Specification
AA865-PCT
Amendment
DESCRIPTION
Title of Invention: Separator
Technical Field
[ 0 0 0 1 ] The present invention relates to a separator
which is arranged downstream of a wet dust collector
which collects dust contained in exhaust gas and which
separates water drops from the exhaust gas from the wet
dust collector.
Background Art
[0002] In an ironmaking plant, to remove the dust from
the exhaust gas of a converter, a wet dust collector is
used. A wet dust collector sprays water on the passing
exhaust gas and collects and removes the dust in the
exhaust gas by the sprayed water. From the wet dust
collector, the exhaust gas which contains the water drops
which contain dust is exhausted. For separating the water
drops from this exhaust gas, a separator is arranged
downstream of the wet dust collector.
[0003] The separator, for example, as shown in PLTs 1
and 2, has a tubular shaped housing which has an inlet
which opens upward and a gas outlet which opens in the
horizontal direction and which is bent about 90". Inside
the housing, partitioning members which partition the
inside space are arranged. The water drops in the exhaust
gas which flows into the separator deposit on the inside
surfaces of the outside walls of the housing and the
surfaces of the partitioning members, and flow along the
surfaces. The water which contains dust which flows along
the inside surfaces of the outside walls (below, referred
to as the "dust-containing water") is drained from a
water outlet which is provided at the outside wall to
outside of the housing. Further, the dust-containing
water which flows along the surfaces of the partitioning
members is dammed by dam parts which are formed at ends
of the partitioning members which adjoin the gas outlet
and is drained from the both end parts of the dam parts
through the drainage port to outside of the housing. In
this way, the exhaust gas which is introduced into the
5 separator is stripped of water drops, then is exhausted
through the gas outlet from the separator.
[0004] Further, PLT 3 describes a separation device
(separator) which comprises an elbow pipe in which guide
plates curved in the same way as the elbow pipe are
10 provided and wherein the inlet of the elbow pipe has a
diffuser part of a venturi pipe connected to it so as to
raise the flow rate of the gas flowing in the separator
device. In the invention of PLT 3, the flow rate of the
gas is raised so as to increase the amount of liquid
15 drops which collide with the guide plates or inside
surface of the elbow pipe.
[0005] Furthermore, PLT 4 describes an elbow type of
separator which is provided with a plurality of impact
plates which are inclined at a slant with respect to the
20 direction of flow of gas at the gas inlet of the
separator and which increase the particle size of the
water drops contained in the gas so as to make it easier
to trap the water drops.
25 Citations List
Patent Literature
[0006]
PLT 1: Japanese Patent Publication No. 63-140022A
PLT 2: Japanese Utility Model Publication No. 51-114307U
30 PLT 3: Japanese Utility Model Publication No. 43-15417Y
PLT 4: Japanese Patent Publication No. 55-79022A
Summary of Invention
Technical Problem
35 [0007] In the separator according to the prior art
which is described in the already explained PLTs 1 and 2,
the housing is formed so as to extend in the horizontal
direction near the gas outlet. The partitioning members
inside of the housing are similarly formed so as to
extend in the horizontal direction near the gas outlet.
Therefore, the dust-containing water which flows along
the surface of the partitioning members falls in flow
rate at the portions which extends in the horizontal
direction and easily pool inside the dam parts. For this
reason, inside the dam parts, dust may separate from the
dust-containing water and accumulate. In particular, dust
easily accumulated at the dam parts at the portions away
from the drainage port.
[ 0 0 0 8 ] If dust accumulate at the dam parts in this
way, the dust-containing water will no longer be drained
from the drainage port. It will pass over the dam parts
and resplatter to the gas outlet resulting in a drop in
the efficiency of the separator. In this case, water
drops which contain dust will flow into the facility
downstream of the separator and stable operation of the
converter will be obstructed.
[0009] In the invention of PLT 3, the elbow pipe and
venturi pipe are configured to be combined and guide
plates are configured to be arranged inside the elbow
pipe, and therefore the configuration is complicated and
the cost becomes higher. In addition, since the gas flow
rate in the elbow pipe is raised by the venturi pipe,
there is the problem that the pressure loss increases.
