U.S. patent number 3,852,168 [Application Number 05/312,950] was granted by the patent office on 1974-12-03 for stratifier with a pneumatic product recirculation.
Invention is credited to Hans Oetiker.
United States Patent |
3,852,168 |
Oetiker |
December 3, 1974 |
STRATIFIER WITH A PNEUMATIC PRODUCT RECIRCULATION
Abstract
A method and apparatus for pneumatically stratifying granular
materials wherein a pneumatic means is provided for recycling a
middlings product to the feed. The middlings are raised
pneumatically and then separated from the gas and subsequently
conveyed by vibration to the feed. Separation of the middlings
product, pneumatic treatment at the inlets and outlets, pulsating
means and reciprocating means are also disclosed.
Inventors: |
Oetiker; Hans (9000 St. Gallen,
CH) |
Family
ID: |
27173862 |
Appl.
No.: |
05/312,950 |
Filed: |
December 7, 1972 |
Related U.S. Patent Documents
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Application
Number |
Filing Date |
Patent Number |
Issue Date |
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12108 |
Feb 17, 1970 |
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Foreign Application Priority Data
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Feb 21, 1969 [CH] |
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2706/69 |
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Current U.S.
Class: |
209/469; 209/488;
209/492; 209/467; 209/504 |
Current CPC
Class: |
B03B
4/005 (20130101); B03B 4/02 (20130101) |
Current International
Class: |
B03B
4/00 (20060101); B03B 4/02 (20060101); B07b
004/08 (); B07b 011/06 () |
Field of
Search: |
;209/466-469,488,492,502,321,474-476,312,318,504 |
References Cited
[Referenced By]
U.S. Patent Documents
Foreign Patent Documents
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23,077 |
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Jun 1935 |
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AU |
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213,076 |
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Jun 1956 |
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AU |
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Primary Examiner: Lutter; Frank W.
Assistant Examiner: Hill; Ralph J.
Attorney, Agent or Firm: McGlew and Tuttle
Parent Case Text
CROSS-REFERENCE TO PARENT
This case is a continuation of Ser. No. 12,108, filed Feb. 17,
1970, now abandoned.
Claims
What is claimed is:
1. In a method for separating bulk material mixtures into separated
fractions, in accordance with the specific gravities of the mixture
components, under the influence of vibrations of a material support
carrying the bulk material in a layer and conveying it from an
inlet to outlets for separated fractions, and under the influence
of aeration by an aeration air current flowing through the material
support and the layer, which aeration air current is collected in a
hodd covering the material support and is exhausted from the hood:
the improvement comprising the steps of providing an additional air
current flowing along a path separate from the path of flow of the
aeration air current flowing through such layer, the path of flow
of such additional air current being completely outside such layer
of bulk material; discharging at least one separated fraction of
the bulk material, leaving its outlet into such additional air
current; thereafter separating the additional air current flow from
such at least one separated fraction; returning such at least one
separated fraction to such layer; and exhausting the aeration air
current from said hood conjointly with exhaustion of the separated
additional air current.
2. A method, as claimed in claim 1, in which the additional air
current flows along a path extending from a point below said
material support to a point above said material support, and
conveys such at least one separated fraction from such point below
said material support to such point above said material support;
said additional air current flow being separated from such at least
one separated fraction at a point above said material support for
flow into said hood.
3. A method, as claimed in claim 2, including the step of conveying
such at least one separated fraction between such point below said
material support and such point of separation of the additional air
current flow from such at least one separated fraction.
4. A method, as claimed in claim 2, including the step of returning
such at least one separated fraction, after separation of the
additional air current flow therefrom, to such layer in the area of
the inlet for the bulk material entering the material support for
merger with such bulk material.
5. A method, as claimed im claim 1, in which said aeration air
current flowing through such layer is periodically interrupted to
provide a pulsating air current.
6. Apparatus for separating bulk material mixtures, in accordance
with the specific gravities of the mixture components, under the
influence of vibrations of a material support carrying the bulk
material in a layer and conveying it from an inlet to outlets, and
under the influence of aeration by an aeration air current flowing
through the material support and the layer, which aeration air
current is collected in a hood covering the material support and
exhausted from the hood, said apparatus comprising, in combination,
a porous and gas-permeable material support having an inlet for
bulk material and outlets for separated fractions; means operable
to feed bulk materials to said inlet; means operable to vibrate
said support; a hood covering said support and connected to air
exhaust means; a first aeration air inlet arranged beneath said
support for flow of the aeration air current for aerating the bulk
material mixture flowing over said material support; an additional
air inlet separated from said first inlet port; a separate flow
duct extending from said additional air inlet port into the range
of said material inlet for the flow of an additional air current
through said additional air inlet port and through said separate
flow duct; means supplying material from at least one outlet to
said separate flow duct for entrainment in said additional air
current, for return through said separate flow duct to said bulk
material inlet; and means in said separate flow duct separating
said additional air current from the material supplied thereto, and
communicating with said exhaust means for conjoint exhaust of the
additional air current with the aeration air current collected
under said hood.
