Process Calculations GATE-1997
Q 1: Pure carbon is completely burnt in oxygen. The flue gas analysis is 70 % CO2, 20 % CO, and 10 % O2. The percent excess oxygen used is
Q 2: The flowsheet is given below:
If the single pass conversion of A to B is 20 %, then the rate of recycle R (mol/h) is
Q 3: A feed at 1298 K, consisting of flue gas (CO2, O2, and N2) and air, is passed through a bed of pure carbon. The reactions that occur both go to completion.
CO_2(g)+C(s)\rightarrow2CO(g),\;\triangle H_R^0\;at\;298\;K=170\frac{kJ}{mol}
O_2(g)+2C(s)\rightarrow2CO(g),\;\triangle H_R^0\;at\;298\;K=-220.4\frac{kJ}{mol}
The combustor is adiabatic and the product gases exit at 1298 K. Calculate the required moles of CO2 per mole of O2 in the feed stream, so that the net heat generated is zero and the bed temperature remains constant at 1298 K. Data: Mean molar heat capacities, CPm
Substance | C | O2 | CO | CO2 |
CPm (kJ/mol.K) | 0.02 | 0.03 | 0.03 | 0.05 |
Q 4: Sea water is desalinated by reverse osmosis as shown in the figure:
All compositions are on a mass basis. Calculate R/E.