A liquid fuel containing C, H and O, was burned completely using excess air. The Orsat analysis of the combustion gas shows 4.48% CO2, 11.21% O2 and 84.31% N2, And the molal humidity of the product gas is 0.179 mol water vapor per mol of dry gas. Calculate % composition by weight of the liquid fuel.
A liquid fuel containing C, H and O, was burned completely using excess air. The Orsat...
A liquid fuel containing C, H and O, was burned completely using excess air. The Orsat analysis of the combustion gas shows 4.48% CO2, 11.21% O2 and 84.31% N2, And the molal humidity of the product gas is 0.179 mol water vapor per mol of dry gas. Calculate % composition by weight of the liquid fuel.
A liquid fuel containing C, H and O, was burned completely using excess air. The Orsat analysis of the combustion gas shows 4.48% CO2, 11.21% O2 and 84.31% N2, And the molal humidity of the product gas is 0.179 mol water vapor per mol of dry gas. Calculate % composition by weight of the liquid fuel.
A liquid fuel containing Co and H2, was burned using excess air. Its Orsat analysis of the combustion gas is 5.34% CO2, 13.23% O2 and 81.43% N2. The molal humidity of the product is 0.179 mol water vapor/mol of dry gas. Calculate percent composition by weight of the liquid fuel.
A liquid fuel containing Co and H2, was burned using excess air. Its Orsat analysis of the combustion gas is 5.34% CO2, 13.23% O2 and 81.43% N2. The molal humidity of the product is 0.179 mol water vapor/mol of dry gas. Calculate percent composition by weight of the liquid fuel.
A fuel is burned with bone dry air in a furnace. The stack gas is at 116 kPa and has a dew point of 47 °C. The Orsat Analysis of the gas shows 10 mol% CO2 and the balance being O2 and N2. Calculate the ratio of H/C in the fuel.
n-Pentane is burned with excess air in a continuous combustion chamber. Below is a skeleton flowchart. n (mol n-pentane) Combustion Chamber 100 mol Dry Product Gas (DPG) Xp (mol n-pentane / mol DPG) Xaq (mol O2/mol DPG) Xco, (mol CO2/mol DPG) XNC (mol N2 mol DPG) n (mol H2O) Excess Air n2 (mol O2) na (mol N) Air Composition Correct. 169.25 If n2 were 45.0 moles, what would be the value of n4? mol the tolerance is +/-2% Your answer...
A fuel gas containing 85.0 mole% methane and the balance ethane is burned completely with 15.0 % excess air. The stack gas leaves the furnace at 900.0 °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. Physical Property Tables Combustion Gases Correct. Take as a basis 100.0 mol of the fuel gas fed...
From a combustion process that used ethane (C2He) as a fuel, the ORSAT analysis of the stack gases on a nitrogen free basis is as follows: Component CO2 CO O2 Xi (molar basis) 0.289 0.191 0.520 Determine: 1.1. Percentage of the fuel that produced CO 1.2. Percentage of the fuel that produced CO 1.3. Selectivity of CO: with respect to CO 1.4. Theoretical Oxygen. 1.5. Percentage Excess Air 1.6. Amount of Nitrogen produced 1.7. Composition of flue gas (molar) on...
Question Completion Status: QUESTION 1 10 points A hydrocarbon gas is burned with air. The dry-basis (without H20) product gas composition is 1.5 mole% CO, 6 mole% CO2, 8.2 mole% O2, and 84.3 mole% N2. ne(mol C) (mol no (malain (100 mol dry gas 0.21 mol Oymol 0.015 mol COmol dry gas 0.79 mol Ny/mol 0.060 mol CO2 mol dry gas 0.082 mol Oz moi dry g 0.843 mol Nymol dry gas "wmol H20) 1. Using the method of atomic...
A fuel has an average chemical composition of C4H8S0.02 and is burned with (dry) air.The mole fraction of CO2 in the product stream is 0.05 mol CO2/mol gas. The flow rateof the exit stream is 500 liters/min at 2000C and 1 atm of pressure. Assume exit streamis an ideal gas.3a. Draw and label a flow chart for this process3b. Calculate the composition (mol%) of the exit stream on a dry basis, (assumecomplete combustion) and the flow rates of the air...