7. Apparatus, as claimed in claim 6, in which said separate flow
duct terminates in such range on said material support covered by
said hood; said at least one of said outlets opening into said
separate flow duct downstream therein from said additional air
inlet port.
8. Apparatus, as claimed in claim 7, including an injector-like
constriction in said separate flow duct between said additional air
inlet port and the opening of said at least one outlet into said
separate flow duct; said separate flow duct, downstream of said
injector-like constriction, increasing in cross sectional flow
area.
9. Apparatus, as claimed in claim 8, including means operable to
adjust the flow area of said constriction.
10. Apparatus, as claimed in claim 7, in which said conveyor line,
intermediate the opening of said at least one outlet thereinto and
the range of said material inlet, is formed with a flow deflecting
portion elevated substantially above said material support; said
conveyor line being formed with an air slot beneath said hood and
between said flow deflecting portion and the range of said material
inlet.
11. Apparatus, as claimed in claim 7, including a partition
positioned between said material inlet and the exit of said
conveyor line to said material support.
12. Apparatus, as claimed in claim 11, in which said partition is
curved in the direction of flow.
13. Apparatus, as claimed in claim 6, in which said separate flow
duct forms a pneumatic conveyor line and is constructed as part of
said hood covering said material support.
14. Apparatus, as claimed in claim 6, including a periodically
operable air current interrupter provided in said aeration air
inlet.
15. Apparatus, as claimed in claim 14, including panels subdividing
said aeration air inlet into plural flow ducts communicating with
said material support; each flow duct having a respective air
supply opening; said periodically operable air current interrupter
controlling flow of aeration air through said air supply openings
and closing said air supply openings at least partially.
16. Apparatus, as claimed in claim 15, in which said periodically
operable air current interrupter comprises a rotating disk having
at least one aperture therethrough and positioned opposite said air
supply openings.
17. Apparatus, as claimed in claim 16, in which said rotatable disk
has a plurality of apertures therethrough.
18. Apparatus, as claimed in claim 16, in which said disk is formed
as a turbine runner having inclined vanes in said apertures serving
to drive said turbine runner by the aeration air flowing through
said apertures and said air supply openings.
19. Apparatus, as claimed in claim 14, in which said air supply
means is vibratable with said material support; a
vibration-generating motor oscillatably mounted on said material
support; eccentric weights rotatable by said motor; a free-wheeling
clutch having a driving member and a driven member; means
connecting said driving member to said motor for driving thereby;
and means connecting said driven member in driving relation with
said periodically operable air current interrupter.
20. Apparatus, as claimed in claim 19, including a first grooved
pulley connected to said driven member; a second grooved pulley
connected to said periodically operable air current interrupter; an
endless drive means interconnecting said grooved pulleys; said
pulleys having plural grooves of respective different diameters for
adjustment of the transmission ratio between said free-wheeling
clutch and said periodically operable air current interrupter.
21. Apparatus, as claimed in claim 19, in which said means
connecting said motor to said clutch driving member comprises a
link articulated at one end to said clutch driving member and
articulated at the opposite end to said motor.
22. Apparatus, as claimed in claim 6, including a plurality of
individually adjustable baffle plates each in the transition zone
from said material support to a respective one of said outlets; and
common adjusting means connected to all of said baffle plates for
conjoint adjustment of the latter.
23. Apparatus, as claimed in claim 22, including a respective
adjusting shaft secured to each baffle plate; and a respective
adjusting plate adjustably secured to each adjusting shaft; said
common adjusting means comprising a movable linkage articulated to
all of said adjusting plates.
24. Apparatus, as claimed in claim 23, including spring means
maintaining each adjusting plate in adjusted position on its
associated adjusting shaft.
Description
BACKGROUND OF THE INVENTION
In this type of material treatment, which is known also as "light
grain-sorting," and involving the combined use of vibration and
fluidization, equivalent to aeration by an air current, it is known
to subject a second fraction, of partial fractions obtained
separately from the repeated material treatments, by returning it
to the incoming bulk material, together with the latter, to a
second treatment in order to improve the degree of sorting or
separation. Such recirculation frequently proves absolutely
necessary, since a clean separation, into the various components of
the bulk material mixture, cannot be effected completely, with
economically acceptable equipment expenditures, without an
excessive stay or dwell period of the bulk material in the range of
action of the treatments effecting the separation, that is,
vibration and fluidization or pneumatic aeration.
