
Abel, O ;
Helbig, A ;
Marquardt, W ;
Zwick, H ;
Daszkowski, T .
JOURNAL OF PROCESS CONTROL, 2000, 10 (04) :351-362
[2]  
ALLINGER NL, 1981, CHIMIE ORG, V2
[3]   Optimal operation policies in batch reactors [J].
Aziz, N ;
Mujtaba, IM .
CHEMICAL ENGINEERING JOURNAL, 2002, 85 (2-3) :313-325
[4]   Measurement of aldehydes in low density lipoprotein by high performance liquid chromatography [J].
Bailey, AL ;
Wortley, G ;
Southon, S .
FREE RADICAL BIOLOGY AND MEDICINE, 1997, 23 (07) :1078-1085
[5]   TARGET FACTOR-ANALYSIS FOR THE IDENTIFICATION OF STOICHIOMETRIC MODELS [J].
BONVIN, D ;
RIPPIN, DWT .
CHEMICAL ENGINEERING SCIENCE, 1990, 45 (12) :3417-3426
[6]   EFFECT OF STRUCTURE ON REVERSIBILITY OF ALDOLE CONDENSATION - REACTION OF PHOSPHONOESTERS AND BENZALDEHYDE [J].
BOTTINSTRZALKO, T .
TETRAHEDRON, 1973, 29 (24) :4199-4204
[7]  
Box GEP, 1978, STAT EXPT
[8]   Modeling and optimization of lactic acid synthesis by the alkaline degradation of fructose in a batch reactor [J].
Cabassud, M ;
Cognet, P ;
Garcia, V ;
Le Lann, MV ;
Casamatta, G ;
Rigal, L .
CHEMICAL ENGINEERING COMMUNICATIONS, 2005, 192 (06) :758-786
[9]   OPTIMIZATION OF SEMIBATCH POLYMERIZATION REACTIONS [J].
CAWTHON, GD ;
KNAEBEL, KS .
COMPUTERS & CHEMICAL ENGINEERING, 1989, 13 (1-2) :63-72
[10]   Identification of 5,5′-oxy-dimethylene-bis(2-furaldehyde) by thermal decomposition of 5-hydroxymethyl-2-furfuraldehyde [J].
Chambel, P ;
Oliveira, MB ;
Andrade, PB ;
Fernandes, JO ;
Seabra, RM ;
Ferreira, MA .
FOOD CHEMISTRY, 1998, 63 (04) :473-477