Etude de la combustion de gaz de synthèse issus d'un processus de ...
Etude de la combustion de gaz de synthèse issus d'un processus de ... Etude de la combustion de gaz de synthèse issus d'un processus de ...
Chapter 7 composition on the condition of biomass used, the type of gasifier and conditions of pressure and temperature. tel-00623090, version 1 - 13 Sep 2011 Another issue evolved in this work is the combustion, which detailed bibliographic revision allows to verify that in premixed flames, the laminar burning velocity and flame structure data can be extremely useful in the analysis of fundamental processes such as ignition, NO, and soot formation, and flame quenching. Also, turbulent flame models often prescribe the turbulent burning velocity as a function of laminar burning velocity. Thus, detailed information describing the dependence of the laminar burning velocity, flame thickness, ignition temperature, heat release rate and flame quenching on various system parameters can be a valuable diagnostic and design aid. Burning velocity is a physicochemical constant for a given mixture. It is the velocity, relative of unburned gas, which a plane, one-dimensional flame front travels along the normal to its surface. Clearly, it is the volume of combustible mixture, at its own temperature and pressure, consumed in unit time by unit area of flame front. It is independent of flame geometry, burner size and flow rate. The experimental methods for burning velocity determination are described with emphasis for the constant volume and constant pressure methods. In the constant pressure method the laminar burning velocity and Markstein length are deduced from schlieren photographs. Moreover, any experimental or computed value of laminar burning velocity should be associated with a value of the flame stretch rate. Ideally, the stretch-free value of the burning velocity should be quoted and the influence of stretch rate upon this value should be indicated by the value of the appropriated Markstein length. This is the main reason of the increasing use of the constant pressure method in which the stretch rate is clearly defined. The main advantage of the constant volume method for determining the burning velocity is the possibility of exploring a wide range of pressures and temperatures with one explosion. This is the main reason of its utilization for burning velocity determination in engine conditions. Following the biographic revision, the combustion characterization of typical syngas-air mixtures was initiated by the determination of the flammability limits in spherical chamber. These results show that the pressure has a definite effect on flammability limits of the syngas-air mixtures reducing the flammable region in the lean side. The syngas combustion characterization continues with the laminar flame characteristics to four equivalence ratios (0.6, 0.8, 1.0 and 1.2) within the flammability limits. The influence of stretch rate on flame was determined by the correspondent Markstein and Karlovitz numbers. Combustion demonstrates a linear relationship between flame 195
Conclusions radius and time for syngas–air flames. The maximum value of syngas-air flame speeds is presented at the stoichiometric equivalence ratio, while lean or rich mixtures decrease the flame speeds. Tendency observed on the unstretched burning velocity is in agreement with the heat of reaction of the syngas composition. The higher heat value is associated with the higher amount of H 2 and lower dilution by N 2 and CO 2 in the syngas composition. Markstein numbers shows that syngas-air flames are generally unstable. Karlovitz numbers indicates that syngas-air flames are little influenced by stretch rate. Based on the experimental data a formula for calculating the laminar burning velocities of syngas–air flames is proposed, S =− 0.8125φ + 1.6375φ − 0.5725 (Updraft) 0 2 u S =− 0.7313φ + 1.5428φ − 0.4924 (Downdraft) 0 2 u S =− 0.7500φ + 1.5450φ − 0.6210 (Fluidized bed) 0 2 u tel-00623090, version 1 - 13 Sep 2011 for updraft, downdraft and fluidized bed syngas–air mixture combustion, respectively. When compared with common gas fuels like methane and propane, the laminar burning velocity of typical syngas compositions shows to be similar to that of methane, especially the downdraft syngas case, although somewhat slower than propane. This could be due to the syngas stoichiometric air–fuel ratio that is ten times lower than the methane air-fuel ratio and more than twenty times in the case of