U.S. patent number 3,892,706 [Application Number 05/279,171] was granted by the patent office on 1975-07-01 for method of processing refuse for conversion into shaped bodies.
This patent grant is currently assigned to Jetzer Engineering AG. Invention is credited to Raimund Jetzer.
United States Patent |
3,892,706 |
Jetzer |
July 1, 1975 |
Method of processing refuse for conversion into shaped bodies
Abstract
Household, agricultural and forestry refuse is processed by
subjecting it to aerobic decomposition in order to liberate its
fiber content, whereupon the resulting product is sterilized, has
its moisture content adjusted to a predetermined range and is
converted into a mass of substantially dry, heterogeneous
fiber-containing matter. This mass is then segregated into a
plurality of different-size fractions with the coarsest fractions
being separated from the remaining fractions which are admixed with
a binder and shaped and hardened.
Inventors: |
Jetzer; Raimund (Nussbaumen,
CH) |
Assignee: |
Jetzer Engineering AG (Vaduz,
FL)
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Family
ID: |
27428293 |
Appl.
No.: |
05/279,171 |
Filed: |
August 9, 1972 |
Related U.S. Patent Documents
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Application
Number |
Filing Date |
Patent Number |
Issue Date |
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7996 |
Feb 2, 1970 |
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Foreign Application Priority Data
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Feb 6, 1969 [CH] |
|
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1803/69 |
Jun 12, 1972 [CH] |
|
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8749/72 |
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Current U.S.
Class: |
523/129; 106/697;
428/2; 524/10; 241/DIG.38; 524/9; 106/164.01 |
Current CPC
Class: |
E04C
2/16 (20130101); B03B 9/06 (20130101); C08L
99/00 (20130101); C08K 11/00 (20130101); C04B
18/30 (20130101); C08L 61/20 (20130101); C08L
97/02 (20130101); C08L 61/20 (20130101); C08L
2666/26 (20130101); C08L 97/02 (20130101); C08L
2666/02 (20130101); Y02W 30/91 (20150501); Y10S
241/38 (20130101) |
Current International
Class: |
C04B
18/04 (20060101); C04B 18/30 (20060101); B03B
9/00 (20060101); B03B 9/06 (20060101); C08K
11/00 (20060101); E04C 2/10 (20060101); E04C
2/16 (20060101); C08L 61/00 (20060101); C08L
61/20 (20060101); C08L 97/02 (20060101); C08L
97/00 (20060101); C08L 99/00 (20060101); C08g
051/04 () |
Field of
Search: |
;106/163,90 ;264/331
;260/37R,39R,15,14,9 |
References Cited
[Referenced By]
U.S. Patent Documents
Primary Examiner: Czaja; Donald E.
Assistant Examiner: Person; S. M.
Attorney, Agent or Firm: Striker; Michael S.
Parent Case Text
CROSS REFERENCE TO RELATED APPLICATION
The present application is a continuation-in-part of my copending
application, Ser. No. 7,996 filed on Feb. 2, 1970, and now
abandoned.
Claims
What is claimed as new and desired to be protected by Letters
Patent is set forth in the appended claims:
1. A method of processing refuse for conversion into shaped bodies,
comprising the steps of subjecting a quantity of refuse containing
liquid and solid constituents to aerobic decomposition so as to
liberate the fiber content of said refuse; treating the resulting
product to sterilize said product, adjust the moisture content of
said product to within a predetermined range and convert said
product into a mass of substantially dry heterogeneous
fiber-containing matter; segregating said mass into a plurality of
fractions including one fraction containing the matter of largest
particle size, the remainder of said fractions containing the
matter of smaller particle size and including a fibrous component
and another component; separating said fibrous component from said
other component; and converting said fibrous component into at
least one shaped body.
2. A method as defined in claim 1, said remainder including at
least two fractions; and wherein the step of separating said
fibrous component from said other component is performed
individually for each of the fractions of said remainder.
3. A method as defined in claim 1; and further comprising the step
of isolating said one fraction from said remainder.