In known arrangements, this return of material into the total
material flow is effected by mechanical conveyor elements, such as
bucket conveyors, returning material to the total material input
through the material inlet to the material support. Thus, the
recirculating arrangements necessitate the provision of a special
driving means and at least one gate, if the separation of the bulk
material mixture takes place in a closed chamber collecting the
aeration air in a pipe leading from the chamber, and this also
involves considerable increase in operating expenses. For example,
increased expenses are involved in the additional driving means and
in the elastic or flexible connections.
SUMMARY OF THE INVENTION
This invention is directed to the separation of components of
mixtures of bulk materials utilizing vibration and fluidization
and, more particularly, to a novel, improved, simpler and more
efficient method and apparatus for effecting such separation with a
higher degree of efficiency.
In accordance with the invention, it has been found, surprisingly,
that, in addition to the air current necessary for aeration and
flowing through the material support and the layer, with subsequent
collection under a hood and exhaust from the hood, separately
supplied and conducted treatment air can be fed into the exhaust
air current. Thus, in accordance with the invention, at least one
treatment air flow is provided and conducted separately from the
air current flowing through the layer on the support, and utilized
to effect separate treatments of the bulk material, fed through the
inlet, or parts of the bulk material, and the aeration air current
and the treatment air current are conjointly exhausted after the
aeration treatment and the special treatment.
In addition to the separation of bulk material mixtures, according
to specific gravities, under the influence of vibrations and
aeration, it is known to effect a so-called inlet aspiration of the
incoming bulk material, that is, to direct the air current,
necessary for the aeration, in the range of the inlet across the
incoming bulk mixture and thus to separate the light fractions.
However, this stepwise use of the aerating air for a second purpose
has the disadvantage that light portions of the bulk mixture, which
were removed on the vibrating material support by the air current,
are deposited again at least partly in the bulk material during the
sifting in the inlet. This is usually connected with a constant
circulation of certain bulk material components, which leads to a
reduction of the effectiveness of the separating method, after
which light portions, under the influence of heavier portions, are
discharged with the latter from the apparatus. Variations of the
air current manifest themselves immediately as variations in the
inlet sifting, because of the varying layer thickness of the bulk
material.
An advantage of using a separate air current for aeration of the
bulk material on the vibrating support and another special
treatment air current for separate treatment of the bulk material
from the separation operation, or apart of the bulk material,
resides in the fact that optimum air flow conditions must be
created for these separate treatments, and this leads to a
substantial improvement in efficiency of the operation. In
addition, these measures permit the simplified performance of
treatments which could be carried out heretofore only at much
greater expense. Thus, mixture components which must be fed a
second time, under the influence of vibration and aeration, to the
material support, can be returned again to the range of the inlet
utilizing the separated air current as a pneumatic conveyor.
In addition, certain light fractions of the bulk mixture can be
removed by air sifting, by causing the separately conducted
treatment air to flow through the inlet in such a way that neither
contaminated air nor air moistened by a previous treatment or
influenced by working variations in the current, are used.
Additionally, the mixture components issuing through an outlet can
be exhausted by air sifting between this outlet and the joint
exhaust of the aeration air current and the treatment air current
in the outlet. Despite the separate flow of air, the treatment air,
for a separate treatment, the air current passing through the
material support, and the layer of material on the support can be
pulsated by periodic interruption of the main air aeration air
flow.
The invention apparatus includes a main air inlet or air feeding
device beneath a porous and gas-permeable material support, for the
air current for aerating the bulk material mixture flowing over
this support, and includes a separate air inlet opening connected
to a special flow duct for the flow of the treatment air current
which is conducted to a treatment apparatus separate from the
aeration arrangement. Means are provided for commonly or conjointly
exhausting the treatment air current and the aeration air current,
collected under a hood covering the material support, after the
aeration treatment and the separate treatment.
In concordance with the invention method, it is essential that, in
the invention apparatus, the individual air currents for the two
separate treatments of the material are fed separately to the
treatment stations in the apparatus.
A flow duct can be arranged adjoining the air inlet for the
treatment air, for the pneumatic feed from the range of at least
one of the outlets up to the range of the bulk material inlet.
An air passage can be provided, under the hood covering the
material support, for the treatment air providing the pneumatic
feed, and this air passage can be provided between the mouth of a
feed pipe in the range of the material inlet and a deflection
arranged at a higher level opposite this mouth.
The treatment air can be fed from the treatment air inlet through a
falling bulk mixture mist in the range of the material inlet and
into the air current under the hood.
Additionally, an air sifting duct can be formed between the inlet
for the treatment air and the common exhaust, into which one of the
outlets opens above the inlet.
A periodically operating air current interrupter can be provided in
the main air supply to the material support.
The application of the aforementioned measures individually or in
combination offers the advantages of a very economical operation of
the overall apparatus, a very efficient separating effect on the
bulk mixture supply, and substantial savings in equipment
costs.
An object of the invention is to provide an improved method of and
apparatus for separating mixtures of bulk materials, according to
specific gravity, under the influence of vibration and
aeration.
