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

Business, Finance, Economics, Accounting, Operations Management, Computer Science, Electrical Engineering, Mechanical Engineering, Civil Engineering, Chemical Engineering, Algebra, Precalculus, Statistics and Probabilty, Advanced Math, Physics, Chemistry, Biology, Nursing, Psychology, Certifications, Tests, Prep, and more.
Post Reply
answerhappygod
Site Admin
Posts: 899603
Joined: Mon Aug 02, 2021 8:13 am

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

Post by answerhappygod »

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 20 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)
Join a community of subject matter experts. Register for FREE to view solutions, replies, and use search function. Request answer by replying!
Top
Post Reply

Return to “Archived Questions & Answers”