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(25) Reactor Heat Duty Specification The reactor in this process is run isothermally at 350°C. Since the reaction is exotherm

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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

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

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