Another object of the invention is to provide such a method and
apparatus in which a separate treatment air current flow is
provided and at least part of the bulk material is subjected to a
separate treatment by the treatment air current.
A further object of the invention is to provide such a method and
apparatus in which, after aeration and such separate treatment, the
aeration air current and the treatment air current are commonly
exhausted.
Another object of the invention is to provide such a method and
apparatus in which treatment air flow is pulsating.
A further object of the invention is to provide such a method and
apparatus characterized by simplicity, economy and increased
efficiency.
For an understanding of the principles of the invention, reference
is made to the following description of typical embodiments thereof
as illustrated in the accompanying drawings.
BRIEF DESCRIPTION OF THE DRAWINGS
In the Drawings:
FIG. 1 is an elevation view, looking in the direction of arrow I of
FIG. 2, of one form of apparatus for performing the method of the
invention;
FIG. 2 is an elevation view of the apparatus looking in the
direction of the arrow II of FIG. 1;
FIG. 3 is a vertical sectional view of the apparatus taken on the
line III--III of FIG. 2;
FIG. 4 is an elevation view, partly in section, illustrating
details of a modified form of the apparatus;
FIG. 5 is a partial bottom plan view illustrating a further
modification of the apparatus; and
FIG. 6 is a partial vertical sectional view, to a much larger
scale, illustrating a further modification of the apparatus of the
invention.
DESCRIPTION OF THE PREFERRED EMBODIMENTS
Referring to FIGS. 1, 2 and 3, the apparatus of the invention
comprises a material support 1 which is porous and gas-permeable,
and thus also permable to air. The apparatus further includes a
hood 2 arranged above support 1 and an air supply device or main
air inlet 3 arranged beneath the gas-permeable support. Hood 2
opens into a line 5 connected by an elastic bellows 6 with an air
exhaust pipe 7. Hood 2 also encloses several outlets 11, 12, 13 and
14 which are arranged laterally about gas-permeable material
support 1. An inlet 20, for feeding of bulk material, discharges
onto material support 1, and this inlet 20 is connected by a
bellows 21 with a material feed pipe 22. Inlet 20 opens on to
material support 1 in the same plane as the supporting surface of
the support 1, and has pivotally mounted therein a feed regulating
flap or damper provided with a counterweight 26.
The air feeding device or main inlet arranged beneath material
support 1 acts simultaneously as a partial distributing device for
the air current, since its entire base area is subdivided by
partitions 31 and 32 into separate air flow passages. Each air flow
passage, at the lowest point of the apparatus, has a respective air
supply opening 35 for supply of air thereto. Above each air supply
opening 35, there is arranged an adjustable flap or partition 36
having openings 37 which permit individual regulation of the
effective cross section of each air supply opening 35. A moving
shut-off valve 40 is arranged on the inlet side of the air supply
openings and, in the embodiment of the invention shown in FIGS. 1,
2 and 3, comprises a rotating disk 41 having s number of passages
42 greater than the number of air supply openings 35. For the
purpose of effecting rotation of disk 41, as a moving shut-off
element relative to air supply openings 35, disk 41 has, in the
range of the passages 35, inclined vanes 43 oriented in such a
manner that a rotary movement is imparted to the treatment air
acting on the bulk material to be treated, so that disk 41 is
driven in the manner of a turbine runner.
Material support 1 comprises a porous mat 16, a perforated plate 17
and spacers 18. For the purpose of influencing the discharge of
bulk material treated on the porous and gas-permeable material
support 1, adjustable baffle plates 45 are provided along one side
thereof, and define between themselves adjustable discharge gaps
46. Distribution flaps are arranged along the other side of
material support 1 in such a manner that the push-off-bulk
material, from various outlet regions of the porous and
gas-permeable material support 1, can be fed without change in
quantity, to the various outlets 11-14.
In addition to the treatment effected by the air drawn through the
entire apparatus from main air inlet or air feeding device 3 to the
hood 2 and into line 5, means are provided for effecting a
vibration treatment. For this purpose, a shaft 51 is positioned in
apertures in two pairs of side bars 50 on an assembly consisting of
material support 1, hood 2 and air feeding device 3. This assembly
is mounted for vibration and oscillation by springs 52 in
oppositely directed sockets 55 and 56, and a hinged support
generally indicated at 58. The support by springs 52 in the two
sockets 55 and 56 can be adjusted by the clamping rocker 60, the
two springs 52 being arranged obliquely to each other between the
sockets 55 and 56 and the bearings 61 and 62 on shaft 51.
Proceeding from base 10 to the vibratable assembly, hinged support
58 comprises a bearing block 65, a substantially horizontal lateral
plate 66, a substantially vertical link 67, and a bearing head 68
engaging a pivot pin 69 on the assembly. Respective hinge pins 70
interconnect bearing block 65 to lateral plate 66, lateral plate 66
to link 67 and link 67 to bearing head 68.
