CA1078260A - Incinerator for burning combustible refuse - Google Patents
Incinerator for burning combustible refuseInfo
- Publication number
- CA1078260A CA1078260A CA334,073A CA334073A CA1078260A CA 1078260 A CA1078260 A CA 1078260A CA 334073 A CA334073 A CA 334073A CA 1078260 A CA1078260 A CA 1078260A
- Authority
- CA
- Canada
- Prior art keywords
- refuse
- combustion
- chamber means
- combustion chamber
- air
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired
Links
- 238000002485 combustion reaction Methods 0.000 claims abstract description 94
- 239000007789 gas Substances 0.000 claims abstract description 26
- 230000000694 effects Effects 0.000 claims abstract description 6
- 239000000779 smoke Substances 0.000 claims abstract description 6
- 230000003247 decreasing effect Effects 0.000 claims abstract description 3
- 238000007599 discharging Methods 0.000 claims abstract description 3
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 22
- 239000007787 solid Substances 0.000 description 6
- 239000000428 dust Substances 0.000 description 5
- 239000013618 particulate matter Substances 0.000 description 5
- 238000001816 cooling Methods 0.000 description 3
- 239000000498 cooling water Substances 0.000 description 3
- 238000010586 diagram Methods 0.000 description 3
- 230000033001 locomotion Effects 0.000 description 3
- 238000010276 construction Methods 0.000 description 2
- 239000012716 precipitator Substances 0.000 description 2
- 229910000975 Carbon steel Inorganic materials 0.000 description 1
- 229910045601 alloy Inorganic materials 0.000 description 1
- 239000000956 alloy Substances 0.000 description 1
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 1
- 230000000903 blocking effect Effects 0.000 description 1
- 239000010962 carbon steel Substances 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 239000002184 metal Substances 0.000 description 1
- 229910052760 oxygen Inorganic materials 0.000 description 1
- 239000001301 oxygen Substances 0.000 description 1
- 238000005192 partition Methods 0.000 description 1
- 229920006395 saturated elastomer Polymers 0.000 description 1
- 239000010935 stainless steel Substances 0.000 description 1
- 229910001220 stainless steel Inorganic materials 0.000 description 1
- 238000003466 welding Methods 0.000 description 1
Abstract
ABSTRACT OF THE DISCLOSURE:
An incinerator for burning combustible refuse which comprises: a horizontally disposed stationary cylindrical combustion chamber means having an inlet end for receiving refuse and an outlet end for discharging residue and exhaust gases; ignition means adjacent the inlet end for igniting the refuse; screw conveyor means extending through the length of the chamber means for moving refuse at a decreasing rate from the inlet end to the outlet end of the chamber means as the volume of refuse is reduced by combustion, to effect better combustion of particulate smoke at the outlet end of the chamber means, the screw conveyor means including a rotatable auger having a longitudinal axis and a spiral flight having a larger pitch at the inlet end of the chamber means and a smaller pitch at the outlet end of the chamber means; and air supply means for supplying combustion air to said chamber means.
An incinerator for burning combustible refuse which comprises: a horizontally disposed stationary cylindrical combustion chamber means having an inlet end for receiving refuse and an outlet end for discharging residue and exhaust gases; ignition means adjacent the inlet end for igniting the refuse; screw conveyor means extending through the length of the chamber means for moving refuse at a decreasing rate from the inlet end to the outlet end of the chamber means as the volume of refuse is reduced by combustion, to effect better combustion of particulate smoke at the outlet end of the chamber means, the screw conveyor means including a rotatable auger having a longitudinal axis and a spiral flight having a larger pitch at the inlet end of the chamber means and a smaller pitch at the outlet end of the chamber means; and air supply means for supplying combustion air to said chamber means.
Description
.l~
a~s~60 - The present illvention is a division of the Canadian patent application No. 272.765 ~ . -The invention relates generally to incinerators, and more ;~` particularly to continuous controlled movement of combustible ..
refuse into, and through, a combustion chamber by a rotating auger conveyor.
i~ .
The use of an auger to convey combustible refuse throughthe combustion cycle results in very accurately controlled move-ment of refuse through the combustion chamber, in comparison to presently used rotary kiln incinerators. However, if the auger 10 flight is integral with the auger shaft, with no spacing between ,....
them, the passage of air through the refuse is restricted, and lt - is necessary to introduce air into the combustion chamber through the auger shaft and/or auger flight. Also, it lS necessary to supply cooling means for the auger flight as well as for the auger shaft. As a result, this type of auger is expensive to .~, .
....
~ manufacture, requiring much welding, and equally expensive to : ,.
1 repair or replace parts.
....;
`~ The auger construction used in the present invention over-.',~'."
comes these disadvantages by incorporating an annular space ;.:
20 between the auger shaft and auger flight. Thus air can move freely in the combustion chamber except for the space occupied by the auger shaft, and air can be introduced solely through the ,..
~i.
~- combustion chamber walls rather than through the auger shaft and flight assembly.
':
.
: .
~ .