propane. Thus, the energy content per unit quantity of mixture (air + fuel) inducted to the chamber is only marginally lower when using syngas, compared with the corresponding common gas fuels. The values of laminar burning velocity reported for simulated syngas can be seen to be higher than those obtained for typical syngas compositions. The simulated syngas mixture that better matches the magnitude of laminar burning velocity for the typical syngas compositions is the mixture comprising 5%H2/95%CO. In order to determine laminar burning velocity at elevated pressures relevant to engine applications, the constant volume method was used. Based on the experimental data α β obtained, empirical formulations of the form Su = Su0( T T0) ( P P0) have been establish for pressure range 0.75-20 bar and temperature range 293-450 K tanking into account the stretch effect. The influence of the equivalence ratio is included through the temperature and pressure exponents, α and β, and through the reference burning velocity S u0 as square functions for updraft and downdraft syngas compositions and as a linear function for fluidized bed syngas due to the limited possible data: 196
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Conclusions<br />
radius and time for syngas–air f<strong>la</strong>mes. The maximum value of syngas-air f<strong>la</strong>me speeds<br />
is presented at the stoichiometric equivalence ratio, while lean or rich mixtures<br />
<strong>de</strong>crease the f<strong>la</strong>me speeds. Ten<strong>de</strong>ncy observed on the unstretched burning velocity is<br />
in agreement with the heat of reaction of the syngas composition. The higher heat<br />
value is associated with the higher amount of H 2 and lower dilution by N 2 and CO 2 in<br />
the syngas composition. Markstein numbers shows that syngas-air f<strong>la</strong>mes are<br />
generally unstable. Karlovitz numbers indicates that syngas-air f<strong>la</strong>mes are little<br />
influenced by stretch rate. Based on the experimental data a formu<strong>la</strong> for calcu<strong>la</strong>ting the<br />
<strong>la</strong>minar burning velocities of syngas–air f<strong>la</strong>mes is proposed,<br />
S =− 0.8125φ + 1.6375φ<br />
− 0.5725<br />
(Updraft)<br />
0 2<br />
u<br />
S =− 0.7313φ + 1.5428φ<br />
− 0.4924<br />
(Downdraft)<br />
0 2<br />
u<br />
S =− 0.7500φ + 1.5450φ<br />
− 0.6210 (Fluidized bed)<br />
0 2<br />
u<br />
tel-00623090, version 1 - 13 Sep 2011<br />
for updraft, downdraft and fluidized bed syngas–air mixture <strong>combustion</strong>, respectively.<br />
When compared with common gas fuels like methane and propane, the <strong>la</strong>minar<br />
burning velocity of typical syngas compositions shows to be simi<strong>la</strong>r to that of methane,<br />
especially the downdraft syngas case, although somewhat slower than propane. This<br />
could be due to the syngas stoichiometric air–fuel ratio that is ten times lower than the<br />
methane air-fuel ratio and more than twenty times in the case of propane. Thus, the<br />
energy content per unit quantity of mixture (air + fuel) inducted to the chamber is only<br />
marginally lower when using syngas, compared with the corresponding common gas<br />
fuels. The values of <strong>la</strong>minar burning velocity reported for simu<strong>la</strong>ted syngas can be seen<br />
to be higher than those obtained for typical syngas compositions. The simu<strong>la</strong>ted<br />
syngas mixture that better matches the magnitu<strong>de</strong> of <strong>la</strong>minar burning velocity for the<br />
typical syngas compositions is the mixture comprising 5%H2/95%CO.<br />
In or<strong>de</strong>r to <strong>de</strong>termine <strong>la</strong>minar burning velocity at elevated pressures relevant to engine<br />
applications, the constant volume method was used. Based on the experimental data<br />
α<br />
β<br />
obtained, empirical formu<strong>la</strong>tions of the form Su<br />
= Su0( T T0) ( P P0)<br />
have been establish<br />
for pressure range 0.75-20 bar and temperature range 293-450 K tanking into account<br />
the stretch effect. The influence of the equivalence ratio is inclu<strong>de</strong>d through the<br />
temperature and pressure exponents, α and β, and through the reference burning<br />
velocity S u0 as square functions for updraft and downdraft syngas compositions and as<br />
a linear function for fluidized bed syngas due to the limited possible data:<br />
196