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Transcript of Chemical Reaction Engineering Asynchronous Video Series Chapter 8, Part 1: Developing the Energy...
Chemical Reaction Engineering
Asynchronous Video Series
Chapter 8, Part 1:
Developing the Energy Balance. Adiabatic Operation
H. Scott Fogler, Ph.D.
Energy Balances
Energy Balances
User Friendly EquationsThese equations relate X and T, and Fi and T
User Friendly EquationsThese equations relate X and T, and Fi and T
User Friendly EquationsThese equations relate X and T, and Fi and T
User Friendly Equations
User Friendly Equations
User Friendly Equations
User Friendly Equations
User Friendly Equations
Energy Balance
Energy Balance
Energy Balance
Energy Balance
Energy Balance
€
H i = H io TR( ) + ˜ C p T − TR( )
Energy Balance
€
H i = H io TR( ) + ˜ C p T − TR( )
Energy Balance
€
H i = H io TR( ) + ˜ C p T − TR( )
Energy Balance
€
H i = H io TR( ) + ˜ C p T − TR( )
Energy Balance
€
H i = H io TR( ) + ˜ C p T − TR( )
From Chapter 1 we have:
€
Fi = Fi0 + υ iFA 0 X
From Chapter 1 we have:
€
˙ Q − ˙ W S + Fi 0H i 0 − Fi 0 H i − H i Fi 0 + υ iFA 0 X( )∑∑∑
€
Fi = Fi0 + υ iFA 0 X
From Chapter 1 we have:
€
˙ Q − ˙ W S + Fi 0H i 0 − Fi 0 H i − H i Fi 0 + υ iFA 0 X( )∑∑∑
€
H i∑ Fi 0 + υ iFA 0 X( ) = H iFi 0 + υ∑ 0H i
ΔHRX
1 2 4 3 4 FA 0 X
€
Fi = Fi0 + υ iFA 0 X
From Chapter 1 we have:
€
˙ Q − ˙ W S + Fi 0H i 0 − Fi 0 H i − H i Fi 0 + υ iFA 0 X( )∑∑∑
€
H i∑ Fi 0 + υ iFA 0 X( ) = H iFi 0 + υ∑ 0H i
ΔHRX
1 2 4 3 4 FA 0 X
€
˙ Q − ˙ W S − Fi 0 H i − H i 0( ) + ΔH RX FA 0 X = 0∑
€
Fi = Fi0 + υ iFA 0 X
From Chapter 1 we have:
€
˙ Q − ˙ W S + Fi 0H i 0 − Fi 0 H i − H i Fi 0 + υ iFA 0 X( )∑∑∑
€
H i∑ Fi 0 + υ iFA 0 X( ) = H iFi 0 + υ∑ 0H i
ΔHRX
1 2 4 3 4 FA 0 X
€
˙ Q − ˙ W S − Fi 0 H i − H i 0( ) + ΔH RX FA 0 X = 0∑
Heat of Reaction
€
H i T( ) = H i TR( ) + ˆ C pi T− TR( )
€
ΔH RX = H iυ i = υ iH io TR( ) + υ 0
ˆ C pi∑∑∑ T− TR( )
€
ΔH RX = ΔH Ro TR( ) + Δ ˆ C p T− TR( )
€
Fi = Fi0 + υ iFA 0 X
From Chapter 1 we have:
€
˙ Q − ˙ W S + Fi 0H i 0 − Fi 0 H i − H i Fi 0 + υ iFA 0 X( )∑∑∑
€
H i∑ Fi 0 + υ iFA 0 X( ) = H iFi 0 + υ∑ 0H i
ΔHRX
1 2 4 3 4 FA 0 X
€
˙ Q − ˙ W S − Fi 0 H i − H i 0( ) + ΔH RX FA 0 X = 0∑
Heat of Reaction
€
H i T( ) = H i TR( ) + ˆ C pi T− TR( )
€
ΔH RX = H iυ i = υ iH io TR( ) + υ 0
ˆ C pi∑∑∑ T− TR( )
€
ΔH RX = ΔH Ro TR( ) + Δ ˆ C p T− TR( )
€
Fi = Fi0 + υ iFA 0 X
€
ΔH RX =da
H D TR( ) +ca
H C TR( ) −ba
H B TR( ) − H A TR( )
€
=H io TR( )+ CPi T− TR( )
€
Fi0 H i − H i0( ) = Fi0Cpi T −Ti0( )∑∑
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˙ Q − ˙ W S − Fi 0 H i − H i 0( ) + ΔH RX FA 0 X = 0∑
If Ti0=T0
€
˙ Q − ˙ W S + Fi 0C pi T − T0( ) − ΔH RX FA 0 = 0 X∑
€
FA = FA0 1− X( )
Writing the energy balance in terms of conversion:
€
rA
V
∫ dV = FA0 X
Writing the energy balance in terms of conversion:
€
FA = FA0 1− X( )
€
rA
V
∫ dV = FA0 X
Writing the energy balance in terms of conversion:
€
FA = FA0 1− X( )
€
Fi 0C pi T − T0( )∑ = FA 0θ iCpi∑ T − T0( )
€
rA
V
∫ dV = FA0 X
Writing the energy balance in terms of conversion:
€
FA = FA0 1− X( )
€
Fi 0C pi T − T0( )∑ = FA 0θ iCpi∑ T − T0( )
€
˙ Q − ˙ W S + FA 0 X ΔH RX TR( ) + ΔC p T − TR( )[ ] = FA 0 θ iCpi T − T0( )∑
€
rA
V
∫ dV = FA0 X
Writing the energy balance in terms of conversion:
€
FA = FA0 1− X( )
€
Fi 0C pi T − T0( )∑ = FA 0θ iCpi∑ T − T0( )
€
˙ Q − ˙ W S + FA 0 X ΔH RX TR( ) + ΔC p T − TR( )[ ] = FA 0 θ iCpi T − T0( )∑
Neglecting and rearranging:
€
˙ W S
€
˙ Q − FA 0 θ iCpi T − T0( )∑ + FA 0 X ΔH RX TR( ) + ΔC p T − TR( )[ ] = 0
€
FA = FA0 + rAdVV
∫ = FA 0 1− X( )
€
rA
V
∫ dV = FA0 X
€
Fi 0C pi T − T0( )∑ = FA 0θ iCpi∑ T − T0( )
€
˙ Q − ˙ W S + FA 0 X ΔH RX TR( ) + ΔC p T − TR( )[ ] = FA 0 θ iCpi T − T0( )∑
€
FA = FA0 + rAdVV
∫ = FA 0 1− X( )
€
rA
V
∫ dV = FA0 X
€
Fi 0C pi T − T0( )∑ = FA 0θ iCpi∑ T − T0( )
€
˙ Q − ˙ W S + FA 0 X ΔH RX TR( ) + ΔC p T − TR( )[ ] = FA 0 θ iCpi T − T0( )∑
€
FA = FA0 + rAdVV
∫ = FA 0 1− X( )
€
rA
V
∫ dV = FA0 X
€
Fi 0C pi T − T0( )∑ = FA 0θ iCpi∑ T − T0( )
€
˙ Q − ˙ W S + FA 0 X ΔH RX TR( ) + ΔC p T − TR( )[ ] = FA 0 θ iCpi T − T0( )∑
T
X
Slope ≈
€
ΔH Rxn
θ iC pi∑