8;~;0 .. :
Accordin~ to the present invention there is provided an incinerator for burning combustible refuse which comprises:
a horizontally disposed stationary cylindrical combustion cham-ber means having an inlet end for receiving refuse and an outlet ~, end for discharging residue and exhaust gases; ignition means ~, adjacent the inlet end for igniting the refuse; screw conveyor , means extending through the length of the chamber means for moving refuse at a decreasing rate from the inlet end to the outlet end of the chamber means as the volume of refuse is re-duced by combustion, to effect better combustion of particulate smoke at the outlet end of the chamber means, the screw conveyor means including a rotatable auger having a longitudinal axis and a spiral flight having a larger pitch at the inlet end of the chamber means and a smaller pitch at the outlet end of the ;, chamber means; and air supply means for supplying combustion air to the chamber means.
The following paragraphs give more details of the various features of the present invention.
The incinerator for burning combustible refuse dis-closed herein has a horizontally disposed stationary cylindri-cal combustion chamber. Refuse is introduced into an inlet por-:
tion of the incinerator from a feed hopper, and conveyed through the :
"
.
,, ., .
., ' 17 .,, .: .
, .
.. . .
~, . .
, . - . . ..
. ~ .
, .. . ..
` :` ` " --- 1078Z60 - furnace by a rotating auger, which also conveys the residue ,::":
~- remaining out the other end of the combustion chamber, where it drops into a water filled ash receptacle. The cooled residue `~ is then removed from this ash receptacle by a helical screw mechanism for disposal elsewhere.
Air for combustion is supplied by a fresh air inlet - blower through a hot air manifold extending substantially the ; length of the combustion chamber and forming a top inner por-tion of the combustion chamber wall. The bottom wall of this hot air manifold is uninsulated to effect good heat transfer from the combustion chamber to the air flowing in the manifold.
. . .
; The air is introduced into the lower part of the combustion chamber through hot air pipes spaced uniformly along both sides of the manifold, and extending around the combustion chamber to randomly spaced openings in the lower part of the combustion chamber, with each hot air pipe connected between the manifold and one air inlet opening.
Air for combustion is also introduced into the top of the , combustion chamber through uniformly spaced openings along both vertical sides of the hot air manifold which pro~ect downward into the combustion chamber. This air is introduced tangentially ; to the inner wall of the combustion chamber and is directed downwardly by the curvature of the wall to effect good mixing of air with the refuse. Also, this air flow prevents refuse from sticking to the top inner sides of the combustion chamber.
Air supplied by the fresh air inlet blower enters the hot air manifold near the exhaust end of the combustion chamber, '' ~ .
;~. . , ~;`
_~ 10782~0 .~ and is heated as it flows counter to the travel of the refus-e .
which is introduced at the inlet end of the combustion chamber.
Thus, while approximately equal volumes of air are supplied along the length of the combustion chamber, the hottest air is supplied to the inlet end, and the coldest and densest air is supplied near the outlet end of the combustion chamber. The hot air supplied at the inlet end quickly heats the incoming refuse; the cooler denser air supplied at the outlet end ~ " , ~, supplies more oxygen to effect total combustion and prevents . .; . .
, 10 emission of smoke.
. . ~
The helical shaped auger flight is disposed concentrically ; about a supporting water cooled hollow shaft extending the length of the combustion chamber, and is spaced from the shaft .:
by support members at uniform intervals along the shaft. This ., ; open area between the auger flight and the auger shaEt allows air to circulate more freely, both radially and longitudinally.
The pitch of the auger flight is varied from a maximum at the inlet end to a minimum at the outlet end of the com-;li; bustion chamber, to compensate for the decrease in volume of 3 20 solid particulate matter throughout the length of the combustion chamber as the refuse is burned.
The hollow auger shaft is cooled by passing water through ~ ., j~ it, ir. either a single or a double pass arrangement. In the . :
double pass arrangement the hollow auger shaft contains a ;~ .
; concentric pipe or smaller diameter tube extending the length - of the combustion chamber. Cold water enters through the smaller ~ :-? pipe, flows the length of the combustion chamber, and then flows back to the same end as it entered in the annular space "'.' ' .
,`:`
, --~
., :
~-` between the two pipes. The hot water leaving the auger shaft is then passed through a heat exchanger disposed in a passage ; for exhaust gases from the combustion chamber where this - water is further heated and the exhaust gases are cooled.
Alternatively, where a supply of steam is desirable, a single passed arrangement of cooling water through the auger shaft can be used. ~old water is flrst passed through the above-mentioned heated exchanger in the exhaust gas passage, and then introduced into one end of the hollow auger shaft.
Saturated steam is then drawn out of the other end of the auger shaft and passed through a superheater coil in the exhaust gas passage disposed between the first mentioned heated ex-, changer and the combustion chamber, to superheat the steam. The - exhaust gases leaving the above-mentioned superheater are passed through a centrifugal dust collector before being ex-hausted to the atmosphere.
` A portion of the exhaust air leaving the dust collector is diverted by a blower to an air curtain located in the refuse :,~
-~ feed hopper, creating an air pressure therein sufficiently . ., ~
high to prevent the flow of combustion air or gases out of the ' inlet side of the combustion chamber. At the same time, this hot exhaust gas pre-heats the refuse entering the incinerator.
Variable speed drives, such as hydraulic motors, or DC
electric motors, are used as the drive means for the auger, the fresh air inlet blower, and the exhaust air blower. In operation, the speed of the auger drive motor can be controlled : .
