U.S. patent number 3,572,524 [Application Number 04/778,726] was granted by the patent office on 1971-03-30 for mechanical equipment for charging sludge and/or semisolid and fluid waste material into rotary incinerating kilns.
This patent grant is currently assigned to Von Roll AG. Invention is credited to Heribert Muckenheim.
United States Patent |
3,572,524 |
Muckenheim |
March 30, 1971 |
MECHANICAL EQUIPMENT FOR CHARGING SLUDGE AND/OR SEMISOLID AND FLUID
WASTE MATERIAL INTO ROTARY INCINERATING KILNS
Abstract
There is disclosed new and improved mechanical charging
equipment for rotary incinerating kilns. This equipment renders it
possible for sludges and/or viscous, pasty and/or semisolid and
fluid waste materials to be fed into such incinerators
indifferently, regardless of their condition at delivery, whether
in bulk or containers.
Inventors: |
Muckenheim; Heribert (Dietikon,
CH) |
Assignee: |
Von Roll AG (Gerlafingen,
CH)
|
Family
ID: |
4419425 |
Appl.
No.: |
04/778,726 |
Filed: |
November 25, 1968 |
Foreign Application Priority Data
|
|
|
|
|
Nov 28, 1967 [CH] |
|
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16,691/67 |
|
Current U.S.
Class: |
414/149;
110/110 |
Current CPC
Class: |
F23G
5/442 (20130101) |
Current International
Class: |
F23G
5/44 (20060101); F23k 003/14 () |
Field of
Search: |
;110/8,101,110
;214/18,18 (RK)/ ;214/21,19,17.82 |
References Cited
[Referenced By]
U.S. Patent Documents
Foreign Patent Documents
Primary Examiner: Sheridan; Robert G.
Claims
I claim:
1. Mechanical charging equipment for charging sludge and/or
viscous, pasty and/or semifluid waste materials into incinerating
furnaces, especially into rotary kilns, comprising a stationary and
substantially circular receiving trough, said receiving trough
incorporating sidewall means and a bottom portion, a substantially
circular and flat distribution plate disposed substantially
horizontally above said bottom portion of said receiving trough and
rotatably supported by a central pivot, electrical drive means for
rotating said distribution plate in both directions of rotation, at
least one conveyor means of the endless screw type, electrical
drive means for driving said conveyor means, said conveyor means
being located in approximately horizontal and radial position above
said distribution plate, said drive means for said distribution
plate and said drive means for said conveyor means enabling the
rotational speeds of said distribution plate and said conveyor
means to be infinitely varied independently of one another, said
conveyor means incorporating a discharge end protruding across said
sidewall means of said receiving trough and assuming a position
capable of communicating with the rotary kiln, a feeding chute
arranged at said rotary kiln, an enclosed substantially duct-shaped
housing provided externally of said receiving trough and tightly
fitted to said sidewall means of said receiving trough, said
duct-shaped housing surrounding the protruding portion of said
conveyor means and leading the refuse via said feeding chute into
said rotary kiln.
2. Mechanical charging equipment as defined in claim 1, further
including an additional conveyor means of the endless screw type
having its helix and rotational sense opposed to the
first-mentioned conveyor means, both said conveyor means being
located in approximately side-by-side relationship and
approximately parallel to one another within said substantially
duct-shaped housing leading the refuse via said feeding chute into
said rotary kiln.
3. Mechanical charging equipment as defined in claim 1, further
including means for heating said distribution plate.
4. Mechanical charging equipment as defined in claim 1, wherein
said central pivot is arranged substantially at the central region
of said receiving trough.
Description
BACKGROUND OF THE INVENTION
The present invention relates to new and improved equipment for
charging sludges and/or viscous, pasty and/or semifluid waste
materials into rotary kilns or the like with the intention of
bringing about their incineration therein.
The use of rotary kilns as incinerators for sludgy viscous, pasty
and/or semifluid waste materials, hereinafter conveniently referred
to as refuse, either alone or together with solid refuse, is well
known and practiced in the art of refuse destruction. It has hereby
been found that the combustion process of such materials is very
much prompted and favored by a homogeneous mixture of the various
materials to be incinerated, and that such homogeneous mixture may
be best achieved prior to the actual incineration, that is, during
charging into the incinerator.
Although such materials are usually received in very different
states, with regard to both their consistency and their containers,
they have to be fed into the incinerator through a single charging
aperture, this aperture usually being provided with a funnel or
hopper or with some similar device and with an adjoining chute
leading into the kiln proper.
The refuse to be incinerated is usually handled by means of
grab-cranes, gripping some 30-- 70 cu. ft. at a time. This means
that intermittent amounts of this volume have to pass at a time
through the charging funnel or hopper and the following chute. On
the other hand, due to the limited width of the kiln proper, the
devices mentioned above can be only of comparatively small cross
section, unable to "swallow" the amounts delivered by the
grab-crane. This unfailingly leads to bridging or clogging in the
charging path, resulting in irregularities in the combustion
process, and with the kiln eventually being placed out of service
due to lack of feeding.
