Chemical Engineers' Portable Handbook

Physical Column Design

Actual physical design of a distillation column is a complicated process. Detailed descriptions of such designs can be found in references 39 42, 45.

Some items of interest will be discussed below.

For example, Figure 5-24 is a typical bubble cap column performance chart.


Figure 5-24: Bubble cap column performance (41).

Distribution of areas in a bubble cap column are given in Table 5-7 and Figure 5-25.


Figure 5-25: Tray area classification (41).
Table 5-7: Bubble Cap Column Distributions [*](41)

Tower Diam., ft

Downflow area

Liquid-distribution area

End Wastage

Crossflow

Double Pass

Crossflow

Double pass

Cascade double

3

10 20

10 25

10 30

4

10 20

8 20

7 22

6

10 20

20 30

5 12

15 20

5 18

8

10 20

18 27

4 10

12 16

4 15

10

10 20

16 24

3 8

9 13

20 30

3 12

12

10 20

14 21

3 6

8 11

15 25

3 10

15

10 20

12 18

2 5

6 9

12 20

2 8

20

10 15

5 7

9 15

2 6

[*]Allocated cap area is determined by difference.

In Figure 5-26 the effect of liquid and vapor loads on sieve tray performance is shown.


Figure 5-26: Sieve tray performance (41).

Table 5-8 lists various recommendations for bubble cap columns.

Table 5-8: General Conditions and Dimensions (35)

1.

TrayTray spacing

Tower diameter T

Tray spacing t

M

ft

m

in

0.15

6 minimum

1 or less

4 or less

0.50

20

1 3

4 10

0.60

24

3 4

10 12

0.75

30

4 8

12 24

0.90

36

2.

Liquid flow

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