Title: Transfer of hot feed materials from a preprocessing plant to an electric smelting or melting furnace
Abstract: Apparatus for transferring hot material between a preprocessing plant and an electric furnace has an enclosed housing extending between the plant and the furnace and within which a controlled atmosphere is maintained, at least one bin having at least one compartment receiving feedstock material at a delivery station from the plant, mechanism for shuttling the at least one bin along a path within the housing between the delivery station and discharge tubes above and leading into the furnace at distributed locations, and discharge mechanism for dropping material from each compartment into a discharge tube. The path may be horizontal, vertical, or inclined to suit the relative locations of the preprocessing plant and the battery. Each bin is usually each divided to feed multiple tubes. The shuttling mechanism may be a hoist or a railway or cable span, and the discharge mechanism is typically a means for tipping the bin. The bin should be such that the depth of material therein during transit is sufficiently low to limit its coagulation of the material in transit, if this is a problem.
Patent Number: 6,953,337 Issued on 10/11/2005 to McCaffrey
| Inventors:
|
McCaffrey; Felim P. (Toronto, CA)
|
| Assignee:
|
Hatch Ltd. (Mississauga, CA)
|
| Appl. No.:
|
472349 |
| Filed:
|
March 19, 2002 |
| PCT Filed:
|
March 19, 2002
|
| PCT NO:
|
PCT/CA02/00387
|
| 371 Date:
|
June 3, 2004
|
| 102(e) Date:
|
June 3, 2004
|
| PCT PUB.NO.:
|
WO02/07729 |
| PCT PUB. Date:
|
October 3, 2002 |
Foreign Application Priority Data
| Current U.S. Class: |
432/86; 373/79 |
| Intern'l Class: |
F27D 003/00; F27D 015/00 |
| Field of Search: |
432/86,87,93,135,239
219/520,523
373/9,79,81,115,142
|
References Cited [Referenced By]
U.S. Patent Documents
| 1944521 | Jan., 1934 | Miguet et al.
| |
| 3033673 | May., 1962 | Collin et al.
| |
| 3472649 | Oct., 1969 | Sibakin et al.
| |
| 3472650 | Oct., 1969 | Sibakin et al.
| |
| 3746325 | Jul., 1973 | Freeberg et al.
| |
| 3752897 | Aug., 1973 | Atsukawa.
| |
| 3913898 | Oct., 1975 | Wolters.
| |
| 4390168 | Jun., 1983 | Muller.
| |
| 4402083 | Aug., 1983 | Paskarbeit et al.
| |
| 4624003 | Nov., 1986 | Eirich et al.
| |
| 4642048 | Feb., 1987 | Kim.
| |
| 4963182 | Oct., 1990 | Bishop et al.
| |
| 5149062 | Sep., 1992 | Matsuo et al.
| |
| 5238484 | Aug., 1993 | Pirklbauer et al.
| |
| 5390212 | Feb., 1995 | Bonnet et al.
| |
| 6155333 | Dec., 2000 | Vallomy.
| |
| Foreign Patent Documents |
| 0247133 | Dec., 1987 | EP.
| |
| 1536190 | Aug., 1968 | FR.
| |
| 2155160 | Sep., 1985 | GB.
| |
Primary Examiner: Wilson; Gregory
Attorney, Agent or Firm: Kirkpatrick & Lockhart Nicholson Graham LLP
Parent Case Text
CROSS-REFERENCE TO RELATED APPLICATIONS
This application claims the benefit of International Application No. PCT/CA02/00387,
which was filed on Mar. 19, 2002 and published under PCT Article 21(2) in English
and which claims the benefit of Canadian Patent Application No. 2,341,772 filed
on Mar. 22, 2001.
Claims
1. Apparatus for transferring hot material between a preprocessing plant and
an electric furnace comprising an enclosed housing extending between the plant
and the furnace and within which a controlled atmosphere is maintained, at least
one bin having at least one compartment receiving material at a delivery station
from the plant, mechanism for shuttling the at least one bin along a path within
the housing between the delivery station and discharge tubes above and leading
into the furnace at distributed locations, and discharge mechanism for dropping
material from each compartment into a discharge tube; wherein the shuttling mechanism
comprises one of a hoist, a railway, and a cable span.
2. Apparatus according to claim 1, wherein the housing extends vertically.
3. Apparatus according to claim 1, wherein the housing extends horizontally.
4. Apparatus according to claim 1, wherein the discharge tubes have funnels at
their upper ends grouped to receive material simultaneously from the compartments
of a bin.