[OOlO] In the invention of PLT 4, the pressure loss at
inclined members which are provided at the inlet of the
separator becomes higher. In addition, there is the
problem that dust easily accumulates at the inclined
members. In the invention of PLT 4, a cleaning nozzle is
provided for cleaning off the dust accumulating at the
inclined members by water. Therefore, the manufacturing
costs and operating costs rise. Furthermore, while
ejecting water from the cleaning nozzle to clean the
inclined members, the amount of water drops in the gas
increases, and therefore the amount of water drops
passing through the separator and flowing out to the
downstream side remarkably increases.
[OOll] The present invention has as its technical
problem to solve these problems of the prior art and has
5 as its object the provision of a separator which prevents
pooling of dust-containing water which flows along the
surfaces of partitioning members arranged at the inside
of a housing so as to improve the efficiency of
separation by a simple configuration.
10
Solution to Problem
[0012] To achieve the above-mentioned object,
according to the present invention, there is provided a
separator which is connected downstream of a wet dust
15 collector for collecting dust contained in exhaust gas
and which separates water drops containing dust from
exhaust gas from the wet dust collector, characterized by
comprising a housing having a gas inlet which opens
upward and which receives exhaust gas from the wet dust
20 collector, and a gas outlet which opens in a horizontal
direction or below that, the housing forming a passage
which changes the direction of flow of exhaust gas
flowing from the gas inlet to the gas outlet, at least
one partitioning member arranged in the housing and
25 partitioning the inside space of the housing, the
partitioning member being provided with a dam part for
damming dust-containing water flowing along a surface of
the partitioning member, at an end of the partitioning
member at the gas outlet side, and a drainage pipe,
30 connected through a drainage port to the dam part, for
draining the dust-containing water which was dammed by
the dam part from the dam part to the outside of the
housing, wherein at the partitioning member, a deflector
which directs the dust-containing water flowing along the
35 surface of the partitioning member to the drainage port
is arranged.
[ 0 0 13 ] The partitioning member can be arranged so as
to partition the inside space of the housing into upper
and lower spaces at the gas outlet side.
Further, drainage ports can be formed at the
drainage pipes so as to open at the both ends of the dam
5 part in a transverse direction with respect to the
direction of flow of gas inside the housing.
[0014] The deflector can be made an approximately
triangular plate shape which has a vertex at an upstream
side in the direction of flow of gas and expands from the
10 vertex downstream in the direction of flow of gas.
A projecting height H of the deflector from the
partitioning member is preferably selected from
0.5xHolHll. OxHo in range with respect to the height Ho of
the dam part.
15 [OOlS] In the partitioning member, a region which
adjoins the dam part in the direction of flow of gas in
the housing can be formed so as to be inclined toward the
downstream side downward by an inclined angle 8 of
5°181250 in range.
20 [0016] The volume of the dust-containing water which
is introduced to the housing and the inclined angle 8 can
be made to satisfy the following relationship:
When 400 m3/h5v<900 m3/h, 5°181250
When V2900 m3/h, 5°181-0.091xV+106. 81
25 [0017] According to another embodiment of the present
invention, there is provided a separator which is
connected downstream of a wet dust collector for
collecting dust contained in exhaust gas and which
separates water drops containing dust from exhaust gas
30 from the wet dust collector, characterized by comprising
a housing which having a gas inlet which opens vertically
upward and which receives exhaust gas from the wet dust
collector, and a gas outlet which opens in a horizontal
direction, the housing forming a passage which changes
35 the direction of flow of exhaust gas flowing from the gas
inlet to the gas outlet from the vertically downward
direction to the horizontal direction, at least one
partitioning member arranged in the housing and
partitioning the inside space of the housing, the
partitioning member being provided with a dam part for
damming dust-containing water flowing along a surface of
the partitioning member, at an end of the partitioning
member at the gas outlet side, and drainage pipes,
connected through drainage ports to the dam part, for
draining the dust-containing water which was dammed by
the dam part from the dam part to the outside of the
housing, wherein the at least one partitioning member is
arranged at the gas outlet side so as to partition an
inside space of the housing into upper and lower spaces,
and wherein a region of the partitioning member which
15 adjoins the dam part in the direction of flow of gas in
the housing is inclined toward the downstream side
downward by an inclined angle 8, the inclined angle 8
being 5O<8125O.
