U.S. patent number 3,668,836 [Application Number 05/004,947] was granted by the patent office on 1972-06-13 for electrostatic precipitator.
This patent grant is currently assigned to Chemical Construction Corporation. Invention is credited to Robert C. Craig, Harry L. Richardson.
United States Patent |
3,668,836 |
Richardson , et al. |
June 13, 1972 |
ELECTROSTATIC PRECIPITATOR
Abstract
An electrical or electrostatic precipitator is provided with a
grounded collector plate upstream of the electrically charged
wires. The plate is juxtaposed adjacent to the wires and provides
greater overall removal of entrained discrete particles from a gas
stream.
Inventors: |
Richardson; Harry L. (New York,
NY), Craig; Robert C. (Morristown, NJ) |
Assignee: |
Chemical Construction
Corporation (New York, NY)
|
Family
ID: |
21713338 |
Appl.
No.: |
05/004,947 |
Filed: |
January 22, 1970 |
Current U.S.
Class: |
96/66 |
Current CPC
Class: |
B03C
3/09 (20130101) |
Current International
Class: |
B03C
3/09 (20060101); B03C 3/04 (20060101); B03c
003/47 () |
Field of
Search: |
;55/138,137,136,131,132,154,155,150,151,128,129 |
References Cited
[Referenced By]
U.S. Patent Documents
Foreign Patent Documents
|
|
|
|
|
|
|
519,391 |
|
May 1953 |
|
BE |
|
1,334,881 |
|
Jul 1963 |
|
FR |
|
459,961 |
|
May 1928 |
|
DD |
|
471,795 |
|
Feb 1929 |
|
DD |
|
167,939 |
|
Aug 1921 |
|
GB |
|
959,655 |
|
Jun 1964 |
|
GB |
|
Other References
German printed Application No. 1,078,096, printed March 24, 1960,
(2 pages specification, 1 sheet drawing).
|
Primary Examiner: Talbert, Jr.; Dennis E.
Claims
We claim:
1. An apparatus for the electrostatic removal of entrained
particles from a gas stream which comprises a duct, means to pass a
feed gas stream containing entrained discrete particles into said
duct, said duct being of constant cross-sectional area in the
direction of gas flow over the initial portion of the length of
said duct and of progressively increased cross-sectional area in
the direction of gas flow over the terminal portion of the length
of said duct, whereby the linear velocity of flow of said gas
stream is substantially constant through said initial duct portion
and decreases through said terminal duct portion, a first plurality
of parallel spaced apart linear banks of wires, each of said first
banks containing a plurality of parallel spaced apart electrically
charged wires and extending transversely into said initial portion
of said duct, means to continuously maintain an electrical
potential relative to ground on each of the wires in each of said
first banks of wires, a primary foraminous plate, said primary
plate being transversely disposed within said initial portion of
said duct upstream of said first banks of wires and juxtaposed
adjacent to the first bank of said banks of wires, whereby said
feed gas stream containing entrained discrete particles initially
passes through the plurality of openings in said primary plate, a
first plurality of secondary foraminous plates, each of said first
plurality of secondary plates being transversely disposed within
said initial portion of said duct downstream of and spaced from one
of said first banks of wires, a second plurality of parallel spaced
apart linear banks of wires, each of said second banks containing a
plurality of parallel spaced apart electrically charged wires and
extending transversely into said terminal portion of said duct,
means to continuously maintain an electrical potential relative to
ground on each of the wires in each of said second banks of wires,
a second plurality of secondary foraminous plates, each of said
second plurality of secondary plates being transversely disposed
within said terminal portion of said duct downstream of and spaced
from one of said second banks of wires, said primary plate and said
first and second plurality of secondary plates being connected to
ground, the entire periphery of each of said plates being attached
to said duct by a fluid-impervious connection, said primary and
secondary plates being provided with substantially linear slits for
gas flow, said slits being parallel with the wires in said banks,
means to remove separated particles from said primary plate and
said secondary plates, said separated particles being derived from
said feed gas stream, and means to remove a product gas stream of
depleted entrained particles content from said duct downstream of
the last of said second plurality of secondary plates.
2. The apparatus of claim 1, in which said duct is horizontally
oriented, and said primary and secondary plates and banks of wires
are vertically oriented.
3. The apparatus of claim 1, in which said entrained discrete
particles comprise liquid droplets.
4. The apparatus of claim 1, in which said entrained discrete
particles comprise solid particles.
5. The apparatus of claim 1, in which said duct is of rectangular
cross-section.
