- Thank You So Much 1 (38.83 KiB) Viewed 16 times
Thank you so much.
-
answerhappygod
- Site Admin
- Posts: 899603
- Joined: Mon Aug 02, 2021 8:13 am
Thank you so much.
Thank you so much.
B In Psat (kPa) = A - T(K) + C A B Species Methanol Acetonitrile Nitromethane 16.5785 3638.27 14.895 3413.1 14.7513 3331.7 с -33.65 -22.627 -45.55 b) One of your colleagues proposed to used flash distillation column operated at 330 K and 80 kPa to separate a liquid mixture containing 30 moles% chloroform(1) and 70 moles% ethanol(2). In his proposal , he stated that the mixture exhibits azeotrope with composition of X*2 = y202 = 0.77 at 330 K and the non-ideality of the liquid mixture could be estimated using the following equation : Iny, = Axz and Inya = Ax Given that P, and Pat is 88.04 kPa and 40.75 kPa, respectively at 330 K. Comment if the proposed temperature and pressure of the system can possibly be used for this flash process? Support your answer with calculation (Hint: Maximum 4 iterations is required in any calculation) (10 marks)
B In Psat (kPa) = A - T(K) + C A B Species Methanol Acetonitrile Nitromethane 16.5785 3638.27 14.895 3413.1 14.7513 3331.7 с -33.65 -22.627 -45.55 b) One of your colleagues proposed to used flash distillation column operated at 330 K and 80 kPa to separate a liquid mixture containing 30 moles% chloroform(1) and 70 moles% ethanol(2). In his proposal , he stated that the mixture exhibits azeotrope with composition of X*2 = y202 = 0.77 at 330 K and the non-ideality of the liquid mixture could be estimated using the following equation : Iny, = Axz and Inya = Ax Given that P, and Pat is 88.04 kPa and 40.75 kPa, respectively at 330 K. Comment if the proposed temperature and pressure of the system can possibly be used for this flash process? Support your answer with calculation (Hint: Maximum 4 iterations is required in any calculation) (10 marks)