~ in dependence on the temperature sensing means located near the .,~.
exhaust end of the combustion chamber, to assure complete :' .. . .
-` 10782~0 combustion of the refuse. Likewise, the output of the fresh air inlet blower can be varied by varying the speed of its drive motor in dependence on a temperature sensing means lo-:'.'cated near the inlet end of the combustion chamber to assure ^"
~ that the air enterlng the combustion chamber at that point ~, :
` ~ has been properly pre-heated in the hot air manifold. Since : . .
the exhaust air blower operates to oppose the pressure pro-, , duced by the fresh air inlet blower, its speed can be varied the same as the fresh air inlet blower. Alternatively, the output of the exhaust air blower can be controlled in dependence on a directional air pressure sensing means dis-posed in the inlet hopper between the air curtain and the ., , inlet section of the combustion chamber to increase the output of the exhaust air blower whenever reverse flow of air through the inlet hopper is sensed.
,:
i For start-up of this incinerator, all fired igniters ., .
"~ are disposed in the cornbustion chamber walls near the inlet combustion chamber to start the combustion of the refuse.
:,. .
Also during start-up, a movable plate vertically disposed ,:
between the combustion chamber and the passage for exhaust gases, can be lowered to partially block passage of exhaust ; gases from the combustion chamber, thereby retaining heat ' '~'! , ,` in the combustion chamber to shorten the start-up period.
The present invention will becom~ more apparent from , study of the appended drawings herein:
., ...
. .
~:, ~, '~, .
, BRIEF DESCRIPTION OF THE DRAWINGS
.
, Fig. 1 is a side elevational view of the incinerator - with parts of the combustion chamber and exhaust passage `~ being shown broken away to show other parts in detail;
Fig. 2 is a cross-sectional end view of the inlet end of the incinerator taken along lines 2-2 of Fig. l;
.::
Fig. 3 is a cross-sectional view of the exhaust end of the lncinera,tor, taken along lines 3-3 of Fig. l;
Fig. 4 is a cross-sectional view of the combustion ~t'' 10 chamber, taken along lines 4-4 of Fig. l;
,;.
Fig. 5 is a water flow diagram for a double pass cooling arrangement for the auger tube; and ~; Fig. 6 is a water flow diagram for a single pass cooling : .
arrangement for the auger tube used for steam generation.
,;
,~f',"' Referring now to the drawings, Figs. 1-3 show a hori-;;" zontally disposed stationary cylindrical combustion chamber 10 ., ~ ~ having an opening 12 in the inlet section 14 through which ' r~ .:
combustible refuse is fed from a feed hopper 16. The outlet ~; section 18 has an upward-extending passage 20 for exhaust gases f 20 and a downward extending section defining an ash receptable 22 which is filled with water to a predetermined level 24.
. :.' .
Extending the length of the combustion chamber is a rotatable ., . - .
auger 26 having a tubular axis 28 supported at the inlet end ~ ~ 14 by bearing 30 mounted to the front wall 32 and at the outlet .,.:~ .
end 18 by another bearing 34 mounted to the rear wall 36, and ':.,`, ,~ -7-.'., `;
''' 107~Z6(~
~ ~ .
* driven by an hydraulic motor 38. The spiral flight 40 of . the auger 26 extends from the front wall 32 to the ash recep-. tacle 22, so that when the auger 26 is rotated, the auger flight 40 will convey combustible refuse entering from the ..,.. ~
feed hopper 16 through the combustion chamber 10, and deliver the solid residue to the ash receptacle 22. As can be seen in Fig. 1, the pitch of the auger flight 40 is greatest at the inlet section 14, and becomes gradually less toward the outlet section 18, to compensate for the reduction in volume of the ~;' 10 refuse which takes place during combustion. The tubular axis 28 is positioned off center of the ;l~is of the combustion .... .
.. chamber 10 so that there is minimum clearance between the , .I outer edge 42 of the auger flight 40, to assure movement of ^,~. essentially all of the refuse through the combustion chamber 10 .
~s shown in Fig. 1, the auger flight 40 is comprised of .:^ individual segments which are joined together and concentrically ." spaced from the tubular auger shaft 28 by a plurality of :~ .
support members 44, so that an open annular space 46 is formed 20 between the inner edge 48 of the auger flight 40 and the auger shaft 28. This open space 46 allows air to freely move upward through the combustion chamber 10 as well as along the auger shaft 28 to the outlet section 18. Different materials ,, , ~ having different heat resistant characteristics can be used in forming these sections of the auger flight 40. For example, in the inlet portion, where there is little heat, carbon steel could be used, while stainless steel or a refractory "',' '';
. .
' ` -~ 1078Z.60 .' , alloy could be used in the rest of the combustion chamber 10.
The tubular auger shaft 28 is water cooled and the advantages of this type of construction will be now described.
:
Fig. 1 shows an incoming water pipe 50 concentrically mounted within the tubular auger shaft 28 and connected to a source of cooling water 52. Water flows through this water pipe 50 the length of the combustion chamher 10, then reverses dir-ection by reason of the baffle 54 and flows back and out the same end of the shaft 28 through the water outlet pipe 56.
