U.S. patent number 3,692,285 [Application Number 05/116,999] was granted by the patent office on 1972-09-19 for multi-stage calciner.
Invention is credited to Hazelton H. Avery.
United States Patent |
3,692,285 |
Avery |
September 19, 1972 |
MULTI-STAGE CALCINER
Abstract
A multi-stage apparatus for drying and hardening ion ore pellets
as they flow over a high-temperature sloping grid and pass through
separated pre-heating and pre-cooling full flow areas. The
apparatus provides a drying stage separated by a pre-heating area
from the indurating stage that in turn is separated by a
pre-cooling area from the cooling stage, with a single directional
flow of air forced longitudinally through each stage to
sequentially dry, heat and cool the green pellets as they flow
through the apparatus.
Inventors: |
Avery; Hazelton H. (Aurora,
IL) |
Family
ID: |
22370487 |
Appl.
No.: |
05/116,999 |
Filed: |
February 19, 1971 |
Current U.S.
Class: |
432/79; 432/99;
432/238; 432/100 |
Current CPC
Class: |
C22B
1/2413 (20130101); B01J 8/125 (20130101); F26B
17/1433 (20130101) |
Current International
Class: |
C22B
1/14 (20060101); C22B 1/24 (20060101); B01J
8/08 (20060101); B01J 8/12 (20060101); F26B
17/14 (20060101); F26B 17/12 (20060101); F27b
001/10 () |
Field of
Search: |
;263/30,19B,21A
;34/57A |
References Cited
[Referenced By]
U.S. Patent Documents
Primary Examiner: Camby; John J.
Claims
Having thus described my invention, what I claim as new and desire
to protect by Letters Patent is:
1. A multi-stage calciner apparatus comprising a vertically
disposed cylinder having an upper inlet and lower discharge chutes
for the material to be indurated, wherein the improvement
comprises
a. means for dividing the cylinder into superimposed stages for the
sequential indurating treatment of fluidized material passing
therethrough,
b. a plurality of spherical elements of different diameters
supported upon said dividing means so as to provide heated sloping
grids over which the material to be treated flows in a continuous
path,
c. means external of said cylinder between certain of said stages
for receiving and pre-treating the material as it passes between
successive stages provided by said apparatus during its continuous
flow therethrough, and
d. means for supplying a continuous flow of gas through said
different stages of said apparatus for effecting different
temperature treatment of the material flowing continuously
therethrough.
2. A multi-stage calciner apparatus as defined by claim 1 wherein
said means for dividing the cylinder into superimposed stages
comprises a plurality of inverted conical shelves having a center
opening providing open communication between each of the
superimposed stages, with said spherical elements supported upon
said shelves and covering said center openings provided therein so
as to form a sloping grid thereon through which said continuous
flow of gas is permitted to pass and over which the fluidized
material flows from one stage to the next.
3. A multi-stage calciner apparatus as defined by claim 1 wherein
said spherical elements are provided with externally projecting
means that cooperate with other of said elements to maintain said
elements in their pre-arranged position after they are placed in a
stacked relation on said dividing means to form the sloping grid
over which the fluidized material will flow.
4. A multi-stage calciner apparatus as defined by claim 1 further
defined by having means providing a pressurized jacket radially
disposed about one of the superimposed stages formed in the
cylinder with said jacket having open communication with said means
for supplying a continuous flow of gas to said apparatus for
pressurizing said jacket about said certain stage during the
operation of the apparatus.
5. A multi-stage calciner apparatus as defined by claim 2 wherein
said spherical elements are provided with externally projecting
means that cooperate with other of said elements to maintain said
elements in their pre-arranged position after they are placed in a
stacked relation on said dividing means to form the sloping grid
over which the fluidized material will flow.
6. A multi-stage calciner apparatus as defined by claim 2 wherein
said spherical elements are each provided with a laterally
extending lugs which cooperates with the lug on other elements to
maintain said elements in their pre-arranged position upon said
inverted conical shelves and over said center openings provided
thereby after they are placed in a stacked relationship with
respect to one another so as to provide a sloping grid over which
the fluidized material will flow.
