Question: Problem 2. The feed to a flash drum is 15.0 mole % n-butane, 35.0 mole % n-pentane, 30.0 mole % n-hexane, and the remainder is

Problem 2. The feed to a flash drum is 15.0 mole % n-butane, 35.0 mole % n-pentane, 30.0 mole % n-hexane, and the remainder is n-heptane. The feed flow rate is 100 kg moles/day. Use the McWilliams equation instead of the De Priester charts. a. The drum temperature is 75 C, and the drum pressure is 175 kPa (absolute pressure). Find V/F, X, and y. .x b. What is the maximum pressure (in kPa absolute pressure) you could have at 75 C and still have vapor/liquid equilibrium? Report the pressure to 3 significant figures

Step by Step Solution

There are 3 Steps involved in it

1 Expert Approved Answer

Step: 1 Unlock blur-text-image

Question Has Been Solved by an Expert!

Get step-by-step solutions from verified subject matter experts

Step: 2 Unlock

Step: 3 Unlock

Students Have Also Explored These Related Chemical Engineering Questions!

need part B answered Problem 2. The feed to a flash drum is 15.0 mole % n-butane, 35.0 mole % n-pentane, 30.0 mole % n-hexane, and the remainder is n-heptane. The feed flow rate is 100 kg moles/day....

I have part a calculated, just need a directive for part b Problem 2. The feed to a flash drum is 15.0 mole % n-butane, 35.0 mole % n-pentane, 30.0 mole % n-hexane, and the remainder is n-heptane....

Problem 2. The feed to a flash drum is 15.0 mole % n-butane, 35.0 mole % n-pentane, 30.0 mole % n-hexane, and the remainder is n-heptane. The feed flow rate is 100 kg moles/day. Use the McWilliams...

The feed to a flash drum is 30 mole % n-pentane, 45 mole % n-hexane, and 25 mole % n-heptane. The feed flow rate is 100 kg moles/day, the drum temperature is 90 C, and the drum pressure is 200 kPa...

PRESSURE, K Pa 0001 900 800 700 600 500 400 300 250 200 150 Oll 101.3 8 METHANE ETHYLENE ETHANE PROPYLENE PROPANE ISOBUTANE N-BUTANE ISOPENTANE N-PENTANE N-HEXANE N-HEPTANE N-OCTANE N- NONANE " -50...

Mini Project 1: Matlab Program for Multicomponent Flash Distillation with Rachford-Rice Equation Problem Statement A feed that is 50 mol% methane, 10 mol% n-butane, 15 mol% n-pentane, and 25 mol%...

A feed that is 45.0 mol% n-butane, 35.0 mol% n-pentane, and 20.0 mol% n-hexane is fed at a rate of 1.0 kmol/min to a flash drum operating at 50C and 200 kPa. You can use Antoines equation to...

Mass Transfer Table. Operating of a flash drum: Feed Composition mole %: - 34 n- ethane - 66 n- pentane m: 429,988 kg/hr T: 39 C P: 861 kpa Problem 2. We wish to flash distill a feed consisting of...

Problem 2. A liquid containing 35 mole % benzene and 65 mole % 2-propanol is continuously fed to and distilled in a flash drum at 101.3 kPa. The feed rate is 100 kg moles/hr. Equilibrium data is...

Describe various ways in which conflict and negotiations may be related.

Briefly explain why the magnitude of the absorption coefficient (? in Equation 21.18) depends on the radiation wavelength. (21.18) I; = 1be ix

Question 9 5 pts Using the duration approximation, what is the approximate percentage price change of a $ 1 , 0 0 0 zero coupon bond with five years to maturity if the current required rate of return...

JUMP + makes a comparison with the contents of the AC . Select one: True False

(7) How do you import new ideas and approaches into the organization?

(12) What gaps are there in the current approach to development?

What does your leadership team need to develop in terms of entrepreneurial approach to business?