This water outlet pipe 56 connects to an inlet 58 of a heat ' exchanger 60 disposed in the exhaust gas passage 20, as shown in the water flow diagram of Fig. 5. After being further heated in this heat exchanger 60, the hot water is removed for use or storage elsewhere through a hot water pipe 62.
,:
,~ Fig. 6 shows an alternate cooling water arrangement .~
that can be used where a source of steam is desired. In this '~ alternate arrangement, cool water first enters the heat , , - exchanger 60 through the inlet 58, flows out of the heat exchanger 60 through outlet pipe 62 which is connected to the : 20 end of the tubular auger shaft 28 at the end of the incinerator.
In this arrangement, the inlet pipe 50 and the baffle or blocking partition 54 are omitted. Steam is generated from . . .
the hot water entering the tubular auger shaft 28, and is drawn off at a steam outlet 64 on the exhaust end of the shaft 28, . ., ' .
which is connected to an inlet 66 of a steam superheater coil 68 disposed in the exhaust gas passage 20 between the exhaust end of the combustion chamber 10 and the heat exchanger ';' .,:' ; _9_ ~ , .- :
` -~ 1078Z60 :`
60. The dry steam flows from the superheater coil 68 through an outlet 70 for use elsewhere.
Combustion air is supplied to the combustion chamber 10 .,~ by a fresh air inlet blower 72 driven by a hydraulic motor , ~ .
~; 74, through a hot air manifold 76 disposed within and extends longitudinally along the top of the combustion chamber 10.
This hot air manifold is formed of heat resistant metal to ~orm a passage shaped in cross-section as an annular segment . . .
'~ to conform to the inner wall 78 of the combustion chamber 10, ,, . ~ .
with an open end at the exhaust end of the combustion chamber ~, 10 to receive air from the fresh air inlet blower 72 and a closed end at the inlet end of the combustion chamber 10.
,:
The bottom of the hot air manifold 76 is uninsulated from the ' combustion chamber 10 so that the air flowing in the manifold ,..
76 can be pre-heated before entering the combustion chamber 10. A first plurality of hot air pipes 80 extends at uni-. ' .
form lntervals from both sides of the hot air manifold 76 through the refractory inner wall 78, around the combustion : ':
~` chamber to randomly spaced openings 82 in the lower portion '~ 20 of the combustion chamber 10, which direct the air radially inward and ~pward through the combusticn chamber. A second plurality of short hot air pipes 84 extend along at uniform ; intervals from both sides of the hot air manifold 76 to direct air tangentially along the top sides of the combustion chamber 10.
. . .
....... .
. --10--. .~, ., .
.~. , .
.. ,~
'', ' . .
-- 107826(~
Turning again to Fig. 1 it will be noted that there is shown a curved portion 86 of the exhaust gas passa~e 20 in which a plurality of inwardly projecting baffle plates 88 are disposed on the inside of the outermost curved wall to serve as preliminary dust collector traps, to trap a portion of the solid particulate matter in the exhaust gas and allow it to fall into the ash receptacle.
The solid particulate matter which falls into the ash receptacle 22 is cooled by the water therein, and then removed ;.,:~ : .
by a rotatable auger 90 which extends downward into the ash receptacle 22, and driven by a motor 92, as shown in Fig. 3.
This ash receptacle 22 has a sloping end wall and a semi-circular sloping bottom 94 concentric to and in close prOximity with the ash removal auger 90, so that essentially all solid particulate matter which enters the ash receptacle is directed ; to the ash removal auger 90.
Solid particulate matter is also removed from the exhaust gases in a dust precipitator 96 disposed near the outlet end ~ of the exhaust gas passage 20.
`~. 20 Also, as shown in Fig. 2, an exhaust gas blower 98 ., .
driven by a hydraulic motor 100 directs a portion of the ~^.......... exhaust gas which leaves the dust precipitator 96 to a plural-ity of inlets 102 in the feed hopper 16 forming an air curtain 104, so that the air pressure of the air curtain 104 is ,~ .
~ approximately equal to the air pressure of the combustion air . .
in the combustion chamber 10. This prevents the backward flow of exhaust gases and smoke from the combustion chamber :: -:
:.; 10. Also, this exhaust gas preheats the incoming combustible ;; --11--' ' ;
. . .
., - -~` 1078Z~;0 . ~
,', ~i refuse.
; A directional air pressure sensor 106, (Fig. 1) disposed :.
; within the feed hopper 12, senses a backward flow of com-bustion air and increases the speed of the hydraulic motor 100 for the exhaust gas blower 98 by a control means in the control panel 108.
~' A temperature sensor 110, disposed on the inner wall 78 of the combustion chamber 10 near the inlet to the combus-. .
;. tion chamber 10 is connected to a control means in the control .,;: .
" 10 panel 108 to regulate the speed of the hydraulic motor 74 driving the fresh air inlet blower 72 proportional to the temperature sensed by sensor 110, to assure that the air which :
enters the inlet end of the combustion chamber 10 is suf-ficiently pre-heated.
In a similar manner, a temperature sensor 112, disposed on the inner wall 78 of the combustion chamber 10 near the exhaust end of the combustion chamher 10 is connectea to a control means in the control panel 108 to regulate the speed of the hydraulic motor 38 for the auyer 26 in dependence on the exhaust end combustion chamber temperature, to assure com-plete combustion and reduce the smoke emission from the ~;, combustion cha~ber 10.
