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A three component mixture is to be separated in a distillation column. The mixture is made-up of 108 kmol of 'A' , 42.6 kmol of 'B' and 5.4 kmol of 'C'. Component 'A' is the most volatile and component 'C' the least volatile. The top product will have 95 mol % 'A' and the bottom product 85 mol % 'B' (assume there is no 'C' in the top product).Determine the top and bottom flows from the column and the mol % 'A' in the bottom product.
the equilibrium constant K for the reaction - what is the concentration of SO3 at equilibrium?
Using all three sizes, what is the ideal weight mixture ratio and what is the maximum oxidizer content possible and the theoretical maximum specific gravity of the propellant? (Hint: The centers of four adjacent coarse crystals form a tetrahedron ..
The R2 for which the developed torque would be a maximum.
Would you reach the same conclusion if the weights for operating cost and labor cost were reversed? Recompute as necessary and explain.
Let C be a linear code of length n = 23 and dimension k = 12 Assume that at most three errors have occurred. What is the complexity of the various attacks described in Subsection 11.2.3.
Design and optimize a suitable shell-and-tube heat exchanger that can satisfy the above mentioned duty and fix a tentative geometry and perform all standard calculations
Here you compare the value of H when you use actual data (steam tables) and when you assume ideal gas. Reference means H = 0. State all reasonable assumptions. Vapor-liquid phase partitioning is involved.
question 1a handling operations for solidpowder substances are often a source of dust generation and are a source of
what is the thermal efficiency of the cycle and what fraction of the steam entering the turbine is extracted for each feedwater heater?
In a process to produce 1000 kgmol/h acetaldehyde, ethane is fed to the reactor at 1500 kgmol/h and the fractional conversion is 0.8. The product stream contains 2 mol% CO2. Calculate the molar composition of the product stream and the fractional sel..
When burnt , the flue gas issuing out of the furnace at 545 oc analyses on dry basis as CO2 =14.5 % , O2 = 4.7%, N2 = 80.8 % , Other relevant data are- Gross C.V. of coal =28000 kj /kg , ambient temperature = 15oc
A balanced delta-connected load with a per-phase impedance of 30 + j10 Ω is connected in parallel with a balanced wye-connected load with a per phase impedance of 40-j10 Ω.
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