5. Apparatus according to claim 1, wherein the bin is discharged by tipping.
6. Apparatus according to claim 1, wherein the bin is a compartmented tray.
7. Apparatus according to claim 1, wherein the bin comprises multiple tubular compartments.
8. Apparatus according to claim 1, having two bins and two shuttling mechanisms,
one bin being at the delivery station while the other is shuttled to the discharge tubes.
9. Apparatus according to claim 1, wherein the housing excludes the ambient atmosphere.
10. Apparatus for transferring hot material between a preprocessing plant and
an electric furnace comprising an enclosed housing extending between the plant
and the furnace and within which a controlled atmosphere is maintained, at least
one bin having at least one compartment receiving material at a delivery station
from the plant, mechanism for shuttling the at least one bin along a path within
the housing between the delivery station and discharge tubes above and leading
into the furnace at distributed locations, and discharge mechanism for dropping
material from each compartment into a discharge tube; wherein the bin comprises
multiple tubular compartments.
11. Apparatus according to claim 10, wherein the housing extends in at least
one of a vertical and a horizontal direction.
12. Apparatus according to claim 10, wherein the shuttling mechanism comprises
one of a hoist, a railway, and a cable span.
13. Apparatus according to claim 10, wherein the discharge tubes have funnels
at their upper ends grouped to receive material simultaneously from the compartments
of a bin.
14. Apparatus according to claim 10, wherein the bin is discharged by tipping.
15. Apparatus according to claim 10, wherein the bin is a compartmented tray.
16. Apparatus according to claim 10, wherein the bin comprises multiple tubular compartments.
17. Apparatus according to claim 10, having two bins and two shuttling mechanisms,
one bin being at the delivery station while the other is shuttled to the discharge tubes.
18. Apparatus according to claim 10, wherein the housing excludes the ambient atmosphere.
19. Apparatus for transferring hot material between a preprocessing plant and
an electric furnace comprising an enclosed housing extending between the plant
and the furnace and within which a controlled atmosphere is maintained, at least
one bin having at least one compartment receiving material at a delivery station
from the plant, mechanism for shuttling the at least one bin along a path within
the housing between the delivery station and discharge tubes above and leading
into the furnace at distributed locations, and discharge mechanism for dropping
material from each compartment into a discharge tube; having two bins and two shuttling
mechanisms, one bin being at the delivery station while the other is shuttled to
the discharge tubes.
Description
FIELD OF THE INVENTION
This invention relates to the transfer of hot feed materials from a preprocessing
plant to an electric smelting or melting furnace. The preprocessing plant may be
a kiln, a direct reduction facility, or a rotary hearth furnace, in which an ore
is calcined, sintered or reduced.
BACKGROUND OF THE INVENTION
The problems associated with the transportation of hot feed materials arise from
their inherent characteristics, which may include some or all of the following:
(a) The materials are hot (up to 1000° C.), are normally abrasive and
normally contain a significant amount of fines. This combination of characteristics
has a strong negative impact on mechanical and electrical equipment, to a degree
that makes it impractical to use certain equipment and devices which perform satisfactorily
over long periods with less aggressive materials.
(b) Once the materials, for example pre-reduced calcined laterite, are exposed
to air, they may begin to burn, releasing pollutants which must then be captured.
(c) The process of pre-reduction in a kiln or other device reduces the oxygen
content of metallic ores. The subsequent burning in air reverses the reduction
process and thereby wastes some of the energy used in reduction.
(d) Certain reduced ores, such as partially reduced iron ore, have a tendency
to agglomerate if piled for even short periods of time. Thus, batch transportation
in a container with a hopper-shaped bottom may cause sufficient agglomeration in
5-10 minutes to prevent the material from flowing out of the opening in the container bottom.
A typical hot material transfer system might consist of the following:
(a) A valve on the output end of a kiln discharges calcine into a container
below, which is mounted on a transfer car.
(b) Once the container is filled, the transfer car travels into the furnace
building with the full container, which is then picked up by the furnace-charging
crane. The crane raises the container to an elevation just above the top of the
furnace feed bins, which are located directly above the furnace.
(c) The crane places the container on the bin and the action of setting
the container down causes it to discharge the calcine down into the bin.
The transfer process just described is characterized by significant release of
pollutants, at the kiln discharge valve, from the container itself while in transit,
and at the loading of the feed bin from the container.