,.,."~
; There is best shown in Fig. 2, two oil fired ignitors 114 which are disposed in the inner wall 78 of the combustion ,~; chamber 10 near the inlet section 14 to initiate combustion of the refuse on initial start up of the incinerator. Also, ''"
':.
`;'''' . . .
.
a movable plate 116, vertically disposed on a side of the exhaust gas passage 20 at the exhaust end of the combustion . .~ .
;
:. chamber 10, can be lowered during the start up period to ,:.
partially block passage of exhaust gases from the combustion chamber 10, thus retaining heat in the combustion chamber 10 and thereby reducing the start up time.
, , .
.'` .
: ~ .
,,~, ~ .
.;;~ , , .
. .
,,.` ' .
....
" ' ' !
'~"1~ , '.
''."
~.. . .
' , ~' `'`, ' .
. ...................................................................... .
~ ~1 .!, ~
~;
,.; .
,. .
: '' .
.'.'.
': :~
:,.
. ',:, , ` .
':
:.,.
~, . .
,. -13-,,;
j: . .
";;
. .
,,:.
, '':,` .- . ~
,; ., .
:, . .
a~s~60 - The present illvention is a division of the Canadian patent application No. 272.765 ~ . -The invention relates generally to incinerators, and more ;~` particularly to continuous controlled movement of combustible ..
refuse into, and through, a combustion chamber by a rotating auger conveyor.
i~ .
The use of an auger to convey combustible refuse throughthe combustion cycle results in very accurately controlled move-ment of refuse through the combustion chamber, in comparison to presently used rotary kiln incinerators. However, if the auger 10 flight is integral with the auger shaft, with no spacing between ,....
them, the passage of air through the refuse is restricted, and lt - is necessary to introduce air into the combustion chamber through the auger shaft and/or auger flight. Also, it lS necessary to supply cooling means for the auger flight as well as for the auger shaft. As a result, this type of auger is expensive to .~, .
....
~ manufacture, requiring much welding, and equally expensive to : ,.
1 repair or replace parts.
....;
`~ The auger construction used in the present invention over-.',~'."
comes these disadvantages by incorporating an annular space ;.:
20 between the auger shaft and auger flight. Thus air can move freely in the combustion chamber except for the space occupied by the auger shaft, and air can be introduced solely through the ,..
~i.
~- combustion chamber walls rather than through the auger shaft and flight assembly.
':
.
: .
~ .
8;~;0 .. :
Accordin~ to the present invention there is provided an incinerator for burning combustible refuse which comprises:
a horizontally disposed stationary cylindrical combustion cham-ber means having an inlet end for receiving refuse and an outlet ~, end for discharging residue and exhaust gases; ignition means ~, adjacent the inlet end for igniting the refuse; screw conveyor , means extending through the length of the chamber means for moving refuse at a decreasing rate from the inlet end to the outlet end of the chamber means as the volume of refuse is re-duced by combustion, to effect better combustion of particulate smoke at the outlet end of the chamber means, the screw conveyor means including a rotatable auger having a longitudinal axis and a spiral flight having a larger pitch at the inlet end of the chamber means and a smaller pitch at the outlet end of the ;, chamber means; and air supply means for supplying combustion air to the chamber means.
The following paragraphs give more details of the various features of the present invention.
The incinerator for burning combustible refuse dis-closed herein has a horizontally disposed stationary cylindri-cal combustion chamber. Refuse is introduced into an inlet por-:
tion of the incinerator from a feed hopper, and conveyed through the :
"
.
,, ., .
., ' 17 .,, .: .
, .
.. . .
~, . .
, . - . . ..
. ~ .
, .. . ..
` :` ` " --- 1078Z60 - furnace by a rotating auger, which also conveys the residue ,::":
~- remaining out the other end of the combustion chamber, where it drops into a water filled ash receptacle. The cooled residue `~ is then removed from this ash receptacle by a helical screw mechanism for disposal elsewhere.
Air for combustion is supplied by a fresh air inlet - blower through a hot air manifold extending substantially the ; length of the combustion chamber and forming a top inner por-tion of the combustion chamber wall. The bottom wall of this hot air manifold is uninsulated to effect good heat transfer from the combustion chamber to the air flowing in the manifold.
. . .
; The air is introduced into the lower part of the combustion chamber through hot air pipes spaced uniformly along both sides of the manifold, and extending around the combustion chamber to randomly spaced openings in the lower part of the combustion chamber, with each hot air pipe connected between the manifold and one air inlet opening.
Air for combustion is also introduced into the top of the , combustion chamber through uniformly spaced openings along both vertical sides of the hot air manifold which pro~ect downward into the combustion chamber. This air is introduced tangentially ; to the inner wall of the combustion chamber and is directed downwardly by the curvature of the wall to effect good mixing of air with the refuse. Also, this air flow prevents refuse from sticking to the top inner sides of the combustion chamber.
Air supplied by the fresh air inlet blower enters the hot air manifold near the exhaust end of the combustion chamber, '' ~ .
;~. . , ~;`
_~ 10782~0 .~ and is heated as it flows counter to the travel of the refus-e .
which is introduced at the inlet end of the combustion chamber.