The throw vibration movement is produced by a motor 80 provided
with eccentric weight 81 and 82, this motor being oscillatably
mounted, in a known manner, by elastic oscillation blocks, on shaft
51. Clamping rocker 60 is secured on a shaft 85 mounted in base 10,
and can be clamped to socket 10 by a nut 86 threaded on shaft
85.
Elastic shut-off elements 90, for example rubber plates, are
associated with the various outlets 11, 13 and 14 in such a manner
that the shut-off elements are pressed against the peripheries of
the outlet openings by the pressure gradient existing between the
outer atmosphere and the interiors of the respective outlet
openings.
Outlet 12 is provided with an outlet pipe 91 which communicates
with a flow duct 92 designed as a conveyor line. Flow duct 92 is
formed by an air inlet opening 94, arranged below the exit 93 of
pipe 91 connected to outlet 12, an injector-like constriction 95, a
diverging rising duct 96, and a trough 97 sloping downwardly to the
range of material inlet 20 from a deflection section 98 arranged in
elevated relation to mouth 93, of outlet 12, and the transfer level
from inlet 20 to material support 1. Constriction 95 is variable in
cross section by a screw 101 acting on a movable plate 100. In the
range of trough 97 between deflection portion 98 and the range of
material inlet 20, there is provided an air slot 102 opening under
hood 20. In the range of material inlet 20, flow duct 92, designed
as a conveyor line, opens to the porous, gas-permeable support 1.
Between material inlet 20 and the mouth 104 of this conveyor line
there is arranged a partition 105, preferably curved in the
direction of flow.
At least one sight glass 110 is provided in hood 2 for observing
the work on the material on support 1.
The apparatus shown in FIGS. 1, 2 and 3 is operable to perform the
method which will now be described. A bulk material mixture, to be
subjected to a separation treatment in accordance with the specific
gravities of its components, is supplied through material inlet 20
to porous, gas-permeable material support 1, with the feed being
regulated, by the counterweight-loaded flap 25, in such a manner
that no excess secondary air is introduced into the apparatus from
feed pipe 22. The separation of the bulk material mixture is
effected by subjecting the mixture to the influence of vibrations
of material support 1, which latter effects, at the same time,
feeding of the material from inlet 20 to the outlets. In the
illustrated apparatus, these vibrations, which are throw
vibrations, are imparted to support 1 by motor 80, mounted for
oscillation on the construction, and having the imbalance-producing
eccentric weights 81 and 82. The conveying effect of the vibrations
imparted to material support 1 can be influenced by the dual
inclination adjustment means. One means is represented with the
rocker and the pivot pin with respect to one machine shaft, but, in
the other means, and in contrast with the illustration, the hinged
support must be adjustable. In addition to the influence of the
vibrations in separating the bulk material mixture on material
support 1, the bulk material is subjected to the influence of an
air current drawn through material support 1 and effecting aeration
of the bulk material through which the air current flows. The
fractions of the charged bulk material mixture, separated according
to the specific gravities of the components, are discharged through
outlets provided for this purpose.
In the application of this method of separating bulk material
mixtures under the influence of an air current flowing through
material support 1 and the layer of material thereon, it has been
found, in accordance with the invention, that separate treatments
of the bulk material supplied through the inlet, or parts of the
bulk material so supplied, can be effected in the same apparatus.
For these separate treatments, there is used a treatment air flow
which is sparate from the air current flow required for the
aeration, and which is exhausted, after the treatment, conjointly
or commonly with the aeration air current.
In the apparatus illustrated in FIGS. 1, 2 and 3, separate
treatment of a part or all of the bulk material is effected by at
least partly pneumatic conveyance of mixture components, which are
separated from the bulk material mixture and flow into an outlet
especially provided for this purpose. From the range of this
outlet, the pneumatic conveyance of the mixture components is
effected as a separate treatment directing the components thus
treated back into the range of the inlet provided for the inflowing
bulk material mixture.
In contrast to presently known so-called recirculations or returns
of parts of the bulk material, using special conveyor devices
provided between respective outlets and the inlet, the discovery of
the present invention has proved to result in a substantial
simplification with respect to these known procedures. The
discovery of the present invention resides in that the energy
imparters, namely the air and vibration, used for separation of the
bulk material mixture, are used simultaneously for a separate
treatment. In the above-mentioned pneumatic return of the separated
layer, conveyance of the separated layer is effected, after
elevated deflection, primarily by the vibration produced, and the
conveyance leads up to the range of the inlet for the bulk material
mixture. It is thereby possible to conduct the specially guided
treatment air, before the returned mixture components are
transferred to the material support, from the flow duct beneath the
hood and to exhaust the treatment air from the hood together with
the aeration air, and through the exhaust air line.
