Q2.A typical de-propanizer column having a feed at 207.3 C°, 100 psia and 1271.519 Ibmol/hr with the following compositi

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Q2.A typical de-propanizer column having a feed at 207.3 C°, 100 psia and 1271.519 Ibmol/hr with the following compositi

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Q2 A Typical De Propanizer Column Having A Feed At 207 3 C 100 Psia And 1271 519 Ibmol Hr With The Following Compositi 1
Q2 A Typical De Propanizer Column Having A Feed At 207 3 C 100 Psia And 1271 519 Ibmol Hr With The Following Compositi 1 (18.21 KiB) Viewed 22 times
Q2.A typical de-propanizer column having a feed at 207.3 C°, 100 psia and 1271.519 Ibmol/hr with the following composition in mole fraction: Ethane 0.0148, propane 0.7315, 1-butane 0.0681, n-butane 0.1462, 1-Pentane 0.0173, n Pentane 0.015 and n-hexane 0.0071. Calculate the propane mass fraction in the distillate if the mole fraction of propane is 0.001 in the bottom and the mole fraction of I-butane in the distillate is 0.02. Total no. of Stages is 17 and the feed stage is no. 8. (SRK)
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