Thus, while approximately equal volumes of air are supplied along the length of the combustion chamber, the hottest air is supplied to the inlet end, and the coldest and densest air is supplied near the outlet end of the combustion chamber. The hot air supplied at the inlet end quickly heats the incoming refuse; the cooler denser air supplied at the outlet end ~ " , ~, supplies more oxygen to effect total combustion and prevents . .; . .
, 10 emission of smoke.
. . ~
The helical shaped auger flight is disposed concentrically ; about a supporting water cooled hollow shaft extending the length of the combustion chamber, and is spaced from the shaft .:
by support members at uniform intervals along the shaft. This ., ; open area between the auger flight and the auger shaEt allows air to circulate more freely, both radially and longitudinally.
The pitch of the auger flight is varied from a maximum at the inlet end to a minimum at the outlet end of the com-;li; bustion chamber, to compensate for the decrease in volume of 3 20 solid particulate matter throughout the length of the combustion chamber as the refuse is burned.
The hollow auger shaft is cooled by passing water through ~ ., j~ it, ir. either a single or a double pass arrangement. In the . :
double pass arrangement the hollow auger shaft contains a ;~ .
; concentric pipe or smaller diameter tube extending the length - of the combustion chamber. Cold water enters through the smaller ~ :-? pipe, flows the length of the combustion chamber, and then flows back to the same end as it entered in the annular space "'.' ' .
,`:`
, --~
., :
~-` between the two pipes. The hot water leaving the auger shaft is then passed through a heat exchanger disposed in a passage ; for exhaust gases from the combustion chamber where this - water is further heated and the exhaust gases are cooled.
Alternatively, where a supply of steam is desirable, a single passed arrangement of cooling water through the auger shaft can be used. ~old water is flrst passed through the above-mentioned heated exchanger in the exhaust gas passage, and then introduced into one end of the hollow auger shaft.
Saturated steam is then drawn out of the other end of the auger shaft and passed through a superheater coil in the exhaust gas passage disposed between the first mentioned heated ex-, changer and the combustion chamber, to superheat the steam. The - exhaust gases leaving the above-mentioned superheater are passed through a centrifugal dust collector before being ex-hausted to the atmosphere.
` A portion of the exhaust air leaving the dust collector is diverted by a blower to an air curtain located in the refuse :,~
-~ feed hopper, creating an air pressure therein sufficiently . ., ~
high to prevent the flow of combustion air or gases out of the ' inlet side of the combustion chamber. At the same time, this hot exhaust gas pre-heats the refuse entering the incinerator.
Variable speed drives, such as hydraulic motors, or DC
electric motors, are used as the drive means for the auger, the fresh air inlet blower, and the exhaust air blower. In operation, the speed of the auger drive motor can be controlled : .
~ in dependence on the temperature sensing means located near the .,~.
exhaust end of the combustion chamber, to assure complete :' .. . .
-` 10782~0 combustion of the refuse. Likewise, the output of the fresh air inlet blower can be varied by varying the speed of its drive motor in dependence on a temperature sensing means lo-:'.'cated near the inlet end of the combustion chamber to assure ^"
~ that the air enterlng the combustion chamber at that point ~, :
` ~ has been properly pre-heated in the hot air manifold. Since : . .
the exhaust air blower operates to oppose the pressure pro-, , duced by the fresh air inlet blower, its speed can be varied the same as the fresh air inlet blower. Alternatively, the output of the exhaust air blower can be controlled in dependence on a directional air pressure sensing means dis-posed in the inlet hopper between the air curtain and the ., , inlet section of the combustion chamber to increase the output of the exhaust air blower whenever reverse flow of air through the inlet hopper is sensed.
,:
i For start-up of this incinerator, all fired igniters ., .
"~ are disposed in the cornbustion chamber walls near the inlet combustion chamber to start the combustion of the refuse.
:,. .
Also during start-up, a movable plate vertically disposed ,:
between the combustion chamber and the passage for exhaust gases, can be lowered to partially block passage of exhaust ; gases from the combustion chamber, thereby retaining heat ' '~'! , ,` in the combustion chamber to shorten the start-up period.
The present invention will becom~ more apparent from , study of the appended drawings herein:
., ...
. .
~:, ~, '~, .
, BRIEF DESCRIPTION OF THE DRAWINGS
.
, Fig. 1 is a side elevational view of the incinerator - with parts of the combustion chamber and exhaust passage `~ being shown broken away to show other parts in detail;
Fig. 2 is a cross-sectional end view of the inlet end of the incinerator taken along lines 2-2 of Fig. l;
.::
Fig. 3 is a cross-sectional view of the exhaust end of the lncinera,tor, taken along lines 3-3 of Fig. l;
Fig. 4 is a cross-sectional view of the combustion ~t'' 10 chamber, taken along lines 4-4 of Fig. l;
,;.
Fig. 5 is a water flow diagram for a double pass cooling arrangement for the auger tube; and ~; Fig. 6 is a water flow diagram for a single pass cooling : .
arrangement for the auger tube used for steam generation.
,;
,~f',"' Referring now to the drawings, Figs. 1-3 show a hori-;;" zontally disposed stationary cylindrical combustion chamber 10 ., ~ ~ having an opening 12 in the inlet section 14 through which ' r~ .:
combustible refuse is fed from a feed hopper 16. The outlet ~; section 18 has an upward-extending passage 20 for exhaust gases f 20 and a downward extending section defining an ash receptable 22 which is filled with water to a predetermined level 24.