Another problem arising in this connection is that, in most cases,
the refuse to be incinerated is received in metallic bins, drums or
barrels which have to be recovered and returned to the owners,
therefore have to be emptied--a most difficult and troublesome
affair.
The charging process is moreover complicated by the fact that the
various kinds of refuse are usually received batchwise at regular
hours of the day, so that the kiln is fed at a time with, for
instance, only very fluid refuse, next with a thick and pasty one,
all of which renders quite elusive the recommended homogenous
mixture. This is the case, even when intermediate storing is
undertaken, which however in most cases is impossible. Thus optimum
conditions cannot be ensured for the incineration process.
SUMMARY OF THE INVENTION
Accordingly, it is a primary object of the present invention to
provide improved mechanical charging equipment for incinerators
which effectively overcomes the drawbacks of the prior art
structures mentioned above.
Another, more specific object of the present invention aims at the
provision of improved mechanical charging equipment for
incinerators, especially rotary kilns, employed for the
incineration of sludges and/or viscous, pasty and/or semifluid
refuse, wherein the incineration process is undertaken during
substantially improved conditions over prior art techniques.
Still a further extremely noteworthy object of the present
invention pertains to the provision of improved mechanical charging
equipment for refuse which handles the refuse in a manner leading
to improved combustion thereof, while simplifying the handling and
charging of the refuse to thereby provide for a more efficient and
uniform combustion process.
Yet a further substantial object of the present invention relates
to the provision of an improved mechanical charging device for
rotary incinerating kilns or the like which is relatively simple in
construction, extremely reliable in operation, requires a minimum
of supervision, can operate in such a manner that there is very
little likelihood of having to interrupt the incineration process
due to malfunction of the charging equipment, and wherein the
refuse or waste materials handled by the charging equipment are
processed in such a way that substantially uniform and efficient
combustion techniques are achieved.
Now, in order to implement these and still further objects of the
invention, which will become more readily apparent as the
description proceeds, the present invention concerns itself with
charging equipment, especially charging equipment which is
particularly suitable for use in conjunction with rotary kilns
employed for the incineration of sludges and/or viscous, pasty
and/or semifluid refuse. According to the invention this charging
equipment incorporates a stationary receiving trough of
substantially circular shape. An equally circular distribution
plate is located above the bottom of the trough and is mounted to
be rotatable about a substantially vertical axis. According to a
preferred construction of the invention there is provided at least
one screw-conveyor which is disposed radially and nearly
horizontally above the distribution plate. This screw-conveyor
protrudes across the sidewall of the receiving trough, terminating
in convenient relative position to the receiving devices of the
rotary kiln. Furthermore, suitable electrical drive means are
provided for both the distribution plate and the
screw-conveyor.
BRIEF DESCRIPTION OF THE DRAWING
The invention will be better understood and objects other than
those set forth above, will become apparent, when consideration is
given to the following detailed description thereof. Such
description makes reference to the annexed drawing wherein:
FIG. 1 is a schematic representation, in longitudinal sectional
view, of the charging end of a rotary kiln equipped with the
inventive charging equipment; and
FIG. 2 schematically shows in a cross-sectional view taken along
the line II-II of the FIG. 1 details of a portion of a modified
form of inventive charging equipment.
DESCRIPTION OF THE PREFERRED EMBODIMENTS
Describing now the drawing, it will be understood that FIG. 1
illustrates, in the exemplary embodiment shown, an incinerator in
the form of a rotary kiln 11, the front end of which is equipped
with a charging hopper 9 and and a feeding chute 10 constituting
the stationary charging equipment for the solid refuse which is to
be combusted. This refuse is conveniently supplied into the
charging hopper 9 by means of a suitable grab-crane 12 which
unloads therein.
As further evident by referring to FIG. 1, the invention
contemplates the provision of a substantially circular receiving
trough 1 which embodies an equally circular and horizontal bottom
1a provided with the substantially circular sidewall 2. The upper
portion 2' of the receiving trough 1 is widened to provide a
suitable taper, as shown. The size of this receiving trough 1, that
is to say, the diameter of its bottom 1a , is advantageously
selected in accordance with the incineration capacity of the rotary
kiln 11. This receiving trough 1 and its supporting frame structure
3 constitute the stationary components of the inventive equipment.
The refuse which is to be incinerated, whether it be sludgy,
viscous, pasty and/or semifluid in consistency, is discharged into
this receiving trough 1 by suitable means, which will be considered
in greater detail hereinafter, such means being completely
appropriate for the condition or state of the refuse when
received.