4. A method as defined in claim 1, wherein said other component
comprises particles of higher specific gravity than said fibrous
component.
5. A method as defined in claim 2, said other component including
particles of higher specific gravity than said fibrous component;
and wherein the step of separating said fibrous component from said
other component comprises entraining the respective fractions
separately with a flowing medium and conveying the entrained
fractions vertically from a lower level to a higher level; and
regulating the flow speed of said medium to be greater than the
floating speed of the fibrous component of the respective fraction
but less than the descending speed of the particles of the
respective fraction.
6. A method as defined in claim 1, wherein the step of segregating
comprises separating said mass into at least four of said
fractions.
7. A method as defined in claim 1, further comprising the steps of
subjecting said one fraction to mechanical particle-size reduction;
and returning the thus reduced one fraction to the third-mentioned
step.
8. A method as defined in claim 1; and further comprising the step
of subjecting said mass to gravity-segregation for removal of
particles of high specific gravity, prior to the step of
segregating said mass into fractions.
9. A method as defined in claim 1, wherein the step of segregating
comprises screening said mass.
10. A method as defined to claim 5, said fractions including a
finest fraction; and wherein the medium for entraining said finest
fraction is water, and the medium for entraining the other
fractions is air.
11. A method as defined in claim 10; and further comprising the
steps of recovering said finest fraction from the water, and drying
the recovered finest fraction.
12. A method as defined in claim 1, wherein the step of segregating
said mass comprises admitting said mass onto a series of
superimposed screens with the mesh of each subjacent screen being
smaller than that of the superimposed screen.
13. A method as defined in claim 12, said other component including
particles of higher specific gravity than said fibrous component;
and wherein the step of separating said fibrous component from said
other component comprises passing a stream of air from below
through said series of screens for entraining the finest one of
said fractions, the flow speed of the air being selected to be
greater than the floating speed of the fibrous component of said
finest fraction but less than the descending speed of the particles
of said finest fraction; and passing the air stream with the
entrained fibrous component of said finest fraction into a
cyclone.
14. A method as defined in claim 12, said other component including
particles of higher specific gravity than said fibrous component;
and wherein the step of separating said fibrous component from said
other component comprises conveying a respective fraction
separately in a vertical stream of flowing medium from a lower to a
higher level; and regulating the flow speed of said medium to be
greater than the floating speed of the fibrous component of the
respective fraction but less than that of the particles of the
respective fraction.
15. A method as defined in claim 14, said fractions including a
finest fraction; and wherein said medium is water for said finest
fraction, and air for the other fractions.
16. A method as defined in claim 15; further comprising the steps
of separating said finest fraction from the water, drying the thus
separated finest fraction, and returning the dried finest fraction
to the third-mentioned step.
17. A method as defined in claim 1, wherein the step of converting
said fibrous component comprises admixing the same with a binder
material, and press-shaping the thus obtained substance to form
shaped bodies therefrom.
18. A method as defined in claim 17, wherein said binder is a
durable synthetic plastic.
19. A method as defined in claim 17, wherein said binder is a
thermoplastic synthetic material.
20. A method as defined in claim 17, wherein said binder is a
mineral binder.
21. A method as defined in claim 17, wherein the step of
press-forming is carried out in a flat press.
22. A method as defined in claim 17, wherein the step of
press-forming is carried out in an extrusion press.
23. A method of processing refuse and converting it into shaped
bodies, comprising the steps of subjecting a quantity of refuse
composed of liquid and solid constituents to aerobic decomposition
so as to liberate its fiber content; treating the resulting product
to sterilize it, adjust its moisture content to at most 10%, and
convert it into a substantially dry fibrous mass having a
substantial fiber content; admixing said mass with a hardenable
binder material; shaping the resulting mixture under pressure so as
to compress and form it into a shaped body; and effecting hardening
of said binder material to thereby convert said body into a rigid
structural element.
