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AZEOTROPIC DISTILLATION
Continuing the previous Azeotropic
distillation example:
Distillation column sizing:
The column diameter should be determined
based on the maximum vapor velocity. If the
velocity is exceeded, the column liquid and
vapor hydraulics will fail and the column
will flood.
As the vapor flow rates change from tray to
tray in a non equi-molar flow system, the
tray with the highest vapor velocity will set
the minimum column diameter.
I used Aspen plus to determine the diameter
of the column. You may check the diameter
calculated by Aspen plus using the
following equation and setting f-factor equal
to 1:
𝐹 − 𝑓𝑎𝑐𝑡𝑜𝑟 = 𝑉𝑚𝑎𝑥√ 𝜌 𝑣
Vmax: Maximum vapor velocity (ft/s)
ρv: Vapor density Ib/ft3
Regarding the height of the column, it can
be determined rigorously based on the
following spacing:
1. The total tray height: The typical
distance between trays (tray spacing)
is 0.61 m (2 ft)
2. The space at the top of the column
where the reflux piping enters the
column.
3. The feed tray for feed distribution
piping.
4. The liquid height in the base of the
column that must be determined
according to NPSH of the pump.
However, the design heuristic is to provide
an additional 20% more height than that
required for the trays.
I used Aspen plus in sizing of the columns.
TD-101:
No. of stage 24
Condenser Total
Reboiler Kettle
Tray type Sieve tray
Column Diameter 1.53 m
Column height 16 m
TD-102
No. of stages 8
Condenser Total
Reboiler type Kettle
Tray type Sieve tray
Column diameter 1.2 m
Column height 4.5 m
Reflux drums:
The commonly heuristic holdup time is set
to be 5 min of liquid holdup when the vessel
is 50% full.
Assume L/D = 2.
TD-101 Reflux drum
Diameter 1.32 m
Length 2.63 m
TD-102 Reflux drum
Diameter 0.4 m
Length 0.8 m

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Azeotropic distillation 2

  • 1. AZEOTROPIC DISTILLATION Continuing the previous Azeotropic distillation example: Distillation column sizing: The column diameter should be determined based on the maximum vapor velocity. If the velocity is exceeded, the column liquid and vapor hydraulics will fail and the column will flood. As the vapor flow rates change from tray to tray in a non equi-molar flow system, the tray with the highest vapor velocity will set the minimum column diameter. I used Aspen plus to determine the diameter of the column. You may check the diameter calculated by Aspen plus using the following equation and setting f-factor equal to 1: 𝐹 − 𝑓𝑎𝑐𝑡𝑜𝑟 = 𝑉𝑚𝑎𝑥√ 𝜌 𝑣 Vmax: Maximum vapor velocity (ft/s) ρv: Vapor density Ib/ft3 Regarding the height of the column, it can be determined rigorously based on the following spacing: 1. The total tray height: The typical distance between trays (tray spacing) is 0.61 m (2 ft) 2. The space at the top of the column where the reflux piping enters the column. 3. The feed tray for feed distribution piping. 4. The liquid height in the base of the column that must be determined according to NPSH of the pump. However, the design heuristic is to provide an additional 20% more height than that required for the trays. I used Aspen plus in sizing of the columns. TD-101: No. of stage 24 Condenser Total Reboiler Kettle Tray type Sieve tray Column Diameter 1.53 m Column height 16 m TD-102 No. of stages 8 Condenser Total Reboiler type Kettle Tray type Sieve tray Column diameter 1.2 m Column height 4.5 m Reflux drums: The commonly heuristic holdup time is set to be 5 min of liquid holdup when the vessel is 50% full. Assume L/D = 2. TD-101 Reflux drum Diameter 1.32 m Length 2.63 m TD-102 Reflux drum Diameter 0.4 m Length 0.8 m