Description
BACKGROUND OF THE INVENTION
1. Field of the Invention
The invention relates to the removal of entrained discrete
particles from a gas stream by electrical or electrostatic
precipitation. The entrained discrete particles may consist of
liquid droplets or solid particles such as fume, dust, soot, fly
ash or the like, chemical particles from a chemical process gas
stream such as the off-gas from a fluid bed reactor or ore roaster,
etc. The invention is generally applicable to the treating of
diverse gas streams, such as flue gas, a chemical process gas
stream, or the tail gas from a chemical process, and is especially
useful in the prevention of air pollution due to the discharge of
waste gas streams containing entrained discrete particles into the
atmosphere.
2. Description of the Prior Art
Numerous arrangements of electrical or electrostatic precipitators
have been suggested in the prior art, including types in which the
electrically charged wires are followed by wire mesh or fiber mass
filters or the like. Other types provide grids, wire mesh or rods
downstream of the charged wires. Typical patents showing various
configurations include U. S. Pats. Nos. 3,049,848; 2,990,912;
2,989,146; 2,973,054; 2,847,082; 2,822,058; 2,764,254; 2,715,944,
2,672,947, 2,593,377; 2,582,133 and 2,556,982 and British Pats.
Nos. 962,773 and 444,333.
SUMMARY OF THE INVENTION
In the present invention, a gas or vapor stream laden with
entrained discrete particles consisting of components such as those
described supra or the like, is passed through a duct or similar
gas passage means such as a conduit or elongated container. A first
perforated plate is transversely disposed in the duct, so that the
gas stream initially passes through the openings in the first
plate, which is succeeded by alternate juxtaposed transverse banks
of parallel spaced apart wires and secondary perforated plates. The
plates are grounded and the wires are provided with an electrical
or electrostatic charge, so that a high voltage potential is
maintained between the ionizing wires and the grounded plates, and
the entrained discrete particles are deposited from the gas stream
onto the plates, due to an electrostatic precipitation mechanism in
which the particles receive a charge from the wires and are
discharged by and onto the plates. It has been determined that the
provision of the first plate prior to the initial wire or bank of
parallel wires is highly advantageous, since a considerable
proportion of particles will deposit on the first plate upstream of
the initial bank of wires, and thus the overall particle collection
efficiency and removal of particles from the gas stream are greatly
improved.
It is an object of the present invention to remove entrained
discrete particles from a gas stream in an improved manner, by the
provision of improved apparatus.
Another object is to provide an improved electrical or
electrostatic precipitator.
A further object is to increase the particles removal efficiency of
an electrostatic precipitator.
An additional object is to remove entrained discrete particles from
a gas stream in an electrostatic precipitator by the provision of a
collector plate upstream of the first bank of ionizing wires.
These and other objects and advantages of the present invention
will become evident from the description which follows.
DESCRIPTION OF THE DRAWINGS AND PREFERRED EMBODIMENTS
Referring now to the drawings,
FIG. 1 is a sectional elevation view of one embodiment of the
invention,
FIG. 2 is a sectional plan view of FIG. 1, taken on section
2--2,
FIG. 3 is an isometric view of the preferred embodiment of the
collector plates shown in FIGS. 1 and 2, and
FIG. 4 is an isometric view of an alternative embodiment and
species of collector plate, showing associated ionizing wires.
Referring now to FIG. 1, a gaseous or vaporous stream 1 containing
entrained discrete particles is passed via fan or blower 2 as
stream 3 into the duct 4, which in this embodiment of the invention
is generally horizontally oriented and of a rectangular or square
cross-section. The duct 4 is connected to ground via ground wire or
connection rod 5. The gas stream within duct 4 passes initially
through the spaced openings in the foraminous collector plate 6,
which is disposed upstream of and adjacent to the primary ionizer
wires or rods 7. The elements 7 are provided with an electrical
charge or potential or an electrostatic charge by means of charge
lead wire 8 which connects via an insulated connection through duct
4 to wire 7. Electrical potential is furnished to wire 8 via the
main high potential wire or busbar line 9, which extends from a
suitable high potential source 10, which may be a transformer and
rectifier combination or the like. Unit 10 furnishes a high voltage
potential, either negative or positive, to busbar 9, and the
opposite polarity of unit 10 may be grounded, either via duct 4 or
directly to ground. The influence of the electrical charge imparted
to wire 7 causes the entrained discrete particles in the gas
stream, which may be either liquid droplets or solid particles such
as soot, dust, fly ash, fume, fog or the like, to attain an
electrical charge relative to ground, and a portion of the discrete
particles are discharged by and deposited onto the primary
collector plate 6.