24. A method as defined in claim 23, wherein the adjustment of the
moisture content comprises adjusting said moisture content to be
less than 10%; and wherein said binder material is a synthetic
resin.
25. A method as defined in claim 23, wherein said binder material
is a synthetic resin material.
26. A method as defined in claim 23, wherein the step of treating
said product comprises heating the same to a temperature not
substantially lower than 80.degree.C.
27. A method as defined in claim 23, wherein the step of effecting
hardening of said binder material comprises subjecting said body to
heat.
28. A method as defined in claim 23, wherein said binder material
is an organic binder material.
29. A method as defined in claim 23, wherein said binder material
is an inorganic binder material.
30. A method as defined in claim 23; and further comprising the
step of admixing with said fibrous mass a color substance prior to
shaping of said mixture.
31. A method as defined in claim 23; and further comprising the
step of adding to said mixture, prior to shaping thereof, at least
one substance from the group composed of insecticides, fungicides
and combustion-retardants.
Description
BACKGROUND OF THE INVENTION
The present invention relates generally to the processing of
refuse, and in particular to the method of carrying out such
process.
Still more particularly, the invention relates to a method of
processing household, agricultural, and forestry refuse,
individually or in various combinations.
It is hardly necessary to point to the ever-increasing accumulation
of refuse. The problem of refuse disposal is taking on more and
more importance on a world-wide basis, requiring constantly
increasing expenditures for the collection and disposal of the
rising quantity of refuse generated everywhere. The problems
involved are both physical and financial, not to mention aesthetic.
Physically, refuse is frequently difficult to dispose of, partly
because of its nature (e.g. one-way bottles or the like), and
partly because of the fact that the sheer quantities of refuse
involved tend in many instances to outstrip the disposal
facilities. From a financial point of view, of course, the
increasing amount of refuse generated each year of course puts a
very substantial strain on the budgets of towns and
municipalities.
The attempt to physically dispose of the refuse has included the
proposition to utilize the refuse to the extent possible. This has
involved attempts to compost the refuse in order to try to obtain
humus for use in agriculture. However, no really satisfactory
solution to this problem has heretofore become known. On the other
hand, attempts to burn the refuse have also been only partially
successful because the high percentage of ash residue, and the
attendant disposal problems relative to the same, have made it
economically inadvisable to resort to this disposal method.
SUMMARY OF THE INVENTION
Accordingly, it is an object of the invention to overcome the
disadvantages outlined above.
More particularly, it is an object of the invention to provide an
improved method of processing refuse.
Still more particularly, it is an object of this invention to
provide a method by which household, forestry and agricultural
refuse can be processed in such a manner as not only to dispose of
it physically, in order to rid oneself of it, but so as to actually
convert the refuse into commercially utilizable semi- finished
products.
In other words, the invention proposes to deal with the
refuse-disposal problem by utilizing the refuse to the extent
possible in a positive manner, namely by converting it into useful
products. Evidently, this not only achieves one object, namely to
dispose of the refuse, but it eliminates the expenditures of money
heretofore required for disposing of the refuse, it eliminates the
need to find physical locations or plants for disposal of the
refuse, and even more importantly, in an age of shrinking physical
resources the invention makes it possible to utilize the refuse
itself as such a resource, namely as a basic raw material from
which to make useful products.
In keeping with these objects, and others which will become
apparent hereafter, one feature of the invention resides, briefly
stated, in a method of processing refuse according to which a
quantity of refuse be it household, forestry of the agricultural
variety, is subjected to aerobic decomposition in order to form an
aerobic decomposition substrate having a liberated fiber content.
This substrate is then subjected to a treatment whereby its
moisture content is adjusted within a predetermined range,
preferably below 10%, and results in the conversion of the
substrate into a finely structured essentially dry fibrous mass
containing various particle sizes with the term "particle" as
utilized herein referring to fibrous as well as non-fibrous
particles. The fibers may be of various lengths and may be more or
less straight or curled or rolled up. In any case, the mass is then
admixed with the hardenable binder material, preferably a synthetic
plastic resin, and then the resulting mixture is shaped to a
predetermined configuration which it retains as the binder material
hardens. It is preferred to use a binder material which is
thermo-setting and the admixture is preferably subjected to
pressure as the binder material hardens.
