Butane is burned with air. No CO is present in the combustion products. Perform a DOF analysis to prove that the molar composition of the product gas can be determined if the percentage excess air and the percentage conversion of butane are specified
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Indicate risk or environmental concern associated with the following parameters when receiving on water sink, if it was not treated.
BOD, COD, TPH, PAH, TKN, Sulfate, Phenols, PCBs
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Derive Navier0Stokes equations for the 'agitated vessel'.
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Show the range of temperatures that can be achieved by burning acetylene under various conditions.
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Coal analysis indicates 72.6 wt.% C, 18% H and 4% S and balance non combustion ash. Coal burned in a reactor with 20 percent excess air. Calculate the mole composition of the stack gas ?
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I need the energy balance around the heat exchanger given T1=40.8c (temperature of entering stream), T2= 150c(Temperature of leaving stream).
cp of methanol = 2.55 KJ/Kg.k
cp of water = 4.18 KJ/Kg.k
flow rate of methanol = 139.92 Kmol/hr
the flow rate of water = 21.634 Kmol/hr
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