In order to improve the effectiveness of the separation utilizing
vibration and air flow, the air flow through the material support
and the layer thereon is interrupted periodically, so that, in
effect, the main or aeration air flow is a pulsating air current.
Simultaneously, the separately conducted treatment air can have a
continuous flow, which is necessary particularly in pneumatic
conveyance.
Due to the injector-like design of the flow duct 92, for the
treatment air, and which extends from the exit of one outlet, there
is obtained the necessary pressure difference within the system.
Without this particular provision, it would not be possible readily
to obtain this flow. With this provision, however, a suitable
pressure-velocity conversion is attained, and vice-versa. The
number of openings in the rotating air flow interrupter 41,
designed as a turbine runner, preferably differs from the number of
air supply openings to the gas-permeable material support.
In the illustrated apparatus for carrying out the above described
method, there is obtained an economical operation, and substantial
savings in special apparatus for the return feed of that part of
the bulk material subjected again to the influence of vibration and
aeration. Any very light dust fractions still deposited from the
treatment are conducted, in exactly the same apparatus, into the
air current already laden from the aeration with the very light
particles, so that, in this respect also, an improved operation of
separating means is attained.
This improved dust removal, with respect to that part of the bulk
material returned again for separation, is based on the fact that
the dust particles, during the high level or elevated deflection,
are no longer precipitated from the separately conducted treatment
air through air slot 102 beneath hood 2. Another improvement
consists in that the returned part of the bulk material is fed to
the incoming bulk material mixture in the range of the inlet and in
the lateral region which is particularly preferable for the
subsequent separation. By virtue of this, a final sharp separation
of the returned partial amount of the material is substantially
facilitated during the second passage through the apparatus. The
overall efficiency thereby is substantially improved, as compared
to presently known arrangements for returning mixtures to newly
incoming bulk material mixtures.
It will be clear that the bulk material mixtures, fed through inlet
20, can be subjected to air sifting in the region of this inlet in
a similar manner, by using a separately conducted treatment air
current, also combined with the aeration air current, which thus
effects an initial relief, from the bulk material mixture, of the
lightest fractions, such as husks, dust, etc. This insures, in the
further separation on the porous, and gas permeable material
support 1, an effective operation, since these fractions will not
be able to clog the relatively small openings provided in material
support 1.
The embodiment of the invention shown in FIG. 4 represents an
apparatus for carrying out another method for separating bulk
material mixtures, and represents a further simplification with
respect to the already described apparatus as well as providing
very great savings in additional equipment.
In the case of certain products, it is desirable to obtain
individual light fractions, which are subdivided again into two
partial fractions. In corn, this is the separation between the
kernels and the husk parts, and this separation is desirable
because the kernels have a very useful high fat content. In order
to effect such a separation, it has been known to eliminate the
light parts and to withdraw them subsequently in a special
separation operation. In the first stage separation of bulk
material mixtures according to the specific gravities of the
mixture components, utilizing vibration and aeration, as already
known, it has been found additionally that, following the initial
separation and by the separate guiding of a special treatment air
flow, a second separation is possible in a very simple manner. This
involves conducting the product, discharged through an outlet, into
a rising air sifting duct, forming part of the apparatus, and in
which the very light husk parts and the somewhat heavier kernels
can be separated by air sifting. The treatment air current required
for this air sifting is directed through this duct and is
discharged into the aeration air current separately directed
through the porous material support. Both the treatment air current
and the main or aeration air current are conjointly exhausted.
The basic apparatus corresponds to that shown in FIGS. 1, 2 and 3,
already described, but the pneumatic return through flow duct 92
from outlet 12 and into the range of material inlet 20 is omitted
and is replaced by an auxiliary device 120. Auxiliary device 120
has a rising duct 122, a very simple material separator 124, a
treatment air line 125 and a fines exit gate 126. Rising treatment
air duct 122 is provided with an adjustable plate 128 with
adjustment thereof being effected by two hand wheel operated screws
130. On the opposite side from adjustable plate 128, there is
arranged the feed 132 from outlet 11. Beneath feed 132, there is
provided a treatment air inlet port 135 whose flow area can be
adjusted by a slide valve 133. Duct 122 is closed at its bottom end
by an elastic terminal gate 138.
A throttle valve, or damper, 141 is arranged in air exhaust pipe 7,
and can be adjusted by a hand wheel 140. Treatment air line 125
terminates above or downstream of throttle valve or damper 141, and
communicates with an aperture 142 in exhaust pipe 7, so that both
the main aeration air current and the treatment air current are
combined for conjoint exhaust only downstream of throttle valve or
damper 141.