The refuse is advantageously composed of refuse which is the
product of existing refuse composting installations wherein
heretofore it was attempted to convert refuse to humus capable of
utilization in agriculture. In this manner it is possible to
continue to utilize such installations and to convert their output
into commercially useable products.
A dye or coloring agent may be admixed with the mass and/or the
binder material so that the finished product can have the desired
coloration. Furthermore, at any stage of the processing steps a
combustion-retarding agent can be added in order to retard or
prevent combustion of the finished product. Evidently, the product
can be shaped to many different configurations so that it may have
the form of plates or panels and can be used in the building
industry, or it may have other shapes. Insecticides and/or
fungicides may also be added in addition to or in lieu of
combustion-retarding agents, to prevent the deposition of insect
eggs or the hatching of live insects from the same, either on or in
cracks, pores or the like of the finished article. Insofar as
fungicides are concerned, this avoids the development of mold if
the finished article comes in contact at a later time with
moisture. The density of the finished article may be influenced as
desired by adding thermoplastic materials to the mass of fibrous
matter.
Prior to subjecting the refuse to aerobic decomposition, hard
articles such as rocks, metal parts or the like may be removed
therefrom. Usually, the dry fibrous mass will be admixed with dust
and particles of heavy specific gravity, such as rocks and metallic
pieces, which of course are usually a part of refuse, especially
the household refuse. It will also contain a coarse fiber fraction
and the length of the fibers in the mass will vary greatly. If the
fibers have become rolled up during processing, different diameters
in the thus-formed rolls are observed. If the mass is formed to
make plates or panels for building purposes, the heterogeneous
structure of the mass which is converted into such panels has been
found to be disadvantageous, in that thin plates of 10-15 mm.
thickness are required for the interior structure of buildings and
also particularly for furniture construction and need very
frequently have aesthetically pleasing rather smooth surfaces. On
the other hand, insulating panels of a mixture of fiber material
obtained according to the invention with cement, should have coarse
and rather long fibers. Also, a uniform fiber length may be desired
in order to obtain certain values of strength in the finished
product.
The present invention therefore proposes according to a further
concept to segregate the dry mass obtained into a plurality of
fractions, including a finest fraction and a coarsest fraction. It
has been found advantageous but not mandatory to segregate such
fractions and to use only the finer fractions for further
processing whereas the coarsest fraction is dealt with separately,
for instance by subjecting it to mechanical size reduction and
returning it again to the segregation process.
The novel features which are considered as characteristic for the
invention are set forth in particular in the appended claims. The
invention itself, however, both as to its construction and its
method of operation, together with additional objects and
advantages thereof, will be best understood from the following
description of specific embodiments when read in connection with
the accompanying drawings.
BRIEF DESCRIPTION OF THE DRAWING
FIG. 1 is a diagrammatic illustration showing a series of operating
stages in the method of the present invention;
FIG. 2 is a front view of an apparatus for carrying out the
invention; and
FIG. 3 is a side view of FIG. 2.
DESCRIPTION OF THE PREFERRED EMBODIMENTS
Before entering into a detailed description of the Figures, the
following example will serve to characterize the present
invention.
A quantity of the usual household refuse contaiing rocks, bottles,
metal parts and the like, as well as wet refuse, paper and the
like, was first subjected to a segregation step in which the hard
articles such as the rocks, bottles and metal parts were removed.
Thereupon the remainder of the refuse was subjected to mechanical
comminution. The refuse was then homogenized and subjected to an
aerobic decomposition process with a compost resulting, having a
content of 44.21% water and 55.79% dry substance. This compost was
subjected to the influence of an air stream whose temperature
upstream of the compost was 400.degree.C. and whose temperature
downstream of the compost was 140.degree.C. As a result of contact
with the air stream the compost was heated to 100.degree.C. and
dried to a final moisture content of approximately 5%. The total
quantity loss resulting from such drying process was 75.42%
including the loss of moisture and the loss of a certain amount of
dry substance.