. :.' .
Extending the length of the combustion chamber is a rotatable ., . - .
auger 26 having a tubular axis 28 supported at the inlet end ~ ~ 14 by bearing 30 mounted to the front wall 32 and at the outlet .,.:~ .
end 18 by another bearing 34 mounted to the rear wall 36, and ':.,`, ,~ -7-.'., `;
''' 107~Z6(~
~ ~ .
* driven by an hydraulic motor 38. The spiral flight 40 of . the auger 26 extends from the front wall 32 to the ash recep-. tacle 22, so that when the auger 26 is rotated, the auger flight 40 will convey combustible refuse entering from the ..,.. ~
feed hopper 16 through the combustion chamber 10, and deliver the solid residue to the ash receptacle 22. As can be seen in Fig. 1, the pitch of the auger flight 40 is greatest at the inlet section 14, and becomes gradually less toward the outlet section 18, to compensate for the reduction in volume of the ~;' 10 refuse which takes place during combustion. The tubular axis 28 is positioned off center of the ;l~is of the combustion .... .
.. chamber 10 so that there is minimum clearance between the , .I outer edge 42 of the auger flight 40, to assure movement of ^,~. essentially all of the refuse through the combustion chamber 10 .
~s shown in Fig. 1, the auger flight 40 is comprised of .:^ individual segments which are joined together and concentrically ." spaced from the tubular auger shaft 28 by a plurality of :~ .
support members 44, so that an open annular space 46 is formed 20 between the inner edge 48 of the auger flight 40 and the auger shaft 28. This open space 46 allows air to freely move upward through the combustion chamber 10 as well as along the auger shaft 28 to the outlet section 18. Different materials ,, , ~ having different heat resistant characteristics can be used in forming these sections of the auger flight 40. For example, in the inlet portion, where there is little heat, carbon steel could be used, while stainless steel or a refractory "',' '';
. .
' ` -~ 1078Z.60 .' , alloy could be used in the rest of the combustion chamber 10.
The tubular auger shaft 28 is water cooled and the advantages of this type of construction will be now described.
:
Fig. 1 shows an incoming water pipe 50 concentrically mounted within the tubular auger shaft 28 and connected to a source of cooling water 52. Water flows through this water pipe 50 the length of the combustion chamher 10, then reverses dir-ection by reason of the baffle 54 and flows back and out the same end of the shaft 28 through the water outlet pipe 56.
This water outlet pipe 56 connects to an inlet 58 of a heat ' exchanger 60 disposed in the exhaust gas passage 20, as shown in the water flow diagram of Fig. 5. After being further heated in this heat exchanger 60, the hot water is removed for use or storage elsewhere through a hot water pipe 62.
,:
,~ Fig. 6 shows an alternate cooling water arrangement .~
that can be used where a source of steam is desired. In this '~ alternate arrangement, cool water first enters the heat , , - exchanger 60 through the inlet 58, flows out of the heat exchanger 60 through outlet pipe 62 which is connected to the : 20 end of the tubular auger shaft 28 at the end of the incinerator.
In this arrangement, the inlet pipe 50 and the baffle or blocking partition 54 are omitted. Steam is generated from . . .
the hot water entering the tubular auger shaft 28, and is drawn off at a steam outlet 64 on the exhaust end of the shaft 28, . ., ' .
which is connected to an inlet 66 of a steam superheater coil 68 disposed in the exhaust gas passage 20 between the exhaust end of the combustion chamber 10 and the heat exchanger ';' .,:' ; _9_ ~ , .- :
` -~ 1078Z60 :`
60. The dry steam flows from the superheater coil 68 through an outlet 70 for use elsewhere.
Combustion air is supplied to the combustion chamber 10 .,~ by a fresh air inlet blower 72 driven by a hydraulic motor , ~ .
~; 74, through a hot air manifold 76 disposed within and extends longitudinally along the top of the combustion chamber 10.
This hot air manifold is formed of heat resistant metal to ~orm a passage shaped in cross-section as an annular segment . . .
'~ to conform to the inner wall 78 of the combustion chamber 10, ,, . ~ .
with an open end at the exhaust end of the combustion chamber ~, 10 to receive air from the fresh air inlet blower 72 and a closed end at the inlet end of the combustion chamber 10.
,:
The bottom of the hot air manifold 76 is uninsulated from the ' combustion chamber 10 so that the air flowing in the manifold ,..
76 can be pre-heated before entering the combustion chamber 10. A first plurality of hot air pipes 80 extends at uni-. ' .
form lntervals from both sides of the hot air manifold 76 through the refractory inner wall 78, around the combustion : ':
~` chamber to randomly spaced openings 82 in the lower portion '~ 20 of the combustion chamber 10, which direct the air radially inward and ~pward through the combusticn chamber. A second plurality of short hot air pipes 84 extend along at uniform ; intervals from both sides of the hot air manifold 76 to direct air tangentially along the top sides of the combustion chamber 10.
. . .
....... .
. --10--. .~, ., .
.~. , .
.. ,~
'', ' . .