The total distance travelled by the container, vertical and horizontal, is, in
a typical case, about 60 meters. The provision of an emission control system, large
enough to cover the arrangement just described, and consisting of hood, ducting
fan, baghouse and controls, imposes a large financial burden, in both capital and
operating costs. Systems using drag chain conveyors or other transportation methods
have similar problems.
One transfer system which has been widely discussed but not widely employed,
consists of placing the kiln at a higher elevation than the furnace and using gravity
to transfer the hot material downwards through closed pipes or ducts. This has
the following advantages:
(a) Pollution and dust are eliminated since the material is enclosed at
all times and in an oxygen-starved atmosphere.
(b) A continuously discharging source of material can be continuously distributed
into the furnace below without resorting to batch feeding the furnace. This is
particularly beneficial with an electric smelting furnace.
(e) No complex mechanical/electrical equipment is required which could be
adversely impacted by the hot, abrasive, dusty material.
The operational advantages of this system are offset by the very high capital
cost involved in locating a kiln or a rotary hearth furnace 30 m± above grade
elevation, particularly in areas of high seismic risk.
In practical situations, the material may need to be fed to the furnaces at a
substantially different, but usually higher, level than that at which it is discharged
from the calcining plant. The calcine needs to be distributed in a controlled manner
through multiple feed ports into the furnace.
It is an object of the invention to provide a transfer system which addresses
the above problems.
SUMMARY OF THE INVENTION
According to the invention, apparatus for transferring hot material between
a preprocessing plant and an electric furnace comprises an enclosed housing extending
between the plant and the furnace and within which a controlled atmosphere is maintained,
at least one bin having at least one compartment receiving feedstock material at
a delivery station from the plant, mechanism for shuttling the at least one bin
along a path within the housing between the delivery station and discharge tubes
above and leading into the furnace at distributed locations, and discharge mechanism
for dropping material from each compartment into a discharge tube. The path may
be horizontal, vertical, or inclined, to suit the relative locations of the preprocessing
plant and the battery. Each bin is usually each divided to feed multiple tubes.
The shuttling mechanism may be a hoist or a railway or cable span, and the discharge
mechanism is typically a means for tipping the bin. The bin should be such that
the depth of material therein during transit is sufficiently low to limit coagulation
of the material in transit, if this is a problem.
This arrangement enables the entire transfer operation to be carried out in
a controlled atmosphere, with transfer time reduced to a minimum, and without any
substantial static accumulation of material, while, at the same time, allowing
the transfer components to be very simple and robust with a minimum need for maintenance.
Further features of the invention will be apparent from the following description
of presently preferred embodiments of the invention with reference to the accompanying drawings.
SHORT DESCRIPTION OF THE DRAWINGS
FIG. 1 is a vertical section through a first embodiment of apparatus according
to the invention, and an associated furnace;
FIG. 2 is a schematic plan view, showing tubes connecting between a first, lower
group of discharge chutes and the furnace roof;
FIG. 3 is a schematic plan view, showing tubes connection between a second,
upper group of discharge chutes and the furnace roof;
FIG. 4 is a schematic elevation corresponding to FIG. 2;
FIG. 5 is a schematic elevation corresponding to FIG. 3;
FIG. 6 is a plan view of a second embodiment of apparatus according to the invention,
part of an associated calcining plant, and a furnace with a top cover of passages
between the plant and the furnace omitted for clarity;
FIG. 7 is a corresponding side elevation, with a side cover of a passage omitted
for clarity; and
FIG. 8 is a vertical cross-section of the apparatus and furnace on the line
8—8 in FIG. 7.
DESCRIPTION OF THE PREFERRED EMBODIMENT
Referring to FIG. 1, an enclosed tower
2 is erected alongside a
shed
4 housing an electric furnace
6 with side walls
8, a
floor
10, a roof
12 and a row of electrodes
14 descending
through the roof from electrode and control mechanisms
16 receiving electrical
supply from transformers
18. The construction of the furnace is conventional
and forms no part of the invention beyond that the furnace roof
12 has ports
through which tubes
20,
21,
22 and
23 deliver preprocessed
material to the furnace.
The tower
2 contains two hoists
24 mounted for limited movement
on a platform
26 on a horizontal axis perpendicular to the axis of the row
of furnace electrodes
14. Pairs of funnel assemblies
28a,
28b,
29a,
29b,
30a,
30b,
and
31a,
31b are mounted on the wall of the tower nearest
the shed
4 at different levels above the furnaces
6. The funnel assemblies
are each divided into four funnels, each of which forms an enlarged opening to
one of the tubes through which calcine is delivered to the furnace. The connections
of the tubes between the chutes and furnace are illustrated in FIGS. 2 through 5.
