Environmental Engineering Reference
In-Depth Information
2500
O 2 =7%
7%
1%
2000
High temperature air combustion
Preheated air temperature =1600 K
1600 K
1500
Conventional combustion
1200 K
1000
burner
end
Distance from burner
FIGURE 4.18 Oxygen concentration at peak point and distribution of temperature of flame
on burner center axis.
that of conventional combustion at 1200 K. It proves that the peak temperature in
high temperature air combustion can be controlled even if the preheated air temper-
ature is raised. Further, since the oxygen concentration at the peak point is much
lower than that in the conventional combustion, it is possible to realize low NO x
combustion in high temperature air combustion.
4.3.2 R ESULTS OF THE T EST
Figure 4.19 shows a series of data including NO x concentration, furnace temper-
ature, preheated air temperature, and exhaust gas temperature of the exhaust gas
obtained from the combustion test executed in the common test facility II. The
furnace temperature was measured by a thermocouple at 100 mm below the furnace
ceiling. Note that the preheated air temperature was lower than the furnace tem-
perature by only 50 K. Using such high temperature combustion air, NO x concen-
tration as low as 90 ppm (not converted) resulted. This value is less than 1/3 of
NO x concentration in a conventional low NO x b urner and less than 1/10 of that in
a quick-mixing type burner, thus marking a large NO x reduction in high temper-
ature air combustion. The time-based variations in the preheated air temperature,
exhaust gas temperature, and NO x concentration were caused as a result of the
change of combustion behavior of a regenerative burner combustion system using
the burner switching time intervals of 30 s.
 
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