hi...
i am not still getting clear picture....
again explaining my problem,
1.SO2 is converted to SO3 in Catalytic converter, in 4 stages....
SO2 + 1/2O2
SO3
According to reaction equation,
Kp = P
SO3/(P
SO2 x P
O21/2)
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Temp.(K) Kp
688 323
713 185
698 261
ref: Process industries by Norris Shrieve, page 333
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Inlet composition of reactor and efficiency of each stage is known, so no. of moles in each stage of SO2,O2 and SO3 can be calculated up to 3 stages.
Beds Efficiencies are given below;
1st bed. 56%
2nd bed. 28%
3rd bed. 9.5%
4th bed. 6%Beds Inlet Temperature are given below;
1st bed. 688k
2nd bed. 713K
3rd bed. 713K
4th bed. 698KComposition of 1-3 beds are given below;
1st Bed 2nd Bed 3rd Bed IN OUT IN OUT IN OUT
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N2 304.231 304.231 304.231 304.231 304.231 304.231
SO2 46.159 20.310 20.310 7.386 7.386 3.000
SO3 0.000 25.849 25.849 38.774 38.774 43.159
O2 34.712 21.787 21.787 15.325 15.325 13.132
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Total 385.102 372.177 372.177 365.715 365.715 363.523
(KMoles)
4th bed composition can not calculated by me, because after 3rd pass there is an Inter-Absorber which absorbs SO3 formed upto 3rd stage,as equilibrium is achieved.so, to convert remaining SO2 to SO3 , an absorber is placed to disturb equilibrium, and convert remaining SO2 to SO3.
Here i have two question;
1. How to calculate no. of moles of SO3 absorbed in absorber?
2. How to calculate no. of moles of SO3 in 3rd stage, where equilibrium is established using Kp equation ?
These are my two problems , hop u understand for any confusion, plz ask.... but help me in these two problems....
regards,