Answer to Question #216693 in Chemical Engineering for Waj

Question #216693
Blue water gas is obtained by passing steam over red hot carbon enriched
coal (coke). The gas is called "blue" water gas because of its blue flame, a characteristic of the combustion CO. A typical composition shows 4.7% CO2, 41% CO, 49% H2, 0.8% CH4, and 4.5% N2. If the blue water gas at 30 deg C, 700 torrs and 93% RH is burned in wet air, 38% in excess, supplied at the same condition as BWG with 85% RH, calculte
A.) Orsat analysis of the stack gas if the molar ratio of CO2 to CO is 1:8 and H2 to CO is 1:4
B.) GCV of BWG
C.) % Calorific value lost due to sensible heat
D.) Thermal Efficiency
1
Expert's answer
2021-07-14T05:48:31-0400

Part a


T=250C=298KPs=e73.6497258.22987.3037ln(298)+4.1653106(2982))(760101325)=23.57torrN  Dry  BWD=100(74523.570.9760)(273298)=87.25kgmol  BWGnH2On dry gas=pH2Op dry gasnH2O=87.24(23.570.974523.570.9)=2.556kgmoleO2 theo=46.5+101.2425.2=46.6kgmoleO2 supplied=1.3046.6=60.58kgmoleN2 air=60.58+7921=227.896kgmoleN2 total=N2 air+N2 fuel=227.896+4.5=232.4kgmoleCO2 formed=8946.6=41.33kgmoleCO formed=1946.6=5.167kgmoleUnburned H2=145.167=1.2967kgmoleH2 combusted=101.2(12)1.29167=49.3083kgmole=nH2O combustionNH2O from air=(60.58+227.896)(23.570.8574523.570.85=7.9721kgmoleFree O2from=13.98+5.1672+1.291672=17.2092kgmoleT= 25^0 C = 298 K\\ P_s= e^{73.649- \frac{7258.2}{298}-7.3037 \ln(298)+4.1653*10-6(298^2))(\frac{760}{101325})}=23.57 torr\\ N \space \space Dry \space \space BWD =100(\frac{745-23.57*0.9}{760})(\frac{273}{298})=87.25 kgmol \space \space BWG\\ \frac{nH_2O}{ n \space dry \space gas}=\frac{ p H_2O}{ p \space dry \space gas}\\ nH_2O = 87.24 (\frac{ 23.57*0.9}{745-23.57*0.9})=2.556 kgmole\\ O_2 \space theo = 46.5 + \frac{101.2}{4}-25.2 = 46.6 kgmole\\ O_2 \space supplied = 1.30*46.6=60.58 kgmole\\ N_2 \space air =60.58 + \frac{79}{21} = 227.896 kgmole\\ N_2 \space total = N_2 \space air + N_2 \space fuel = 227.896 +4.5=232.4 kgmole\\ CO_2 \space formed = \frac{8}{9}*46.6 = 41.33 kgmole\\ CO \space formed = \frac{1}{9}*46.6 = 5.167 kgmole\\ Unburned \space H_2 = \frac{1}{4}*5.167 = 1.2967 kgmole\\ H_2 \space combusted = 101.2( \frac{1}{2})-1.29167 = 49.3083 kgmole=n H_2O \space combustion\\ NH_2O \space from \space air= (60.58+227.896)(\frac{23.57*0.85}{745-23.57*0.85} = 7.9721 kgmole\\ Free \space O_2 from = 13.98+\frac{5.167}{2}+\frac{1.29167}{2} = 17.2092 kgmole\\


Part b

M3 air/m3 BWG=2.884822.4176074523.570.9298273122.427329874523.570.9760=2.88M^3 \space air /m^3 \space BWG = 2.8848* \frac{22.4}{1}* \frac{760}{745-23.57*0.9}*\frac{298}{273}*\frac{1}{22.4}*\frac{273}{298}* \frac{745-23.57*0.9}{760}=2.88


Part c

m3 stack gas100 moles BWG=357.2322.41101.325100573273=17017.84m3kgmol\frac{m^3 \space stack \space gas }{100 \space moles \space BWG} = 357.23 * \frac{22.4}{1}*\frac{101.325}{100}* \frac{573}{273}=17017.84 \frac{m^3}{kg mol}


Part d

TCTH100253010083.33%\frac{T_C}{T_H}*100\\ \frac{25}{30}*100\\ 83.33\%


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