U.S. patent number 3,628,473 [Application Number 05/028,710] was granted by the patent office on 1971-12-21 for sewage mud sludge drying and incinerating installation.
This patent grant is currently assigned to Stein Industries. Invention is credited to Claude Maille.
United States Patent |
3,628,473 |
Maille |
December 21, 1971 |
SEWAGE MUD SLUDGE DRYING AND INCINERATING INSTALLATION
Abstract
A cyclone furnace for an installation for drying and
incinerating mud or sludge such as sewer sludge comprises a
vertical cylindrical chamber closed at its upper end and extended
downwardly by an internal frustoconical wall. The fuel and air for
combustion are introduced, optionally with the material to be
incinerated, tangentially into the cylindrical chamber. The waste
gases are removed by a duct at the lower end of the combustion
chamber. The temperature is sufficiently high to enable the ash to
drop from the lower end of the combustion chamber in liquid
form.
Inventors: |
Maille; Claude (Sarcelles,
FR) |
Assignee: |
Stein Industries (Paris,
FR)
|
Family
ID: |
9032476 |
Appl.
No.: |
05/028,710 |
Filed: |
April 15, 1970 |
Foreign Application Priority Data
|
|
|
|
|
Apr 16, 1969 [FR] |
|
|
6911743 |
|
Current U.S.
Class: |
110/244 |
Current CPC
Class: |
F23G
5/32 (20130101); C02F 11/06 (20130101); F23G
7/001 (20130101); Y02W 10/40 (20150501) |
Current International
Class: |
C02F
11/06 (20060101); F23G 7/00 (20060101); F23G
5/32 (20060101); F23g 005/12 () |
Field of
Search: |
;110/7,8R,8C,18,28,28F |
References Cited
[Referenced By]
U.S. Patent Documents
Primary Examiner: Sprague; Kenneth W.
Claims
What is claimed is:
1. Apparatus for incinerating dried sludges such as sewage mud or
sludge comprising a cyclone furnace having a vertical cylindrical
chamber closed at its upper end, an internal frustoconical wall
portion connected to the lower end of said cylindrical chamber,
said wall portion having a central outlet orifice, inlet means for
introducing fuel, combustion air and the sludges to said
cylindrical chamber, at least said combustion air being introduced
with a substantially tangential component of motion into said
combustion chamber, and means for removing both liquefied ash and
combustion gases from said cyclone furnace through said
orifice.
2. Apparatus according to claim 1, in which said orifice is
surrounded by a lower chamber having a frustoconical wall
surface.
3. Apparatus according to claim 2, in which said chamber has a
downwardly flared frustoconical wall surface.
Description
The invention relates to sewage mud or sludge drying and
incinerating installation, comprising substantially a drier and a
cyclone furnace, the latter being used for burning the dried sludge
and imparting a high temperature to the fumes, a first circuit
conveying the fumes from the drier to the outlet of the cyclone
furnace, where they mix with the furnace fumes, a second circuit
returning the said mixture to the drier inlet and being of
sufficient length, taking into account the temperature of the fume
mixture, for the latter to be practically deodorized at the drier
inlet, and a third circuit removing part of the deodorized fumes at
the drier inlet for expelling them into the atmosphere.
The present invention concerns a particular embodiment of the
cyclone furnace for incinerating the dried mud or sludge in an
installation according to U.S. application Ser. No. 800,149, filed
Feb. 18, 1969, now U.S. Pat. No. 3,521,581.
The cyclone-furnace type of incinerator according to the invention
comprises a vertical cylindrical chamber closed at the top part and
extended downwardly by a conically shaped portion provided with a
central orifice, the fuel and combustion air, and possibly the
materials to be incinerated, being introduced tangentially into the
cylindrical chamber.
Owing to this construction, the fumes are discharged through the
lower orifice and consequently maintain the walls of this orifice
at a temperature high enough to facilitate the flow of ash in the
liquid state through the said orifice.
The materials to be incinerated may be introduced tangentially,
like the combustion air and fuel, or separately through the upper
part of the apparatus. Of course, the cyclone furnace, which is to
provide intense combustion with a high-combustion temperature is
lined internally with refractory concrete and externally with an
insulating material.
Such an incinerator is particularly advantageous in an installation
according to said application because this simple construction is
very suitable for an industrial installation while ensuring safe
operation through the flow of ash in the liquid condition. This
liquid ash may be collected in a dry device or in cold water,
producing rapid cooling favorable to possible granulation of the
ash by a crusher placed below the cyclone furnace.
The following additional description, together with the single
FIGURE of the drawing, will make it quite clear how the invention
may be put into practice.
The drawing shows diagrammatically a vertical section of an
incinerator according to the invention coupled to a fume discharge
conduit in an installation according to said application, and to a
liquid ash recovery tank.
Preferably, the orifice 34 is bounded by a downwardly flared
conical surface 35. The furnace may be extended by a downwardly
flared conical portion 36 surrounding the orifice 34.
Internally, the furnace is lined with refractory concrete 37 and is
covered externally with insulating material 38.
The materials to be incinerated, which are dried mud or sludge, are
introduced into the cyclone furnace through one or more nozzles 39,
being preferably carried by the combustion air. The nozzles,
supplied by the conduit 12 of an installation according to the
parent U.S. Pat. No. 3,521,581 are substantially tangential to the
furnace wall for imparting a rotational motion to the materials and
air. The fuel which may be gas or fuel oil, may also be introduced
through the nozzle or nozzles 39 or through a separate nozzle.
Possibly, the materials to be incinerated may be introduced through
the top wall 32 of the cyclone, but in that case, the fuel and part
at least of the combustion air should be introduced
tangentially.
The liquid ash and the fumes escape through the orifice 34 and pass
through the chamber 40 bounded by the wall 36 which is also lined
with refractory concrete. By the action of the radiation from the
walls of the chamber 40 and the circulation of the fumes, the
orifice 34 is kept at a high temperature, facilitating the flow of
liquid ash. Furthermore, the shape of the orifice 34, particularly
the edge 41 at the junction of the conical surfaces 33 and 35, is
designed to facilitate the flow of this liquid ash.
The fumes are discharged through the conduit 18 of the installation
according to said application, being possibly exhausted by a fan
(not shown) for ensuring good circulation inside the apparatus.
The liquid ash is collected, below the furnace, in a device 43,
either dry or in cold water, producing rapid cooling for permitting
possible granulation of this ash.
Of course, the cyclone-furnace type of incinerator, described more
particularly here, may be used not only for sewage mud or sludge
but also in a general manner for any residual mud or sludge from
chemical or various other industries.
* * * * *