[ 0 0 18 1 The partitioning member may be provided with a
20 deflector which directs dust-containing water flowing
along the surface of the partitioning member toward the
drainage port.
Brief Description of Drawings
25 [0019] FIG. 1 is a schematic view of a converter
exhaust gas treatment facility which is provided with a
separator according to the present invention.
FIG. 2 is a schematic cross-sectional view of a separator
according to a first embodiment of the present invention.
30 FIG. 3 is a schematic partial cross-sectional perspective
view which shows cut away a portion of the partitioning
member near the gas outlet.
FIG. 4 is a cross-sectional view along an arrow IV-IV of
FIG. 2.
35 FIG. 5 is a cross-sectional view along an arrow V-V of
FIG. 2.
FIG. 6 is a graph which shows the results of an
experiment.
F I G . 7 is a graph which shows the results of an
experiment.
FIG. 8 is a schematic cross-sectional view of a separator
5 according to a second embodiment of the present
invention.
F I G . 9 is a cross-sectional view along an arrow I X - I X of
F I G . 8.
F I G . 10 is a graph which shows the results of an
10 experiment.
F I G . 11 is a graph which shows the results of an
experiment.
F I G . 12 is a schematic cross-sectional view of a
separator according to a third embodiment of the present
15 invention.
F I G . 13 is a cross-sectional view along an arrow X I I I -
X I 1 1 of F I G . 12.
F I G . 14 is a schematic partial cross-sectional view which
shows cut away a portion of the partitioning member near
20 the gas outlet similarly to F I G . 3.
Description of Embodiments
[0020] Below, referring to the attached drawings, a
separator according to a first embodiment of the present
25 invention will be explained.
The separator 20 according to the present embodiment
is, as one example, used in a converter exhaust gas
treatment facility 10 for treating the exhaust gas of a
converter 11 which treats molten pig iron, in an
30 ironmaking plant shown in F I G . 1. The converter exhaust
gas treatment facility 10 is provided with a hood 12
positioned above the converter 11, a skirt 13 connecting
the converter 11 and the hood 12 in a sealed state, a wet
primary dust collector 15 connected through a duct 19 to
35 the hood 12 and removing dust from the exhaust gas, an
exhaust gas cooler 14 arranged in the duct 19 and cooling
exhaust gas from the converter 11, and a secondary dust
collector 17 arranged downstream of the primary dust
collector 15. In the present embodiment, the separator 20
is arranged between the primary dust collector 15 and the
secondary dust collector 17. Note that, downstream of the
5 secondary dust collector 17, various gas treatment
devices are arranged.
[0021] Here, in the secondary dust collector 17
arranged downstream of the separator 20, a damper 18
which controls the pressure of the gas phase in the
10 converter 11, is arranged. If dust etc. deposits at the
damper 18, it is no longer possible to precisely control
the pressure in the converter 11, and stable operation of
the converter may be obstructed. For this reason, it is
necessary to sufficiently remove the dust by the
15 separator 20 upstream of the secondary dust collector 17.
COO221 The primary dust collector 15 sprays water on
the exhaust gas which runs through it, and traps and
removes the dust in the exhaust gas by the sprayed water.
The exhaust from the primary dust collector 15 contains
20 water drops sprayed to trap and remove dust and
containing dust (below, described as "water drops"). The
separator 20 according to the first embodiment of the
present invention separates the water drops from the
exhaust gas exhausted from the primary dust collector 15.
25 COO231 The separator 20 according to the present
embodiment, as shown in FIG. 2, has a housing 21 which
forms a passage, and at least one partitioning member 30
which partitions the inside space of the housing 21. The
housing 21 has a gas inlet 22 which opens in the vertical
30 direction upward and a gas outlet 23 which opens in the
horizontal direction. Further, the housing 21 has inside
and outside walls 21a and 21b which extend along a
quarter circle with a center angle of approximately 90°,
and side walls 21c and 21d which are connected to the
35 inside and outside walls and extend in the vertical
direction, and forms a passage having a rectangular
cross-section which is vertical to the center axis 0
(FIG. 4) and is bent about 90'. In this way, the housing
21 extends in the vertical direction at a first portion
adjoining the gas inlet 22, and extends in the horizontal
direction at a second portion adjoining the gas outlet
23. Further, at the outside wall 21b near the gas outlet
23, a water outlet 24 which opens downward is provided.
