3. Results and discussion
The effect of main stream inlet temperature on the stability limits is
illustrated in Figure 1 for the opposed reacting jet combustor over a
range of equivalence ratios. Fuel lean combustion promises to be an
effective means of limiting pollutant formation. Very lean combustion
however adversely affects the stability of the combustion process. Thus,
initial efforts are directed toward determining the lean stability
limits. The primary variables which affect the stability limits of the
opposed reacting jet are jet stream equivalence ratio, jet stream flow
rate, and main stream inlet temperature. The main stream equivalence
ratio at blowout can be reduced by increasing the jet stream equivalence
ratio, however the net result is little or no reduction in the
equivalence ratio of the recirculation region. Thus, extending the
stability limits to lower equivalence ratios through a variation in the
jet stream composition does not appear useful to gas turbine
applications. Stable operation with both a lean primary and jet stream
can be accomplished by increasing the jet exit velocity. An upper limit
of 200 meters per second is imposed on the jet velocity in the present
investigation due to a desire to avoid compressibility effects
encountered at Mach numbers greater than 0.6. Compressibility effects
threaten the convergence of the numerical solution and change the nature
of the governing equations from elliptic to hyperbolic. In the present
investigation, a jet exit velocity of 90 meters per second is selected.
This minimized the number of grid points required for the numerical
solution while at the same time providing a flame zone large enough to
make possible good spatial resolution in the composition and temperature
measurements. The most effective way of increasing the lean stability
limits of the opposed reacting jet combustor is found to be an increase
in primary stream inlet temperature. For a jet exit velocity of 90
meters per second and a primary stream velocity of 7 meters per second,
an inlet temperature of 600 K allows stable operation to be maintained
at an overall equivalence ratio as low as 0.38. An increase in jet
velocity will of course reduce this stability limit further.