What are the compositions (mole and mass fractions) and volumetric flow rates (mº/kmol CH, fed to burners) of (a) the ef

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What are the compositions (mole and mass fractions) and volumetric flow rates (mº/kmol CH, fed to burners) of (a) the ef

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What Are The Compositions Mole And Mass Fractions And Volumetric Flow Rates Mo Kmol Ch Fed To Burners Of A The Ef 1
What Are The Compositions Mole And Mass Fractions And Volumetric Flow Rates Mo Kmol Ch Fed To Burners Of A The Ef 1 (36.81 KiB) Viewed 15 times
What are the compositions (mole and mass fractions) and volumetric flow rates (mº/kmol CH, fed to burners) of (a) the effluent gas from the reformer burners and (b) the gas entering the stack? What is the specific gravity, relative to ambient air (30°C, 1 atm, 70% rh), of the stack gas as it enters the stack? Why is this quantity of importance in designing the stack? Why might there be a lower limit on the temperature to which the gas can be cooled prior to introducing it to the stack? Use a methane feed rate to the reformer of 1600 kmolh as a basis for subsequent calculations. When all calculations have been completed, scale the results based on the required production rate of specification-grade methanol.
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