MIXING AND CHEMICAL KINETIC CONSTRAINTS ON PIC PRODUCTION DURING CHLOROCARBON COMBUSTION

Citation
J. Brouwer et al., MIXING AND CHEMICAL KINETIC CONSTRAINTS ON PIC PRODUCTION DURING CHLOROCARBON COMBUSTION, Combustion and flame, 99(2), 1994, pp. 231-239
Citations number
13
Categorie Soggetti
Engineering,"Energy & Fuels",Thermodynamics
Journal title
ISSN journal
00102180
Volume
99
Issue
2
Year of publication
1994
Pages
231 - 239
Database
ISI
SICI code
0010-2180(1994)99:2<231:MACKCO>2.0.ZU;2-M
Abstract
The amount and composition of products of incomplete combustion (PICs) in combustion systems is controlled by the complex interactions of tu rbulent mixing and chemical kinetics. The current paper addresses this problem by focusing on the effects of incomplete turbulent mixing on the extent of reaction and on the distribution of the local equivalenc e ratio, and investigating the contributions of chlorocarbon inhibitio n of chemical reaction to the emission of PICs. The experimental facil ity has been designed to simulate the conditions in actual incinerator systems; it consists of a Toroidal Jet Stirred Reactor (TJSC) followe d by a Plug Flow Reactor (PFR). The experimental conditions allow one to investigate the combined effects of turbulent mixing and chemical k inetic inhibition on PIC emissions. To address these issues methyl chl oride is injected into a baseline flow of hot products flowing in the PFR. Instantaneous temperature measurement, obtained by application of a laser Rayleigh scattering diagnostic, and stable species concentrat ions are then measured at various distances from the point of injectio n. The temperature probability density functions (pdfs) for fuel-lean and fuel-rich conditions show evidence of mixing constraints. Stable s pecies concentration measurements prove that both mixing and chemical kinetic constraints are present in the PFR environment. Detection of a romatic species is interpreted as an effect of the variation of the lo cal value of the equivalence ratio due to imperfect mixing. Finally, i n order to model the combined chemical kinetic and mixing constraints and to determine which constraints are responsible for PIC emission, r esults from a highly simplified turbulent reacting flow model are pres ented. The model can predict the trend and magnitude of methyl chlorid e burnout and CO/CO2 ratio. Species, such as aromatic compounds, havin g a strong nan-linear dependence on the equivalence ratio can provide insights on the mixing history and might serve as diagnostics of failu re modes in incinerators.