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categoryهندسة كيميائية
schoolبكالوريوس
event_available2026-07-13
السؤال
Transcribed Image Text:
A mixture containing 65.0 mole% acetone (Ac) and the balance acetic acid (AA) is separated in a
continuous distillation column at 1 atm. A flowchart for the operation is as follows:
Feed ①
65% acetone,
35% acetic acid
CONDENSER
Reflux
Overhead product
98% acetone,
2% acetic acid
REBOILER
Boilup
Bottoms product
15.5% acetone,
84.5% acetic acid
The stream from the top of the column is a vapor that passes though a condenser. The
condensed liquid is divided into two equal streams: one is taken off as the overhead product
(distillate) and the other (the reflux) is returned to the column. The stream from the bottom of the
column is a liquid that is partially vaporized in a reboiler. The liquid stream emerging from the
reboiler is taken off as the bottoms product, and the vapor is returned to the column as boilup.
Negligible heat is lost from the column, so that the only places in the system where external heat
transfer takes place are the condenser and the reboiler.
Stream Data
Feed 1
Stream 2
Liquid, 67.5°C, 65 mole% Ac, 35% AA
Vapor, 63.0°C, 98 mole% Ac, 2% AA
Reflux 3
Distillate 4
Bottoms ⑤
Boilup 6
Liquid, 56.8°C, 98 mole% Ac, 2% AA
Liquid, 98.7°C, 15.5 mole% Ac, 84.5% AA
Vapor, 98.7°C, 54.4 mole% Ac, 45.6% AA
Thermodynamic Data
Ĥ(cal/mol)
Acetone
Acetic Acid
T(°C)
Ĥ₁
Ĥy
Ĥ₁
56.8
0
7205
0
5723
63.0
205
7322
194
6807
67.5
354
7403
335
6884
98.7
1385
7946
1312
7420
(a) Taking 100 mol of feed as a basis, calculate the net heat requirement (cal) for the process. (You
may neglect heats of mixing, although doing so for dissimilar liquids like acetone and acetic acid
may introduce some error.)
(b) For the same basis, calculate the required heat input to the reboiler and the required heat removal
from the condenser.
(c) Suppose that instead of the condensed liquid from the top of column being split into two equal
streams to form the reflux and the overhead product, it is split into two streams, with the reflux
being 3 times the overhead product. As before, take a basis of 100 mol of feed and determine the
net heating requirements (cal) for the process and the heat removed in the condenser and added
in the reboiler.
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