Packed Bed flooding.pdf - Youngstown State University's Personal ...
Packed Bed flooding.pdf - Youngstown State University's Personal ...
Packed Bed flooding.pdf - Youngstown State University's Personal ...
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14-74 EQUIPMENT FOR DISTILLATION, GAS ABSORPTION, PHASE DISPERSION, AND PHASE SEPARATION<br />
(especially in refinery towers), and in small-diameter towers where a<br />
single spray nozzle can be used. They are inexpensive and offer a large<br />
open area for vapor flow and a robustness for handling of fouling fluids<br />
when correctly designed, and the sprays themselves contribute to<br />
mass and heat transfer. On the debit side, the spray cones often generate<br />
regions of over- and underirrigation, the sprays may not be<br />
homogeneous, the spray nozzles are prone to corrosion, erosion, and<br />
damage. With highly subcooled liquids, the spray angle may collapse<br />
when pushed at high pressure drops (above 100 to 150 kPa) (Fractionation<br />
Research Inc., “A Spray Collapse Study,” motion picture<br />
919, Stillwater, Okla., 1985). The design and spray pattern are highly<br />
empirical. Sprays also generate significant entrainment to the section<br />
above [Trompiz and Fair, Ind. Eng. Chem, Res., 39(6), 1797 (2000)].<br />
Orifice pan distributors (Fig. 14-69a) and orifice tunnel distributors<br />
(Fig. 14-69b) have floor holes for liquid flow and circular (Fig. 14-69a)<br />
or rectangular (Fig. 14-69b) risers for vapor passages. When they are<br />
used as redistributors, a hat is installed above each riser to prevent liquid<br />
from the bed above from dripping into the risers. Unlike the ladder<br />
pipe and spray distributors that operate by pressure drop, orifice distributors<br />
operate by gravity, and therefore use a much smaller liquid<br />
head, typically 100 to 150 mm at maximum rates. Using Eq. (14-163),<br />
the lower head translates to either more distributions points (nD), which<br />
helps irrigation quality, or larger hole diameters, which resists plugging.<br />
However, the low liquid velocities, large residence times, and open pans<br />
(or troughs) make them more prone to plugging than the pressure distributors.<br />
A good hole pattern and avoidance of oversized risers are<br />
essential. Orifice distributors are self-collecting, a unique advantage for<br />
redistributors. Orifice distributors are one of the most popular types<br />
and are favored whenever the liquid loads are high enough to afford<br />
hole diameters large enough to resist plugging (>12 mm).<br />
(a)<br />
(b)<br />
Orifice trough (or orifice channel) distributors (Fig. 14-69c–f) are<br />
some of the most popular types. The trough construction does away<br />
with the multitude of joints in the orifice pans, making them far more<br />
leak-resistant, a major advantage in large towers and low-liquid-rate<br />
applications. Liquid from a central parting box (Fig. 14-69c, e) or middle<br />
channel (Fig. 14-69d) is metered into each trough. The troughs<br />
can have floor holes, but elevating the holes above the floor<br />
(Fig. 14-69c–g) is preferred as it enhances plugging resistance. Tubes<br />
(Fig. 14-69c, d, f) or baffles (Fig. 14-69e) direct the liquid issuing from<br />
the elevated holes downward onto the packings. Orifice trough distributors<br />
are not self-collecting. When used for redistribution, they<br />
require a liquid collector to be installed above them.<br />
Turndown of orifice distributors is constrained to about 2 : 1 by Eq.<br />
(14-163). For example, a 100-mm liquid head at the design drops to<br />
25 mm when the liquid rate is halved. Lower heads give poor irrigation<br />
and high sensitivity to levelness. Turndown is often enhanced by<br />
using two rows of side tubes (in the Fig. 14-69c type) or of side holes<br />
(in the Fig. 14-69d or e types). Perforated drip tubes (as in Fig. 14-<br />
69d) are popular in either orifice trough or orifice pan distributors.<br />
The lower, smaller hole is active at low liquid rates, with the larger<br />
upper hole becoming active at higher liquid rates. Use of perforated<br />
drip tubes is not recommended when the vapor dew point is much<br />
higher than the liquid bubble point, because liquid may boil in the<br />
tubes, causing dryout underneath [Kister, Stupin, and Oude<br />
Lenferink, IChemE. Symp. Ser. 152, p. 409, London (2006)].<br />
A popular type of the orifice trough distributor is the splash plate distributor<br />
(Fig. 14-69e). The splash plates spread the issuing liquid over<br />
their lengths, making it possible to reduce the number of irrigation<br />
points. This is a special advantage with small liquid rates, as fewer irrigation<br />
points (at a given head) translate to larger, more fouling-resistant<br />
FIG. 14-68 Pressure liquid distributors. (a) Ladder pipe. (b) Spray. (Courtesy of Koch-Glitsch LP.)