Inlet Mole of C6H6 (B) =210 mol/h Mole of C3H6 (P) =104 mol/h Inlet Temperature=350 °C=350+273=623 K Specific heat of P=64.32 J/mol-K Specific heat of B=82.4 J/mol-K Heat at inlet= [Mole of B*Specific heat of B+ Mole of P*Specific heat of P]*Temperature Inlet= [210 mol/h*82.4 J/mol-K+104 mol/h*64.32 J/mol- K]*673 K=16147477.44 J/hr=16147477.44/1000=16147.477 KJ/h Outlet Mole of C6H6 (B) =116 mol/h Mole of C3H6 (P) =4 mol/h Mole of C9H12 (B)=88 mol/h Mole of C12H18 (DB) =6 mol/h Specific heat of B=143.3 J/mol-K Specific heat of DB=184.4 J/mol-K Outlet Temperature=350 °C=350+273=623 K Heat at outlet=[Mole of B*Specific heat of B+ Mole of P*Specific heat of P+ Mole of B*Specific heat of B+ Mole of DB*Specific heat of DB]*Temperature Outlet= [116 mol/h*82.4 J/mol-K+4 mol/h*64.32 J/mol- K+88 mol/h*143.3 J/mol-K+6 mol/h*184.4 J/mol-K]*673 K Heat at outlet=15837359.04 J/hr=15837359.04 /1000=15837.36 KJ/h Rate of heat transfer=Heat at outlet-Heat at inlet=15837.36 KJ/h-16147.477 KJ/h=-310.117 KJ/h
(25) Reactor Heat Duty Specification The reactor in this process is run isothermally at 350°C. Since...
(25) Reactor/Recycle Specification Before performing energy balances on the fire heater and the reactor, you must specify the reacting system. Again, the competing reactions occurring in this process are: C3H6 + C&H. → CH12 or P+BIB C3H + CH12 + C12H18 or P+IB → DB Below is a simplified version of the flow sheet dealing with just the recycle loop of the process. Fresh benzene (B) is mixed with a recycle stream that contains only B and propylene (P). The...
3. (20) Fire Heater Specification After the reactor feed leaves the heat exchanger, it enters a fire heater. In this unit the stream is further heated from 215°C to 350°C, which requires 4649 kJ/h of heat to be added. To accomplish this, the heat from the combustion of methane gas is used: CH4(2) +2 02(g) → CO2() + 2 H20(2) $ = 10.0 molh The design of this fire heater indicates that the temperature of the flue gas will not...