2.5. The off-gases from a gasoline stabilizer are fed to a steam reforming plant to produce hydrogen. The composition of the off-gas, molar%, is: CH4 77.5, C2H6 9.5, C3H§ 8.5, C4H10 4.5. The gases entering the reformer are at a pressure of 2 bara and 35 °C and the feed rate is 2000 m/h. The reactions in the reformer are 1. C,H2, +2+ n(H20) → n(CO) + (2, +1)H2 2. CO + H20→ CO2 +H2 The molar conversion of C,Hu+2 in reaction (1) is 96% and of CO in reaction (2) is 92%. Calculate a. the average molecular mass of the off-gas, b. the mass of gas fed to the reformer, kg/h, c. the mass of hydrogen produced, kg/h.

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2.5. The off-gases from a gasoline stabilizer are fed to a steam reforming plant to produce hydrogen.
The composition of the off-gas, molar%, is: CH4 77.5, C2H6 9.5, C3Hg 8.5, C4H10'4.5.
The gases entering the reformer are at a pressure of 2 bara and 35 °C and the feed rate is
2000 m/h.
The reactions in the reformer are
1. CH2, +2 + n(H,O) → n(CO) + (2, + 1)H2
2. CO + H2O -→ CO2 + H2
The molar conversion of C,H2u+2 in reaction (1) is 96% and of CO in reaction (2) is 92%.
Calculate
a. the average molecular mass of the off-gas,
b. the mass of gas fed to the reformer, kg/h,
c. the mass of hydrogen produced, kg/h.
Transcribed Image Text:2.5. The off-gases from a gasoline stabilizer are fed to a steam reforming plant to produce hydrogen. The composition of the off-gas, molar%, is: CH4 77.5, C2H6 9.5, C3Hg 8.5, C4H10'4.5. The gases entering the reformer are at a pressure of 2 bara and 35 °C and the feed rate is 2000 m/h. The reactions in the reformer are 1. CH2, +2 + n(H,O) → n(CO) + (2, + 1)H2 2. CO + H2O -→ CO2 + H2 The molar conversion of C,H2u+2 in reaction (1) is 96% and of CO in reaction (2) is 92%. Calculate a. the average molecular mass of the off-gas, b. the mass of gas fed to the reformer, kg/h, c. the mass of hydrogen produced, kg/h.
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