[0024] Each partitioning member 30 is comprised of a
sheet member extending substantially in parallel with the
inside and outside walls 21a and 21b. At the end of the
downstream side in the direction of flow of gas, a dam
part 31 is formed. In the present embodiment, two
partitioning members 30 are provided in the housing 21.
As shown in FIGS. 3 and 4, the inside space of the
housing 21 is partitioned into three spaces in the
vertical direction by the partitioning members 30. At the
partitioning members 30, portions near the gas outlet 23
extend horizontally. The horizontal portions near the gas
outlet 23, as shown in FIG. 4, are inclined so as to
descend downward from the center part in the width
direction (transverse direction with respect to flow of
gas) toward the side walls 21c and 21d of the housing 21.
100251 At the end portions of the partitioning members
30 near the gas outlet 23, dam parts 31 which dam the
dust-containing water flowing along the surfaces of the
partitioning members 30 are provided. In the present
embodiment, the dam parts 31 are formed into halved
tubular shapes by rolling back the ends of the
partitioning members 30 upward. The dam parts 31 extend
across the entire widths of the partitioning members 30
30 in a transverse direction with respect to the direction
of flow of gas.
[0026] Each dam part 31 has a height Ho which is
sufficient for drainage of the dust-containing water,
which flows along the surface of the partitioning member
35 30, from later explained drainage ports 32. The height Ho
can be suitably selected in accordance with the flow rate
of the water drops, but as one example, 200 mmIHo1400 rnrn
is preferable. When the height Ho of the dam part is less
than 200 mm, under ordinary operating conditions, the
dust-containing water sometimes rides over the dam part
131 and resplatters into the exhaust gas which flows
5 through the inside of the housing 21. Further, the higher
the dam part 31, the more difficult it becomes for the
dust-containing water to ride over the dam part 31, but
the greater the pressure loss of the exhaust gas which
flows through the separator 20. On the other hand, under
10 ordinary operating conditions, if the height Ho of the dam
part is 400 mm, the dust-containing water can be
prevented from riding over the dam part, and therefore
making it 400 mm or less is preferable.
[0027] Each partitioning member 30 according to the
15 present embodiment, as explained above, is inclined to
descend downward from the center part in the width
direction toward the both side walls 21c and 21d of the
housing 21, and therefore the dust-containing water
flowing along the surface of the partitioning member 30
20 flows toward the ends of the partitioning member 30 in
the width direction, at the portion near the gas outlet
23. To drain this dust-containing water to the outside of
the separator 20, drainage pipes 28 are connected to the
ends of the dam part 31 in the width direction. At the
25 side faces of the drainage pipes 28 to which the dam part
31 is connected, drainage ports 32 which open toward the
inside of the dam part 31 are formed. The drainage pipes
28 are arranged in the housing 21.
[0028] Further, at the top surface of each
30 partitioning member 30, as shown in F I G . 3, a deflector
35 which directs dust-containing water flowing along the
surface of the partitioning member 30 toward the drainage
ports 32 to the both ends in the width direction, is
arranged. The deflector 35, as shown in F I G . 5, is
35 comprised of an approximately isosceles triangle shaped
member which expands downstream in the direction of flow
of gas in the housing 21. That is, the side faces 35a and
35b which form the two slanted sides of the deflector 35
converge toward each other the further toward the
upstream side. At the center part of the housing 21 in
the width direction, one of the ends of the side faces
35a and 35b are connected with each other whereby a
vertex 35c is formed. The base part 35d which forms the
bottom side of the deflector 35 is arranged in the dam
part 31. Note that, the side faces 35a and 35b of the
deflector 35 are preferably curved slightly in a concave
10 shape, as shown in FIG. 5. Here, the height H of the
deflector 35 is preferably selected from 0.5xH0 rs.@ J , &,L@ -
- 30 %i,..i
.-•
The separator as set forth in claim 5 where'in a flow
rate V of dust-containing water introduced to the housing
and the inclined angle 0 satisfy the following
relationships:
5 When 400 m3/h<~<900 m3/h, 5O<0<25"
When V2900 m3/h, 5"I0I-O.O91xV+106. 81
Dated this 2om day of November, 20 13
ATTORNEY F