Page 246 - Applied Process Design For Chemical And Petrochemical Plants Volume II

Packed Towers 235

Tower
Cover,
- Distribu-
DIMENSIONS OF STANDARD TOWERS Fig. 360
Inside tor,
Diameter of 24 in. 30 in. 36 in. 40 in. 48 in. 60 in. Fig. 401
Tower A - (See op-
-
-I
posite
A 24 30 36
A' 23% 29% 35 page)
B 27% 34 41%
C 36 36 36 Tower
C' 30 30 36 Section
D 6 6 with
E 15 15 Rim for
F 12 14
G 8 12 Dis tribu-
H 8 1;s I;% tor,
I 3% Fig. 356b
I
i 2% 2% 4 4 4
4
4
M 3 3 3
0 7 93.6 11?4
P 3 3 3
8 11
1% ;2 R Pia in
1%
Tower
%
- - See tion
1
S is inside diameter of ground in faucet. Fig. 356
WEIGHTS
R
Tower
- - - Section
-
Diameter
with Rim
- - 40 in. 48 in. - atBottom
24 in.
- - -
30 in.
60 in.
36 in.
Tower Cover. Fig. 356a
Pi. 360
Weight, Ibs. 80 130 215 300 SO0 700
Tower Support-
Distributor, ing Plate
Fig. 401 and Fig. 279*
401.
Weight, Ibs. 36 60 100 I20 I 70 250
Plain Tower
section,
Fig. 356
Weight, Ibr. 220 300 430 520 700 1000 Tower
Section
Tower Sectior
with Rim with
Fig. 356. and Branch,
356b Fig. 355
Weight, Ibs. 225 310 445 540 7% 1100
Supporting
Plate, Fig. 275
Weight. Ibs. 30 80 140 160 250 400 Tower**
Saucer
Tower Section Fig. 354
with branch,
Fig. 355
Weight. Ibs. 230 320 530 630 900 1800
Tower sauccr,
Fig. 354
Weight, Ibs. 120 200 2 50 340 S00 800
rMBottm
Seetion.
?ig. 35511
Height, Ib. 260 370 610 730 1000 1500
-
- -
Figure 9-4. Physical dimensions of stoneware tower sections, bell and spigot. Used by permission of General Ceramics and Steatite Corp.