7. A multi-stage calciner apparatus as defined by claim 2 further
defined by having means providing a pressurized jacket radially
disposed about one of the superimposed stages formed in the
cylinder with said jacket having open communication with said means
for supplying a continuous flow of gas to said apparatus for
pressurizing said jacket about said certain stage during the
operation of the apparatus.
8. A calciner apparatus for heating and freely transporting
materials to be treated, over a sloping surfaced fluid grid,
wherein the improvement comprises
a. a chamber formed within the apparatus by an inverted conically
shaped wall providing an opening at the depending vertex
thereof,
b. a pressurized annular section about said inverted conically
shaped wall,
c. means for pressurizing said section,
d. a combustion chamber within said pressurized section and having
open communication therewith and with said opening provided at the
depending vertex of said wall,
e. means for heating the atmosphere of said combustion chamber,
f. a grid of ceramic balls of different diameters on said wall
arranged to provide a sloping surface for the material heated and
transported thereover,
g. and a discharge means associated with the lowermost edge of said
sloping surface grid through which the treated material is passed
from said apparatus.
Description
SUMMARY OF THE INVENTION
A multi-stage indurating unit which dries and hardens iron ore
pellets, consisting of a vertical cylinder internally divided into
drying, indurating, and cooling stages by sloping ceramic ball
grids. A pair of full-flow moving bed areas external of the divided
stages are utilized to pre-heat and pre-cool the material as it
passes into and exits from the indurating stage. The unit is so
constructed as to provide an annular pressurized chamber about the
refractory-lined indurating stage to prevent deterioration of and
leaking from the metallic wall thereof of the combustible hot gases
utilized in such stage.
GENERAL DESCRIPTION
The invention as hereinafter described will be best understood by
reference to the drawings which disclose the preferred embodiments
of the invention, and in which:
FIG. 1 is a cross-sectional view of the multi-stage apparatus of
the invention;
FIG. 2 is a fragmentary cross-sectional view of a high-temperature
fluid bed unit; and
FIG. 3 is a perspective view of one of the lugged ceramic balls
used to form the sloping grids utilized in the invention;
FIG. 4 is a schematic view showing the use of filler blocks
utilized to control the amount of open area between the ceramic
balls when formed into a sloping bed arrangement; and
FIG. 5 is a perspective view of the filler block.
As viewed in FIG. 1, the apparatus of this invention comprises a
vertical cylinder 10 having an insulated outer metallic wall 11,
the medial portion 12 of which is stepped radially from an inner
refractory lining 13 so as to provide an annular chamber 14. The
top wall 15 of the cylinder 10 is provided with an exhaust 16,
while the bottom wall 17 has connected thereto a removable
clean-out plate 18. Adjacent to the bottom wall 17 of the cylinder
10 is a discharge chute 19 having associated therewith a valve 20
for controlling the discharge of hard pellets from the apparatus.
There is also provided adjacent the bottom wall 17 a fluidizing
blower 21 having open communication with the interior of the
cylinder 10 and a conduit 22 communicating with the annular chamber
14 for the purpose of pressurizing the same during the operation of
the apparatus.
A surge bin 23 is provided having an inlet chute 24 which extends
through the metallic insulated wall 11 and into the upper region of
the cylinder 10. The cylinder 10 is provided with three stages by a
pair of internal conical shelves 25 and 26, each of which provides
a circular opening 27 and 28 at the apex of its conical shape.
These shelves 25 and 26 divide the cylinder 10 into a drying stage
29, which occupies the area of the cylinder vertically above the
shelf 25, an indurating stage 30 which occupies the area between
the shelves 25 and 26, and a cooling stage 31 which occupies the
area below the lowermost shelf 26.
In the cooling stage 31 there is provided a downwardly sloping
perforated plate grid 32 over which the hardened pellets flow into
the discharge chute 19. Also in the cooling stage 31 and
immediately beneath the center opening 28 formed in the shelf 26,
there is a radiation shield 33 positioned immediately beneath a
burner unit 34.
While the description of this invention is directed to pelletizing
iron ore, it should be understood that it is adaptable for many
materials which normally do not respond to fluidization over a
heated sloping surface.
