In: Other
A fuel gas containing
75.0 mole% methane and the balance ethane is burned completely with
15.0 % excess air.
The stack gas leaves the furnace at 800.0 °C and is cooled to 450.0
°C in a waste-heat boiler, a heat exchanger in
which heat lost by cooling gases is used to produce steam from
liquid water for heating, power generation, or process
applications.
Taking as a basis of calculation 100.0 mol of the fuel gas fed to the furnace, calculate the amount (magnitude) of heat (MJ) that must be transferred from the gas in the waste heat boiler to accomplish the indicated cooling. Provide your answer to 3 significant figures.
according to question we have 100 moles of fuel gas
75 moles methane & 25 moles of ethane
combustion reaction for methane
CH4+2O2 =>CO2+2H2O
& for ethane it is
C2H6+7/2 O2 ---> 2CO2+3H2O
for 1 mole of methane 2 moles of oxygen is required
so for 75 moles of methane 150 moles of oxyegn is required
& as 1 mole of ethane need 3.5 mole of oxygen
therefore 25 moles of ethane will need 87.5 moles of oxyegen
so total oxygen needed = 150 +87.5= 237.5 moles
so required air = 237.5*100/21 = 1130.952 moles
as we use 15 % excess air
supplied air = 1.15 *1130.952 = 1300.595 moles
therefore composition of stake gas will be
N2 = 0.79*1300.595 =1027.470 (N2 act as inert & mole % of N2 in air is 79%)
O2 =0.15*237.5 = 53.625 (as 15% excess O2 will remain unreacted )
H2O = 2*75+3*25 = 225 moles
(as 1 mole methane produce 2 mol water & for each mole of ethane 3 moles of water )
CO2 = 75+2*25 = 125 moles
(as 1 mole methane produce 1 mol CO2 & for each mole of ethane 2 moles of CO2 )
so from this we can find
Cp mix data as we know mole data we can find mole fractions ,Cp values from reference books & can find heat transfer as
Q = mR (Cp/R)dT
where xi is mole fraction of species i
so mole fraction calculation
for CO2 =mole of CO2/Total moles =125/(125+225+53.625+1027.470) = 125/1431.095 =0.087
for O2 = 53.625/1431.095 = 0.037
for H2O = 225/1431.095 = 0.157
for N2 = 1027.470/1431.095 =0.718