If such refuse is delivered in bins, drums, barrels or similar
containers or receptacles, these containers are then hoisted by a
suitable elevator 8 fitted with a tilting attachment of any known
design at its upper end, so that they can be emptied into the
receiving trough 1 by a convenient chute or similar device. When
received in bulk, the refuse is handled by the grab-crane 12 for
delivery into the receiving trough 1 by known techniques.
Inside the receiving trough 1 and at a certain distance above its
bottom 1a , a flat and circular distribution plate 5 is located in
substantially horizontal position. This distribution plate 5 is
rotatably supported by a pivot 6 substantially at the center of the
receiving trough 1. A suitable electric drive 20 serves to
selectively rotate the distribution plate 5 in both directions at
infinitely variable speeds. At some distance above the rotating
distribution plate 5 there is provided a substantially horizontal
conveyor 7, here shown as being of the endless screw type. The
screw-conveyor 7, in turn, is equipped with a suitable
schematically illustrated electric drive 21, whereby the rotating
speed of said conveyor 7 is rendered infinitely variable
independently of that of the distribution plate 5. When considered
in relation to the pivot 6 of the rotating distribution plate 5,
such screw-conveyor 7 is located in radial position. The external
end of screw-conveyor 7 protrudes across and through the sidewall 2
of the receiving trough 1. The protruding end of screw-conveyor 7
is enclosed within a duct-shaped housing 7a, tightly fitted to the
sidewall 2, and leading into the feeding chute 10 of the rotary
kiln 11. The helix and the speed of rotation of the screw-conveyor
7 are such as to ensure continuous feeding of refuse into the
rotary kiln 11, the refuse following the path 1-- 7-- 7a --10-- 11
as described above, while the size of said screw-conveyor 7, i.e.
its diameter is chosen in accordance with the throughput to be
handled. The position of the conveyor 7 above the rotating
distribution plate 5, that is, the vertical clearance between them
is infinitely variable and the discharge housing 7a is of
corresponding cross-sectional shape and size, to allow for a
sufficient range of vertical setting or adjustment.
The inventive charging equipment functions as follows:
After the grab-crane 12 unloads its contents into the receiving
trough 1, a heap of refuse is formed on the distribution plate 5
which is more or less pronounced according to the consistency of
the refuse handled. Similarly, by means of the tilting elevator 8
fluid refuse is poured from containers onto the distribution plate
5, where it is spread into a more or less flat patch.
The distribution plate 5 which is rotated at a convenient speed
brings the heaps and patches of refuse into contact with the
screw-conveyor 7, which previously has been set at a convenient
clearance. By virtue of this and with the screw-conveyor in
rotation, the refuse is withdrawn gradually from the receiving
trough 1, to be fed into the kiln 11 at a rate corresponding to the
kiln's incinerating capacity. It may be noted that owing to the
clearance between the screw-conveyor 7 and the distribution plate
5, only part of the refuse lying on said plate is being withdrawn
as described above, while the remainder is left on said plate,
thereby lengthening the time for its mixture with the next refuse
to come. Possible lumps or local accumulations or other similar
phenomena are flattened by the repeated effect of the
screw-conveyor, so that a practically homogeneous material is
obtained on said distribution plate, the inventive equipment acting
as a mixer.
In order to handle refuse of tarlike or extremely viscous
consistency, the rotating plate 5 may be heated by means of steam,
hot water or electricity, such heating means generally being
schematically indicated by reference character 5a.
The charging equipment heretofore described and essentially
comprising the receiving trough 1, the rotating distribution plate
5 and the screw-conveyor 7 may be installed to work either alone or
in combination with the charging equipment 9, 10 for solid refuse,
thus enabling all kinds of refuse to be fed into the rotary kiln
11.
As an alternative to the heretofore illustrated and described
embodiment shown in FIG. 1 of the drawing, it is possible to carry
out a different layout and arrangement as such is essentially
contemplated in FIG. 2. In this modification of the charging
equipment, there are employed two screw-conveyors 22 and 23 which
are located side-by-side and approximately parallel to one another.
These two screw-conveyors advantageously are constructed to possess
opposed helixes and are driven so that they rotate in opposite
directions of rotation or opposed senses. Moreover, the protruding
ends of the two screw-conveyors 22 and 23 outside the receiving
trough 1 can be located within a common ductlike shaped housing 24
which leads the refuse over the chute 10 or other suitable device
into the rotary kiln 11 of FIG. 1. Moreover, these screw-conveyors
can be equipped with separate discharge paths or with their
discharges collected into a single chute, such as shown by the
chute 10 in FIG. 2. As a result of this modification a more
intensive mixing and homogenizing effect may be achieved.
It should be apparent from the foregoing detailed description, that
the objects set forth at the outset to the specification have been
successfully achieved.
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