The method employed for adapting the apparatus to these other
materials resides in the fact that on each of the shelves 25 and 26
there is provided a sloping grid constructed from a plurality of
various sized ceramic balls 35. To form the ceramic balls into a
sloping grid, each ball 35, as seen in FIG. 3, is provided with a
horn or lug 37 which prevents each ball from rolling or sliding
down the sloping grid as it is constructed. To regulate the amount
of gases passing through the sloping grids provided by the balls
35, a triangularly shaped filler block 38, the faces of which are
circularly recessed as at 39 as seen in FIG. 5, may be inserted
between the balls 35 making up such grids.
Adapted to be positioned externally of the cylinder 10 are a pair
of full flow leg sections 40 and 41. referring to the leg section
40, it is shown as comprising a V-shaped duct 42 which has
associated therewith an air-heating unit 43. One leg of the
V-shaped duct 42 has open communication with the lowermost side
edge of the sloping grid positioned on the uppermost shelf 25. The
other section of the duct has open communication with the
indurating stage 30 at a point on the high side of the sloping grid
supported on the shelf 26. The construction of the leg section 41
is identical to that of section 40, except that its V-shaped duct
44 carries an air-cooling unit 45, with one section of the duct
communicating with the low side of the sloping grid constructed on
shelf 26 and with its other portion discharging upon the perforated
plate grid 32, all as shown.
In operation the fluidizing blower 21 forces a stream of gas into
the cooling stage 31 through the perforated plate grid 32 around
the radiation shield 33 and over the burner 34. At this stage, the
burner will heat the gas so that it passes up through the sloping
grid of ceramic balls 35 through the indurating stage 30 into the
opening 27 formed in the shelf 25 around the sloping grid of
ceramic balls 35 supported thereby and into the drying stage 29 and
out the exhaust 16. Simultaneously a certain amount of the gases
will be forced through the conduit 22 into and pressurizing the
chamber 14 surrounding the indurating stage 30. At the same time,
green pellets are fed from the surge bin 23 through its chute 24
into the sloping grid of ceramic balls 35, where such pellets are
dried at a temperature of approximately 750.degree. F.
As the material flows over the grid of ceramic balls 35, it will
pass into the duct 42 of the pre-heating leg section 40. There the
air-heating unit 43 introduces forced heated air in a direction
opposite to the flow of material thereover, wherein the material is
heated to approximately 2,000.degree. F. Here it will pass into the
indurating stage 30 and onto the sloping grid of ceramic balls 35
where it is subjected to temperatures ranging up to 2,400.degree.
F. From this stage it passes into the duct 44 of the pre-cooling
section 41, wherein it is subjected to a flow of pre-cooled gases
before it flows onto the perforated plate grid 32, where it is
subjected to the full stream of cooling gases, an thence out the
discharge chute 19.
In FIG. 2 there is fragmentarily shown a high temperature fluid bed
unit 46 which utilizes the sloping grid of ceramic balls 47 of
different diameters. Here the material may be processed on a batch
or continuous basis. In this device the burner unit 48 heats the
gases in a triangularly shaped chamber 49 which is surrounded by a
pressurized chamber 50 into which the gases from a fluidizing
blower 51 are introduced. The discharge of the material is
controlled by a suitable discharge valve 52 located in a discharge
chute 53.
The heretofore described apparatus permits the controlled heating
and transporting of many materials by reason of the utilization of
the sloping-surface, fluid grids novelly constructed from ceramic
balls. The liberal use of balls of different diameters so as to
build up a high or introduction side, tends to even out any
pressure drop across the grid due to the increased depth of the
piled balls to form the sloping grid. The employment of the
pressurized annular chamber about the refractory lining in the
indurating stage, prevents the metallic material from eroding, or
the hot gases escaping through pin-hole leaks which would follow
from erosion. The pressurized chamber also cools the exterior
surface of the unit, notwithstanding the high temperatures employed
therein.
While I have illustrated and described the preferred form of
construction for carrying my invention into effect, this is capable
of variation and modification without departing from the spirit of
the invention. I, therefore, do not wish to be limited to the
precise details of construction set forth, but desire to avail
myself of such variations and modifications as come within the
scope of the appended claims.
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