The apparatus illustrated in FIG. 4 provides for carrying out a
treatment of the bulk material which will now be described. The
bulk material mixture flows from feed pipe 22 through inlet 20 onto
the porous, gas-permeable material support 1, which is vibrated, in
a throw vibration movement, by motor 80 carrying eccentric weights
81 and 82. Due to this throw vibration, on the one hand, and the
air current drawn through material support 1, on the other hand,
and which air current is transformed, by the moving air current
interrupter 40 into a pulsating current, the bulk material mixture
is separated according to the specific gravity of its components
and the separated components are conveyed to the various outlets 11
through 14. While the mixture components, separated according to
their respective specific gravities under the action of vibration
and air flow, issue individually through respective outlets 12, 13,
or 14, the lightest fraction, collected in outlet 11, is conducted
through the adjoining feed 132 into duct 122. By virtue of the
vibration effective on outlet 11 and on duct 122, transfer of this
lightest fraction takes place over the projecting edge 132a of feed
132, as a uniform mist. The treatment air for air sifting this
material fraction enters through treatment air inlet port 135 into
duct 122, is conducted upwardly into material separator 124, and
flows through treatment air line 125 into air exhaust pipe 7.
The air sifting of this fraction is effected, on the one hand, by
varying the flow area of treatment air inlet port 135, using slide
valve 133, and, on the other hand, by shifting or adjusting movable
plate 138 utilizing hand screws 130. This shifting or adjustment of
plate 128 results in an adjustment of the cross section of the
duct, and also results in an adjustment of the flow velocity of the
treatment air current. In the case of corn, for example, the very
light husk parts are carried by this air sifting with the rising
treatment current into the material separator 124, where they are
removed from the air current and conducted to the fines discharge
gate 138. The latter closes and opens, respectively, in a gradual
manner, in dependence on the amount of material contained therein,
the gate opening against the elastic closing force and the
additional pneumatic closing force resulting from the pressure
difference between the ambient atmosphere and the interior of duct
122.
Despite the pulsating flow of the air current through the material
support 1, there are practically constant flow conditions in duct
122, from treatment air inlet port 135 to aperture 142 in air
exhaust pipe 7, and such conditions are necessary, to a great
extent, for air sifting. By virtue of this design, it is possible
to utilize the suction power, necessary to produce the air current
for aerating the bulk material to be separated by vibration and
aeration, in the same flow system, to provide an at least partly
separately directed current of treatment air for the separate
treatment of the same bulk material. This results in savings both
in energy and equipment, in carrying out bulk material treatments.
A further effect in contrast to known methods and apparatus, is
that the individual separate bulk materials are present in the
desired form for the further treatment.
While, in the two embodiments shown in FIGS. 1, 2 and 3 and in FIG.
4, respectively, the drive of the shut-off element interrupting the
air flow, and including the disk 41 formed with the passages 42 and
the vanes 43 extending into the flow area of these passages, is
effected in the manner of a turbine wheel, FIG. 5 illustrates
another type of drive for the flow interrupting element and which
uses the vibration generator as the driving means. It has been
found that the interesting principle of a turbine wheel for this
drive has the disadvantage of not providing an absolutely constant
speed of the interrupter disk, and thus an absolutely constant
frequency of interruption of the air current. While it would be
possible to provide a separate driving motor for the flow
interruption element, this has the disadvantage that the expense is
high and, in addition, such a motor would be subjected, unless
special measures were provided, to the constant vibration of the
vibratable assembly. The arrangement illustrated in FIG. 5 obviates
this disadvantage and uses the available energy of the freely
swinging motor 80 for driving the shut-off element interrupting the
air current flowing through the material support 1.
Referring to FIG. 5, the moving shut-off element 40' of the air
supply device 3', having air supply openings 35', is designed as a
rotating disk 41' with passages 42'. The number of passages 42'
preferably is greater than the number of air passages 35', and, in
the particular embodiment illustrated in FIG. 5, the ratio is 5:4.
A stepped disk 151 is secured to rotate with the disk 41', and has
the different diameters for receiving an endless driving element,
such as an endless driving cord 152.
Motor 80, provided with the eccentric weights 81 and 82, is mounted
on a bearing plate 83' for swinging or oscillation through the
medium of elastic swinging supports 153 whose outer casing members
are fixedly connected with bearing plate 83', and with which is
associated a bolt 154 fixed relative to shaft 51. The particularly
designed bearing plate 83' is formed with an elongated rectilinear
slot 155.
A double-action freewheeling clutch 160 is also fixedly connected
with shaft 51 by clamping studs 157 and a clamping yoke 158. A stub
shaft 161 on the driving side of clutch 160 has connected thereto a
plate 162 which is articulated, through the medium of a bolt 163,
to a push rod or link 165 having a length sufficient to extend into
the area of bearing plate 83' and particularly slot 155 therein.
Within the area of bearing plate 83', link or pushrod 165 is
adjustably articulated to bearing plate 83' through a connection
168. A stub shaft 166 on the driven side of freewheeling clutch 160
carries a stepped wheel 167 having a groove receiving driving cord
152.