The dried compost, now constituting a fibrous mass, had the
following composition:
carbon 33.19% hydrogen 4.91% oxygen 12.16% nitrogen 1.02% sulphur
0.29% chlorine 1.4% phosphorous 0.37% ash 44.06%.
Heating and drying of the compost at 180.degree. C. temperature
resulted simultaneously in sterilization of the material, and
subsequent tests failed to show the presence of any bacteria.
The resulting matter was a mass which was dry, neutral, and fibrous
as well as odorless. A quantity of 460 grams of this mass was
admixed with 90 grams of woodchips. A quantity of 120 grams of
ureaformaldehyde resin and 30 grams of an accelerator were mixed
separately under intensive stirring and then admixed slowly--again
under intensive stirring--with the mixture of 460 grams of fibrous
mass and 90 grams of woodchips. After the mixture of
ureaformaldehyde resin and accelerator--together constituting a
hardenable binder material--was intermittently admixed with the
combination of fibrous mass and woodchips, the resulting mixture
was arranged in a layer of 7 cm thickness on a Teflon (trademark)
support with which it was placed into a press that had been
preheated to approximately 130.degree.-140.degree.C. In this press
the mixture was subjected for a period of 12 minutes to constant
pressure of 30 kg/cm.sup.2. It was found advisable not to let the
temperature drop below 130.degree.C. during this molding
process.
The shaped article resulting from this operation, namely a plate,
was permitted to slowly cool, until complete hardening of the
binder material and in order to assure polycondensation. The
finished plate had a thickness of 1.5 cm., and the visual
appearance of the conventional fiber board panel with the fiber
structure analogous to that of conventional fiber board panels, was
clearly visible with the naked eye. No coloring agent was added,
but this could have been admixed with the ureaformaldehyde resin if
it had been desired to impart to the finished plate a particular
color.
The refuse as it is derived from household sources may includes
bones, paper, cardboard, plastic discarded packages, meats,
vegetables, wood, ash and so on. An aerobic decomposition substrate
can be produced by any aerobic decomposition of the refuse, but for
accelerating the decomposition process the refuse is composted in a
suitable tank. Fungicides and insecticides may be added up to 20%
of the quantity of the binder material. Ureaformaldehyde and
phenolic resin can be used for binder materials, and suitable
accelerators are available and well known.
Referring now to FIG. 1, the various steps of the novel process
will now be illustrated and discussed, based on this diagrammatic
figure.
Refuse, that is household refuse, agricultural refuse and/or
forestry refuse is generally identified with reference numeral 1
and is admitted via a suitable gripper 2 into a rotating
fermentation drum 3 of the type which is known per se. During the
decomposition period which may last between 2 and 4 days, the
refuse is subjected in the drum 3 to an aerobic decomposition
process and is also subjected to size reduction due to the rotation
of the drum. When the decomposition process is completed, the
refuse leaves the drum 3 as fresh compost or substrate and then is
made to fall onto a belt conveyor 4 from where it is conveyed via a
chute 5 into a drying oven 6. In the latter the substrate or
intermediate product is subjected to drying to reduce its water
content to below 10%, and it is also sterilized. A ventilator 7 is
provided for withdrawing the liberated gases of the oven 6 via a
cyclone 8, a conduit 9 and a horizontal tube 10 which has a
downwardly directed opening 11 preceded, in the flow direction of
and air stream gases by a baffle 12. The opening 11 and baffle 12
serve to reduce the flow speed of the gases and thus permit a
descent of coarse particles of heavy specific weight, for instance
stones, so that these will fall through the opening 11.
The cyclon 8 yields a fiber granulate or fiber material which is
now admitted into an enclosed bucket elevator 14 and from the same
via a slide 15 into the inlet opening 16 of a screen housing 17.
