Question

3. Given the equilibrium data for acetone from ethanol at 1 atm below, 0.262 0.15 0.348 0.417 0.25 0.478 0.524 0.35 0.566 0.6

0 0
Add a comment Improve this question Transcribed image text
Answer #1

醜, %o.go 0.80 RtI R+I0-8 0.6 0:3 ©이 o9 0.3 0-1 15 3况- o 13 Given 2 013 A P at a acetone0.39-030 0-2 001calculated by toon (xo.ro) u&th eguaeboaton &re are aeg:χ toe Replue nab am e teval rm ab-sec. Rmmti 2o4S

Add a comment
Know the answer?
Add Answer to:
3. Given the equilibrium data for acetone from ethanol at 1 atm below, 0.262 0.15 0.348...
Your Answer:

Post as a guest

Your Name:

What's your source?

Earn Coins

Coins can be redeemed for fabulous gifts.

Not the answer you're looking for? Ask your own homework help question. Our experts will answer your question WITHIN MINUTES for Free.
Similar Homework Help Questions
  • We are separating acetone and ethanol in a distillation column with a total condenser and a...

    We are separating acetone and ethanol in a distillation column with a total condenser and a partial reboiler. The column has two feeds and operates at a pressure of 1.0 atm. Feed 1 is a saturated liquid that is 60.0 mol% acetone and has a feed rate of F1 = 200.0 kmol/h. The second feed is 40.0 mol% acetone, has a feed rate of F2 = 300.0 kmol/h, and is a two-phase mixture that is 20% vapor. Assume CMO is...

  • The vapor-liquid equilibrium for n-pentane and n-hexane at 1 ATM is well approximated using a constant...

    The vapor-liquid equilibrium for n-pentane and n-hexane at 1 ATM is well approximated using a constant relative volatility of 2.95. CMO is valid. For all the problems, the feed stream is flowing at 80 mol/s and contains 45 mol% n-pentane, the feed is a saturated liquid (q = 1) at the column pressure, the distillate is 95 mol% n-pentane, and the bottoms is 10 mol% n-pentane. In this problem, you should analyze the column graphically using the McCabe-Thiele Method a....

  • A distillation column is separating a feed that is 40 mol% methanol and 60% water. The...

    A distillation column is separating a feed that is 40 mol% methanol and 60% water. The two phase feed is 60% liquid. Distillate product should be 92% methanol and bottoms 4 mol%. A total reboiler and a total condenser are used and reflux is saturated. Operation is at atmospheric pressure with a reflux ratio of 0.9. Under these conditions, HG = 1.3 ft and HL = 0.8ft in both the stripping and enriching sections. Determine the required packing height in...

  • Question 3 A saturated liquid mixture is fed to a continuous distillation column at 300 kmol/h. The specifications...

    Question 3 A saturated liquid mixture is fed to a continuous distillation column at 300 kmol/h. The specifications of the operation of the column are provided in Table 2. The column operates at 800 kPa. Table 2: Feed, distillate and bottoms flowrates Component Feed (kmol/h) Bottoms (kmol/h) Distillate (kmol/h) methanol 95 ethanol 33 n-propanol (LK) 67 n-butanol (HK) 45 4 n-pentanol 60 Total 300 Additional information: a. n-propanol is the light key component (LK) and n-butanol is the heavy key...

  • The following feed mixture is to be separated by ordinary distillation at 120 psia so as to obtai...

    Please answer the question D-E using the K-value below The following feed mixture is to be separated by ordinary distillation at 120 psia so as to obtain 92.5 mole% of the nc, in the liquid distillate and 82.0 mole% of the iC5 in the bottoms Lbmole/hr C3 iC nC ic nC 10 15 25 20 30 100 a) Estimate the minimum number of equilibrium stages required by applying the b) Use the Fenske equation to determine the distribution of nonkey...

  • Problem #1 A batch still is to be used to separate methanol from an aqueous solution....

    Problem #1 A batch still is to be used to separate methanol from an aqueous solution. The still consists of an equilibrium still pot surmounted by a number of plates equivalent to two more equilibrium stages. A total condenser is used, which returns saturated reflux. During separation the overhead reflux ratio L/D is held constant at 1.00. The holdup on the plates and in the condenser system is insignificantly small in comparison with that in the still pot. Suppose that...

  • Hand Calculations (40 %)-(must not exceed 2 pages) The process involves the separation of a binary mixture containing heptane and ethylbenzene using a countercurrently operated continuous fractio...

    Hand Calculations (40 %)-(must not exceed 2 pages) The process involves the separation of a binary mixture containing heptane and ethylbenzene using a countercurrently operated continuous fractionation unit. A feed at a flowrate of 252 mol/h containing 43 wt% heptane and 57 wt% ethyl benzene is to be fractionated at 1 bar to give a distillate with 95 mol% heptane and a bottom product with 95 m0196 ethyl benzene. The reflux ratio will be 70% more than the minimum. The...

ADVERTISEMENT
Free Homework Help App
Download From Google Play
Scan Your Homework
to Get Instant Free Answers
Need Online Homework Help?
Ask a Question
Get Answers For Free
Most questions answered within 3 hours.
ADVERTISEMENT
ADVERTISEMENT
ADVERTISEMENT