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A mixture of saturated hydrocarbon and N2 us burned in excess air supplied at 25°C, 740 torrs with 90% RH. An orsat analysis of the stack gas shows 7.6% CO2, 2.28% CO, 1.14% H2, 6.03% O2 and 82.95% N2. With a dew point of 53.46°C. The stack gases leave at 300°C, 765 mmHg with a volume ratio of 2.049 m3 wet stack gas/m3 wet air.
a. The formula of hydrocarbon is?
b. Mole % analysis of the fuel
c. % excess air
Saturates hydrocarbon and N2 is burned with air at 25°C and 740 torr
1 torr = 1 mmHg
760 mmHg = 1 atm
P = 740 mmHg = 0.9736 atm
R. H = 90%
R. H = PA/Pas
PA- partial pressure
Pas - saturation pressure
At T = 25°C saturation pressure of water from handbook = 0.0313 atm
0.90= PA/0.0313
PA =0.02817 atm
Mole fraction of water vapor in air = PA/P
= (0.02817/0.9736) = 0.02893
Normal air Contains 21% oxygen and 79% nitrogen
Mole fraction of oxygen in air = (1-0.02894) (0.21) = 0.2039
Mole fraction of nitrogen in air = (1-0.02894) (0.79) = 0.7671
The wet stack gas volume of 2.049 m3
at T = 300°C = 573 K
P = 765 mmHg
P = 765/760 = 1.0065 atm = 1.0196 ×105 Pa
n = PV/RT
n = (1.0196×105) (2.049) /(8.314×573)
n = 43.853 mol
Moles of wet stack gas = 43.853 mol
Dew point of stack gas = 53.46°C
At dew point saturation pressure = partial pressure of water vapor
At T = 53.46°C , partial pressure of water vapor =
0.144 atm
Mole fraction of water vapor =
Partial pressure /P = (0.144/1.0065) = 0.1430
Amount of water vapor present = 0.1430(43.853) = 6.2709 moles
Volume of wet air = 1 m3
T = 25°C = 298 K
P = 0.9736 atm = 0.98625×105 Pa
n = PV/RT
n = (0.98625×105) (1) /(8.314×298)
n = 39.8071 mol wet air
Mole fraction of water vapor in air = 0.02893
Amount of water vapor in air = 0.02893(39.8071) = 1.1516 moles
Amount of water vapor produced due to reaction = 6.2709-1.1516 = 5.1193 moles
The reaction occuring is
According to Stiochiometry amount of H reacted to form 5.1193 moles water vapor = 5.1193(1) = 5.1193 moles
Amount of dry gas present = total stack gas - amount of water vapor in stack
= 43.853-6.2709 = 37.5821 moles
From orsat analysis mole % of H2 = 1.14%
Moles of H2 in stack gas = 37.5821(0.0114) = 0.4284 moles
Moles of H present = 2(0.4284) =0.85687 moles
Total moles of H present = 0.85687+5.1193 = 5.97617
Since hydrocarbon is saturated only single bonds are present so
Each carbon attaches to 3 hydrogen atoms
Carbon atoms present = 5.97617/3 = 1.992 moles
The chemical formula of hydrocarbon
=
~
B)
Mol% analysis of fuel
Component | moles | mol% |
C | 1.992 | 25 |
H | 5.976 | 75 |
Total | 7.968 | 100 |
C)
Dry gas analysis
Dry gas present = 37.5821
Component | mol% | moles |
N2 | 82.95 | 31.174 |
O2 | 6.03 | 2.266 |
CO | 2.28 | 0.856 |
CO2 | 7.6 | 2.8562 |
H2 | 1.14 | 0.5219 |
Total | 100 | 37.5821 |
The reactions occuring are
According to Stiochiometry amount of O2 needed for 2.8562 mole CO2 = 2.8562(1) = 2.8562 mole
According to Stiochiometry amount of O2
Needed for 0.856 mole CO = 0.856/2
= 0.428 mole
Total H present = 5.97619 moles
According to Stiochiometry amount of O2 needs
need 5.97619 moles = 5.97619(0.5) /2 = 1.4940 moles
Total O2 required theoretically = 1.4940+0.428+2.8562 = 4.7782 moles
Amount of O2 in stack gas = 2.266 moles
Excess % = (excess oxygen/theroetical O2)(100)
= (2.266/4.7782)= 0.47423 = 47.423%
Exces oxygen% = excess air% = 47.423%
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