A gaseous fuel has the following composition by volume – CH_4 = 4.0\%; CO = 26\%; CO_2 = 10\%; H_2 = 10\%; N_2= 50\%. If 20% excess air is supplied calculate the volume of air supplied and the % composition of dry flue gases.
Minimum volume of air required = 0.260 × \frac{100}{21} = 1.238 m^3
Excess air = 1.238 × \frac{20}{100} = 0.2476 m^3
Total air supplied = 1.238 m³ + 0.2476 m³ = 1.4856 m³
Calculation of volume of dry flue gases
The flue gas contains CO_2, O_2 from excess air and N_2 of fuel + N_2 of total air supplied.
CO_2 = 0.40 m^3\\ \\ \\ O_2 = 0.2476 × \frac{21} {100} = 0.052 m^3 \\ \\ \\ N_2 = 0.50 m^3 \text{(of fuel gas)} +1.4856 × \frac{79}{100} \text{(from total air supplied)}\\ \\ \\ N_2 = 0.50 + 1.1174 = 1.674 m^3.Total volume of dry flue gases = (0.40 + 0.052 + 1.674)m³ = 2.126 m³
\% CO_2 =\frac{0.40}{2.126} × 100 = 18.81\% \\ \\ \\ \%O_2 = \frac{0.052} {2.126} × 100 = 2.446\%\\ \\ \\ \% N_2 = \frac{1.674}{ 2.126} × 100 = 78.74\%Constituents | Volume in 1 m³ of gas | Combustion Reaction | \bf O_2 required (in m³) |
Volume of dry flue gases(m³)
|
CH_4 | 0.04 m³ | CH_4 +2 O_2 \rightarrow CO_2 +2H_2O | 0.04 × 2 = 0.08 m³ | CO_2 =0.04 ×1 =0.04 m³ |
CO | 0.26 m³ | CO +\frac{1}{2} O_2 \rightarrow CO_2 | 0.26 × \frac{1}{2}= 0.13 m³ | CO_2 =0.26 ×1 =0.26 m³ |
H_2 | 0.10 m³ | H_2 + \frac{1}{2} O_2 \rightarrow H_2O |
0.10 × \frac{1}{2}= 0.05 m³
|
|
CO_2 | 0.10 m³ | – | – | CO_2 =0.10 m³ |
N_2 | 0.50 m³ | – | – | 0.50 m^3 + N_2 \text{in total air supplied} |
Volume of O_2 required = 0.260 m³ | Total CO_2 in flue gas = 0.40 m³ |