Experimental and kinetic modeling study of ethyl butanoate oxidation in a laminar tubular plug flow reactor

被引:20
作者
Bennadji, H. [1 ]
Glaude, P. A. [1 ]
Coniglio, L. [1 ]
Billaud, F. [1 ]
机构
[1] Nancy Univ, Lab React & Genie Proc, UPR CNRS 3349, F-54001 Nancy, France
关键词
Oxidation; Chemical kinetics; Biodiesel; FAEE; Ethyl butanoate; INJECTION DIESEL-ENGINE; METHYL BUTANOATE; GAS-PHASE; LOW-TEMPERATURE; NOX EMISSIONS; BIODIESEL; COMBUSTION; ESTERS; FUELS; OIL;
D O I
10.1016/j.fuel.2011.06.028
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
This investigation examines the experimental and the kinetic modeling of the oxidation of ethyl butanoate (EB) selected as model molecule for fatty acid ethyl esters (FAEE). New experimental information of EB oxidation was generated from a laminar tubular plug flow reactor (PFR) operating at atmospheric pressure, under dilute conditions, over the temperature range 500-1200 K, with various equivalence ratios ranging from 0.5 to 1.6, and at residence times varying between 0.65 and 1.40 s under STP conditions. Concentration profiles of the reactants, stable intermediates, and final products, identified by GC/MS, were measured by infrared ray absorption and GC/TCD-FID analyses. Experiments of EB oxidation carried out in the tubular PFR were simulated using a detailed chemical kinetic oxidation mechanism (117 species and 1035 reactions) proposed in a previous work [Hakka et al. Int J Chem Kin 2010; 42:226] and automatically generated from an improved version of EXGAS software. Globally, good agreement was observed between experimental and simulated results, confirming the validity of the proposed model for EB oxidation. Reaction flux and sensitivity analyses allowed to determine the main reaction pathways involved in the investigated conditions of EB oxidation. (C) 2011 Elsevier Ltd. All rights reserved.
引用
收藏
页码:3237 / 3253
页数:17
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