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Consider the pair of reactions in which ethylene (C2H4) is oxidized either to ethylene oxide (C2H4O, desired) or to carbon dioxide (undesired).
(hint: assume 100 moles feed entering in reactor)
C2H4 + ½ O2 → C2H4O
C2H4 + 3 O2 → 2 CO2 + 2 H2O
The feed to the reactor contains 25% mole ethylene and 75% mole oxygen. The conversion of ethylene is 75% and the selectivity of ethylene oxide over carbon dioxide is 12.
a) determine ξ1 and ξ2 (18 mole, 0.75mole)
b) Calculate the molar composition (mole fractions) of the outlet stream. (0.069, 0.7, 0.198, 0.016, 0.016)
b) Calculate the fractional yield of ethylene oxide.(0.72)
(a)
Feed:
F=100 moles
C2H4=25 moles
O2=75 moles
Now fractional conversion f=0.75 =moles reacted/moles fed
ξ1 = extent of reaction in reaction producing C2H4O
ξ2 = extent of reaction in reaction producing CO2
So
(ξ1+ξ2)/25=0.75------(1) (moles of reacted/moles of ethylene fed)
selectivity=12
selectivity=moles of desired product/moles of undesired product=12
ξ1/2ξ2=12 ( 1mole of C2H4O/2 moles of CO2)
ξ1=24ξ2------(2)
So solving these two equations:
ξ2=0.75 moles
ξ1=18 moles
(b)
Now doing species balance:
Product stream:
C2H4=n1 mole
C2H4O=n2 mole
O2=n3 mole
CO2=n4 mole
H2O=n5 mole
25 – n2 – ξ1 – ξ2 = 0
C2H4=6.25 mol
C2H4O :– n1 + ξ1 = 0
C2H4O=18 mole
O2 :75 – n3 – ξ1/2 – 3ξ2 = 0
O2 :n3=63.75 mole
CO2: – n4 + 2ξ2 = 0
n4=1.5 mole
H2O:– n5 + 2ξ2 = 0
n5=1.5 mole
Total mole=91 mole
Now composition
C2H4=6.25/91=0.069
C2H4O=18/91=0.198
O2=63.75/91=0.7
H2O=1.5/91=0.016
CO2=1.5/91=0.016
(c)
Yield=moles of desired product/Moles of desired product made if the limiting reacting reacts completely
Yield= ξ1/25=18/25=0.72