Since it is characteristic of a free swinging drive of this type,
which acts on material support 1 and also on hood 2 and air supply
device 3, that motor 80, due to the eccentric weights 81 and 82,
can perform a circular movement insofar as the bearing resistance
will permit, there results a linear vibration, for the overall
arrangement, perpendicular to shaft 51. The latter deviates only
slightly from its rectilinearity. On the other hand, motor 80, with
bearing plate 83' mounted on elastic swinging mounts 153, can
perform an elastic swinging displacement or oscillation movement
substantially parallel to shaft 51, about the axis of bolt 154.
Depending on the selected inclination of the axis of the rotor of
motor 80, the linear vibration, acting correspondingly on material
support 1, effects a throwing movement of bulk material on this
support 1. Due to the eccentric articulated securing of pushrod 165
to bearing plate 83', this link moves relatively to shaft 51 on
which double-action freewheeling clutch 160 is clamped. Stub shaft
161 on the driving side of clutch 160 and connected to plate 162 is
thus oscillated. Due to double-action clutch 160, this oscillating
movement is transformed into a stepwise angular movement resulting
in rotation, in one direction, of stub shaft 166 on the driven side
of clutch 160. Thus, stepped wheel 167 is stepped by successive
angular steps corresponding to the oscillation frequency of plate
162, and which is a function of the normal distance of link 165
from bolt 154 forming the axis of rotation of the elastic swinging
block 153. The effect is a quasi-continuous rotation of disk 41' in
strict proportionality to the oscillating frequency of the
swingable assembly and of the motor 80 which produces the
oscillation. This oscillating frequency can be adjusted, in
addition, by adjusting the connection of push rod or link 165 along
slot 155, or by varying the transmission ratio, expressed in
rotations per unit of time, between stepped wheel 167 and stepped
disk 151. This adjustability also adjusts the interruption
frequency of the air current through material support 1. The
auxiliary device is very simple in its construction and assembly
and requires practically no maintenance and no driving element with
a special power source, and furthermore permits, in a very simple
manner, adjustment of the frequency of interruption of the air
current flow through the material support.
Even during operation of material separating apparatus,
occasionally it is necessary to adjust individually the outlet
flaps which are usually provided at outlets in the range of the
push-off of bulk material from the material support. These
adjustments are sometimes necessary to prevent a too vigorous
overshooting, which would influence the separation operation.
Additionally, it has long been desirable to shift an individual
adjustment, after it has initially been set, conjointly with other
adjustments, under certain operating conditions, while maintaining
the individual adjustment. An arrangement for effecting such
combined adjustment is illustrated in FIG. 6.
Referring to FIG. 6, material support 1 which comprises
porous-gas-permeable plate 16, perforated plate 17 and spacers 18,
is provided, beneath hood 2 and along 1 lateral edge 170 toward
outlet 14, with bearing sleeves 171. Sleeves 171 serve to receive
shifting shafts 172 having a single head 173 at one end, with each
head 173 being connected to a respective baffle plate 45. Shafts
172 extend through the entire material support 1 and each shaft
has, at its other end, an external thread 174 receiving a net 184.
Between nut 184 and perforated plate 17 of support 1 there are
arranged cup springs 176, an operating plate 185, another cup
spring 177, and a spiral or helical compression spring 180, a
washer 181 being interposed between spring 180 and perforated plate
17. Each operating plate 185 on a respective bolt 172 has its free
end formed with a slot 186. A movable linkage mounted on the
machine, and extending over the entire length of the machine or at
least through the distance between the extreme baffle plates 45, is
provided, in the range of each slot 186 with a bolt 189 at least
partially embraced by this slot.
Nut 184 is tightened on thread 174 so that operating plate 185 is
so gripped, between the pack of cup springs 176 and the combination
of cup spring 177 with compression spring 177, that it can be
displaced relative to the cup springs 176 and 177 only by expending
a pretermined force. It is thus possible, after removing the
elastic closing cover 190 in outlet 14, to adjust a baffle plate 45
individually by loosening nut 174 and effecting a relative angular
displacement between bolt 172 and plate 185, after which nut 184 is
retightened. On the other hand, by displacing the linkage 188,
adjusting shaft 173, and thus the associated baffle plate 145, are
turned due to the gripping action between cup springs 176, 177 and
operating plate 185. The arrangement of FIG. 6 thus provides a
solution for the problem of providing both individual and conjoint
adjustment of individually adjustable baffle plates 45.
It will be clear that special details of the apparatus can be
designed differently than as illustrated in the drawings, and this
applies particularly with respect to the external design of the
apparatus, the means for producing the vibrations, the vibratable
support, the air supply and distribution, the collection of the
bulk material and the conveyance of the material.
While specific embodiments of the invention have been shown and
described in detail to illustrate the application of the principles
of the invention, it will be understood that the invention may be
embodied otherwise without departing from such principles.
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