FUELS AND COMBUSTION 515dharm
\M-therm\Th11-2.pm5Total carbon in the flue gas = a × b × 12 (CO 2 + CO) per kg of carbon in the flue gas=
ab
ab×× ×
×× +28
122
2N
(CO CO ) ...(i)For every kg of fuel supplied for combustion
C
100
kg of carbon pass out of the flue, whencethe weight of N 2 per kg of fuel is
28
12 1002
2N
(CO CO )C kg
+
× ...(ii)If all this nitrogen has come from the atmosphere, then air supplied per kg of fuel=
28 100
12 100 772
2×××
+××NC
(CO CO )
...(iii)(since air contains 77% nitrogen by weight)
∴ Air per kg of fuel =
NC
(CO CO )2
2100 77 12
28 100×
××
×+= NC
33(CO CO )2
2×
+. (Ans.)
It has been shown above that he total carbon of the flue gas is given by a × b × 12 (CO 2 + CO)
and that in CO by a × b × 12 CO, whence the proportion of carbon burnt to CO is given by
ab
ab×× ×
×× +12(^122)
CO
(CO CO ) =
CO
CO CO+ 2
and if C is the proportion of carbon actually burnt per kg of fuel, then
Carbon burnt to CO per kg of fuel =
(CO)(C)
CO CO+ 2
. Proved.
+ Example 11.11. The following results were obtained in a trial on a boiler fitted with
economiser :
CO 2 CO O 2 N 2
Analysis of gas entering
the economiser 8.3 0 11.4 80.3
Analysis of gas leaving
the economiser 7.9 0 11.5 80.6(i)Determine the air leakage into the economiser if the carbon content of the fuel is 80 per
cent.
(ii)Determine the reduction in temperature of the gas due to air leakage if atmospheric
temperature is 20°C and flue gas temperature is 410°C. Ash collected from ash pan is 15 per cent
by weight of the fuel fired.
Take : cp for air = 1.005 kJ/kg K and cp for flue gas = 1.05 kJ/kg K.
Solution. (i) Air supplied =
NC
(CO CO)2 ×
33 2 +
Air supplied on the basis of conditions at entry to the economiser=
80 3 80
33 8 3 0.
(. )×
+
= 23.45 kg