Each hoist is connected by cables
42 to a frame
32 supporting
a compartmented tray
34 through pivots
36 so that the tray may be
tipped as shown in its uppermost depiction in FIG. 1 by a tipping mechanism
40
to deliver the contents of its compartments into the funnels of an adjacent funnel
assembly. Each tray is approximately the same width as a funnel assembly. When
a tray
34 is in the lowest position shown in FIG. 1, its compartments receive
material in turn through a chute
38 from a calcining plant (not shown).
The compartments need not be filled equally, thus providing great flexibility in
determining how material is distributed within the furnace. Once a tray is loaded,
its associated hoist is operated to raise it to a position just above a funnel
assembly to which it is to deliver its load, and it is then moved to the right
(with reference to its depiction in FIG. 1) to the middle position shown in that
drawing, and hoisted further upwards so that the tipping mechanism discharges its
contents into the chute, whereafter it is withdrawn to the left and lowered to
its initial position at the bottom of the tower to receive further material. One
plafform
26 and its associated hoist serves in turn the funnel assemblies
28a, 29a, 30a, and
31a, while
the other serves in turn the funnel assemblies
28b, 29b,
30b and
31b, servicing each discharge chute so
as to distribute the material throughout the furnace. The hoist
24 and tray
34 are duplicated to eliminate the need for movement within the tower parallel
to the electrodes, with operation of the hoists timed so that one tray is always
available to receive a continuous stream of material from the feed chute
38.
The hoist cables
42 are crossed as shown in known manner so as to dampen
swaying of the tray.
In the embodiment shown in FIGS. 6 to
8, the preprocessing plant, in this
case a calcining plant
100, is at a higher level than the furnace
106,
and the axis of the latter is in line with the processing plant. The tower
2
is replaced by two passages
102 extending to either side of the electrodes
114 of the furnace and above the furnace roof
112. Within each passage
a frame
132 supports a bin
134 for movement along rails
142
in the passage. At any time one or other bin
134 is positioned to receive
calcine through a delivery chute
138 from the calcining plant
100
while the other delivers calcine to a selected funnel assembly
130 which
distributes calcine to the furnace through tubes
120.
The bins
134 in the example shown consist of four compartments in the
form of tubular containers which guides
144 cause to tilt to a vertical
position to place open ends of the tubes beneath the chute
138 so that each
may be wholly or partially filled with calcine. The tubular containers are returned
to a near horizontal position for transit (as seen in FIGS. 6 and 7) before being
tilted open end downwards at a selected funnel assembly
130 by a selectively
engaged tipper mechanism (not shown) so as to discharge their content into funnels
of the assembly which are connected to the tubes
120.
In each embodiment, the tower
2 or passages
102 are enclosed to
exclude the ambient atmosphere, and the atmosphere inside is controlled, both to
avoid release of fumes, and to avoid unwanted reactions with the material being
transported. For example, off-gas from the calcining plant or furnace, or waste
gas from elsewhere in the plant may be admitted, surplus gas being passed to an
appropriate treatment plant. Gas may be admitted at either the top or bottom of
the volume to be filled according to whether it is heavier or lighter than ambient
air such as to displace air from the volume concerned. Alternatively, the volume
may be allowed to fill with gases emitted from the material, suitable treatment
facilities again being provided to handle surplus gas. The tower or passages also
provide an opportunity for dust from the material to settle. A hopper
48
(FIG. 1) or
148 (FIG. 7) provides a means for capturing and removing settled dust.
The embodiments described are exemplary only. In the embodiments described, the
shuttle path is respectively vertical and horizontal. It should be understood that
applications in which the housings (tower or passage) are inclined, either laterally
or longitudinally, so as to have both vertical and horizontal extent are also within
the scope of the invention, with the shuttle(s) for the tray(s) or bin(s) having
suitable guidance to follow the inclined path. Regardless of the arrangement used,
a shuttle mechanism within the housing is used to provide rapid transportation
of material, as it is delivered, to distributed points within the furnace, without
any substantial accumulation of material. Distribution of the material within the
furnace can be controlled by controlling the amount of material discharged into
each compartment within the shuttle tray or bin, while permitting extremely simple
and robust mechanisms to be utilized.
*