The housing 17 is mounted on springs (not separately illustrated)
so that it can vibrate and oscillate and is provided with a
similarly non-illustrated vibratory drive. Such drives are well
known and require no detailed discussion; their purpose is to
transmit vibration to a component, in this instance to the housing
17.
Mounted in the housing 17 in vertically superimposed relationship
are the screens S1, S2, S3 and S4, as well as a receptacle S5. The
mesh of the screens decreases in downward direction, that is the
screen S1 has the largest mesh and the screen S4 the smallest. Each
of the screens S1-S4 as well as the receptacle S5 have an outlet
opening. The largest or coarsest fraction is, of course, retained
on the screen S1 because due to the large mesh thereof all but the
coarsest matter will pass through it. The fraction retained by the
screen S1 is advanced by a conveying device 18 to a comminutor 19
wherein it is mechanically subjected to a reduction of its size,
that is it undergoes comminution. Once it has been comminuted, this
fraction is returned by the conveying device 20 to the inlet
opening 16 of the housing 17 and once again passes through the
segregating cycle. A suction conduit 21 communicates with the
opening 16 and is connected via a cyclone 22 with the suction
intake of a centrifugal blower 23. Of course, other suction sources
could be utilized. The blower 23 draws air through the outlet
openings of the screens S1-S4 as well as the outlet opening of the
receptacle S5. The air is further drawn to the funnel 13 and the
elevator housing 14. Due to this, dust, and some of the smallest
fraction is withdrawn from the fibrous mass admitted via the inlet
opening 16, and is separated in the cyclone 22 from the airstream.
In addition, the air which is aspirated by the blower 23 provides
for cooling of the still warm or hot fibrous matter in the bucket
elevator housing 14 and in the housing 17. Finally, clogging of the
screens S1-S4 by dust and the inevitably resulting decrease in
efficiency, is avoided by this measure.
The material from which the coarsest fraction has already been
removed, now passes through the screens S2, S3 and S4. The screen
S2 retains a fraction which is finer than the coarsest fraction and
is designated as F2. The screen S3 and S4 retain the fractions F3
and F4, with the latter being the finest fraction. The retained
fractions F2, F3 and F4 are withdrawn by respective centrifugal
blowers 24, 25 and 26 via conduits 27, 28 and 29. During such
withdrawal the fractions pass through air sifting or separating
devices 30, 31 and 32, respectively. The flow speed of air in the
devices 30-32 is so selected that the respective fibrous material
of the fraction being processed will float upwardly with the air in
the device, whereas the heavier particles of the fractions will
drop downward and leave the respective device 30, 31 or 32. These
particles can then be added to the particles which issue from the
opening 11; inasmuch as such particles are mostly stones or glass
pieces, they can be deposited in suitable outdoor dumps without any
danger of environmental contamination.
The fractions F2, F3 and F4, which have now been cleaned in the
devices 30-32, respectively, of heavy contaminants, are then drawn
by the air aspirated by the blowers 24-26 into separate storage
units. The portion of the finest fraction F5 which has been drawn
into the cyclone 22 and separated therein from the airstream is
also admitted into a storage unit. From the container S5 the
smallest fraction is advanced via a conveying device 33 into the
wet separator 34 shown in FIGS. 1 and 2. In this separator the
heavy particles such as grains of sand and pieces of glass, are
separated from the remainder of the fraction and are removed
separately via a conveyor belt 35, to be introduced into a storage
unit 36. The light-weight components of the finest fraction are
deposited wet onto a conveyor belt 37 which advances them to an
intermediate storage device F'5 from where they are transported by
the conveying device 38 through the funnel 5 into the drying
apparatus 6, to be dried and subsequently to be returned into the
segregating cycle.