The gas stream within duct 4 next passes in series through the
openings in the plurality of downstream foraminous secondary
collector plates 11, between which are disposed the secondary
potential or ionizing wires 12, so that an alternative series of
ionizing wires or rods 12 and secondary collector plates 11 are
provided. An electrical charge or potential is provided on wires 12
via secondary lead wires 13, which extend from busbar 9 through
duct 4 via an insulated connection to the wires 12. Further amounts
of discrete particles are deposited from the gas stream onto the
collector plates 11. A preferred configuration of duct 4 is shown
in FIG. 1, in which the downstream portion 14 of duct 4 increases
progressively in cross-sectional area in the direction of gas flow,
so that the linear velocity of gas flow decreases in section 14.
The decrease in gas flow in section 14 aids in removal of discrete
particles by preventing re-entrainment of deposited material from
plates 11 into the gas stream due to turbulence or high gas
velocity. The final purified or cleansed gas stream, now having a
depleted or negligible content of entrained discrete particles,
flows into outlet duct or conduit 15, which extends from section 14
and passes the gas stream 16 to suitable utilization or atmospheric
discharge via a stack or the like, not shown.
Referring now to FIG. 2, a sectional plan view of the apparatus is
shown, which further illustrates the arrangement of the perforated
or foraminous primary collector plate 6, the ancillary or secondary
collector plates 11, and the linear banks of parallel ionizing
wires or rods 7 and 12 disposed between collector plates.
FIG. 3 shows a typical collector plate provided with circular
openings 17 for gas flow.
FIG. 4 shows an alternative embodiment of a collector plate, in
which vertical slits 18 are provided for gas flow, with the slits
18 preferably being parallel with the ionizing wires or rods 7,
which are juxtaposed and spaced from plate 6.
Numerous alternatives within the scope of the present invention
will occur to those skilled in the art. The duct 4 and
appurtenances such as section 14 may be horizontally or vertically
oriented, or mounted in an inclined position. In all such cases the
collector plates 6 and 11 and associated ionizing wires 7 and 12
will extend substantially transversely within the duct. A single
downstream collector plate 11 disposed adjacent to wire 7 may be
provided in some cases, in which case the banks of wires 12 and
associated downstream collector plates may be omitted. Suitable
rapping or shaking devices or means will usually be provided in
practice, to intermittently or continuously agitate or shake the
collector plates to remove deposited material. Rapping devices may
also be provided for wires 7 and 12. In other instances, the plates
and wires may be intermittently washed down with a suitable wash
liquid such as water or a solvent for the deposited discrete
particles. In instances when the entrained discrete particles in
stream 1 consist of liquid droplets, continuous drainage of
deposited liquid from the collector plates 6 and 11 under the
influence of gravity will usually suffice to remove deposited
material. The foraminous plates 6 and 11 may be provided with
openings which are circular, elliptical, square, triangular or the
like, or slits such as shown in FIG. 4 may be provided in practice.
In some cases the collector plates may even consist of a series of
flat parallel juxtaposed strips, preferably with each strip
oriented opposite to an ionizing wire. Equal distribution of
voltage to the various wire banks 6 and 12 may be assured in
practice by the provision of various electrical chokes or the like.
Half-wave or full wave electrical potential may be provided in
suitable instances. In many cases, the fan or blower 2 will be
provided downstream of the apparatus so that the blower draws the
impurity-laden gas stream through the unit and thus handles only
cleaned gas or vapor. In power plants, this arrangement is required
by insurers, with the fan or blower 2 handling only flue gas free
of fly ash.
An example of laboratory tests of the apparatus of the present
invention will now be described.
EXAMPLE
A test apparatus was provided with five parallel banks of ionizer
wires, with each bank of wires being followed by a grounded
perforated collector plate. A voltage of 40 kv. was impressed on
the wires and the apparatus was operated with an additional primary
collector plate prior to the first bank of wires. An air stream
laden with entrained particles of fly ash dust was passed through
the apparatus and the collection efficiency was measured. The
apparatus was then operated in a second test without the primary
collector plate and the collection efficiency was measured.
Following are the test results.
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Fly Ash Collected Per Hour
Plate Number Test No. 1 Test No. 2 With primary Without primary
Plate Plate Grams % of total Grams % of total
__________________________________________________________________________
1 106 15.1 -- -- 2 244 35.0 237 38.0 3 149 21.3 163 26.2 4 118 16.9
104 16.7 5 61 8.8 97 15.6 6 20 2.9 22 3.5 Total 698 100.0 623 100.0
Feed Rate, Grams/Hr: 754 744 % Collection Efficiency 92.5% 84.0%
__________________________________________________________________________
It is evident that greater efficiency of collection and greater
total amounts of fly ash removal were attained due to the provision
of the primary plate No. 1 prior to the first bank of ionizer
wires. The unit was operated with foraminous collector plates
having perforations consisting of 0.5 inch diameter holes in 22
gauge carbon steel plate. The holes were in staggered rows with a
total open area of 48 percent. Air velocity was 3 feet/second and
the dust loading was 3 grs./SCF.
* * * * *