It has been observed that the individual fractions F2-F5 are of
very uniform structure and are largely free of heavy contaminant
particles. These thus segregated and cleaned fractions can now be
admixed with a binder as outlined earlier and can be pressed in
presses 39 or 40 to form one-layer plates 41, or to form in any
desired combination three or multiple layer plates 42 or any other
desired shape. FIG. 2 shows details of the wet separator 34 and
FIG. 3 is a side view of FIG. 2. The separator 34 has a container
50 which is closed at the top and provided with a lateral
connecting flange 51 to which there is secured an outlet housing
52. The latter is supported on supports 54. An endless conveyor
belt 35, driven by a motor 55 is mounted in the housing 52 and
extends diagonally into the housing 50. Four (corresponding to the
number of fractions) separating funnels 56 extend from above into
the housing 50 and at each of the funnels 56 there is arranged,
ahead of or in front of the rear wall, a deflecting baffle 57 which
defines at its free end with the rear wall a slot 58. A
water-conduit 59 terminates in the rear wall and is connected with
the supply conduit 70 via a reducing valve 60. A further reducing
valve 61 is interposed in an additional conduit 62 which also
communicates with the supply conduit 70 and communicates with the
interior of the housing 50.
Each of the funnels 56 is provided at its front side with an
overflow edge joined by a slide or chute 63 which discharges onto
the conveyor belt 36. The latter is driven by a motor 64, and
located below the belt 36 is a collecting container 65 with an
outlet 66.
When the device 34 is operated, the housing 50 is filled with water
to the overflow edges of the funnels 56 via the conduit 70, the
reducing valve 61 and the conduit 62. The supply of water via the
conduit 62 is maintained during the entire operation of the device
34. Water is further admitted via the conduit 59 into the funnels
56, and enters into the same via the slot 58. This means that in
the respective funnels 56 there exists a flow of water from below
in upward direction, and at the surface of the funnel a flow of
water from the slot 58 towards the overflow edge and the chute 63.
The finest fraction F5 received in the receptacle S5 is poured into
the funnels 56, from above. The flow of water in the device 34 is
adjustable with the valves 60 and 61, and in particular in such a
manner that the flow is not strong enough to prevent the heavier
particles of the fraction in the funnels 56 from dropping
downwardly counter to the flow of water, but is strong enough to
carry along the lighter particles which are those desired to be
recovered, to the chute 63 and the conveyor 36. The heavier
particles, however, descend under the force of their own weight in
the flow of water counter to the flow direction thereof, to become
deposited on the conveyor 35 which carries them out of the housing
50. This means that at the outlet end of the conveyor 35, the
heavier particles can be recovered, and that at the outlet end of
the conveyor 36 the lighter particles of the finest fraction can
also be recovered.
It is also possible, although not specifically illustrated, to dry
the lighter particles recovered at the outlet end of the conveyor
36 in a separate non-illustrated drying apparatus and to convey
them from there into the storage unit provided for storage of the
finest fraction F5.
The admixing of the individual fractions, which latter may in turn
be admixed in any desired ratio or be utilized separately, with a
binder can be carried out in the manner outlined earlier, and
similarly, the resulting mixture can be further processed as
outlined earlier in order to obtain shaped bodies therefrom.
Organic or inorganic binders may be used, particularly such
duroplastic binders as epoxy or polyurethane resins, or else
thermoplastic bituminous substances combined with carbohydrate
resins or analogous matter. Also, mineral-based fibers of cement,
gypsum or alkali-silicate mixtures can be employed.
It will be understood that each of the elements described above, or
two or more together, may also find a useful application in other
types of constructions differing from the types described
above.
While the invention has been illustrated and described as embodied
in a method of processing refuse for conversion into shaped bodies,
it is not intended to be limited to the details shown, since
various modifications and structural changes may be made without
departing in any way from the spirit of the present invention.
Without further analysis, the foregoing will so fully reveal the
gist of the present invention that others can, by applying current
knowledge, readily adapt it for various applications without
omitting features that, from the standpoint of prior art, fairly
constitute essential characteristics of the generic or specific
aspects of this invention and, therefore such adaptations should
and are intended to be comprehended within the meaning and range of
equivalence of the following claims.
* * * * *