-- 107826(~
Turning again to Fig. 1 it will be noted that there is shown a curved portion 86 of the exhaust gas passa~e 20 in which a plurality of inwardly projecting baffle plates 88 are disposed on the inside of the outermost curved wall to serve as preliminary dust collector traps, to trap a portion of the solid particulate matter in the exhaust gas and allow it to fall into the ash receptacle.
The solid particulate matter which falls into the ash receptacle 22 is cooled by the water therein, and then removed ;.,:~ : .
by a rotatable auger 90 which extends downward into the ash receptacle 22, and driven by a motor 92, as shown in Fig. 3.
This ash receptacle 22 has a sloping end wall and a semi-circular sloping bottom 94 concentric to and in close prOximity with the ash removal auger 90, so that essentially all solid particulate matter which enters the ash receptacle is directed ; to the ash removal auger 90.
Solid particulate matter is also removed from the exhaust gases in a dust precipitator 96 disposed near the outlet end ~ of the exhaust gas passage 20.
`~. 20 Also, as shown in Fig. 2, an exhaust gas blower 98 ., .
driven by a hydraulic motor 100 directs a portion of the ~^.......... exhaust gas which leaves the dust precipitator 96 to a plural-ity of inlets 102 in the feed hopper 16 forming an air curtain 104, so that the air pressure of the air curtain 104 is ,~ .
~ approximately equal to the air pressure of the combustion air . .
in the combustion chamber 10. This prevents the backward flow of exhaust gases and smoke from the combustion chamber :: -:
:.; 10. Also, this exhaust gas preheats the incoming combustible ;; --11--' ' ;
. . .
., - -~` 1078Z~;0 . ~
,', ~i refuse.
; A directional air pressure sensor 106, (Fig. 1) disposed :.
; within the feed hopper 12, senses a backward flow of com-bustion air and increases the speed of the hydraulic motor 100 for the exhaust gas blower 98 by a control means in the control panel 108.
~' A temperature sensor 110, disposed on the inner wall 78 of the combustion chamber 10 near the inlet to the combus-. .
;. tion chamber 10 is connected to a control means in the control .,;: .
" 10 panel 108 to regulate the speed of the hydraulic motor 74 driving the fresh air inlet blower 72 proportional to the temperature sensed by sensor 110, to assure that the air which :
enters the inlet end of the combustion chamber 10 is suf-ficiently pre-heated.
In a similar manner, a temperature sensor 112, disposed on the inner wall 78 of the combustion chamber 10 near the exhaust end of the combustion chamher 10 is connectea to a control means in the control panel 108 to regulate the speed of the hydraulic motor 38 for the auyer 26 in dependence on the exhaust end combustion chamber temperature, to assure com-plete combustion and reduce the smoke emission from the ~;, combustion cha~ber 10.
,.,."~
; There is best shown in Fig. 2, two oil fired ignitors 114 which are disposed in the inner wall 78 of the combustion ,~; chamber 10 near the inlet section 14 to initiate combustion of the refuse on initial start up of the incinerator. Also, ''"
':.
`;'''' . . .
.
a movable plate 116, vertically disposed on a side of the exhaust gas passage 20 at the exhaust end of the combustion . .~ .
;
:. chamber 10, can be lowered during the start up period to ,:.
partially block passage of exhaust gases from the combustion chamber 10, thus retaining heat in the combustion chamber 10 and thereby reducing the start up time.
, , .
.'` .
: ~ .
,,~, ~ .
.;;~ , , .
. .
,,.` ' .
....
" ' ' !
'~"1~ , '.
''."
~.. . .
' , ~' `'`, ' .
. ...................................................................... .
~ ~1 .!, ~
~;
,.; .
,. .
: '' .
.'.'.
': :~
:,.
. ',:, , ` .
':
:.,.
~, . .
,. -13-,,;
j: . .
";;
. .
,,:.
, '':,` .- . ~
,; ., .
:, . .
Claims
1. An incinerator for burning combustible refuse which comprises:
a horizontally disposed stationary cylindrical combustion chamber means having an inlet end for receiving refuse and an outlet end for discharging residue and exhaust gases;
ignition means adjacent said inlet end for igniting said refuse;
screw conveyor means extending through the length of said chamber means for moving refuse at a decreasing rate from the inlet end to the outlet end of said chamber means as the volume of refuse is reduced by combustion, to effect better combustion of particulate smoke at the outlet end of said chamber means, said screw conveyor means including a rotatable auger having a longitudinal axis and a spiral flight having a larger pitch at the inlet end of said chamber means and a smaller pitch at the outlet end of said chamber means; and air supply means for supplying combustion air to said chamber means.
a horizontally disposed stationary cylindrical combustion chamber means having an inlet end for receiving refuse and an outlet end for discharging residue and exhaust gases;
ignition means adjacent said inlet end for igniting said refuse;
screw conveyor means extending through the length of said chamber means for moving refuse at a decreasing rate from the inlet end to the outlet end of said chamber means as the volume of refuse is reduced by combustion, to effect better combustion of particulate smoke at the outlet end of said chamber means, said screw conveyor means including a rotatable auger having a longitudinal axis and a spiral flight having a larger pitch at the inlet end of said chamber means and a smaller pitch at the outlet end of said chamber means; and air supply means for supplying combustion air to said chamber means.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CA334,073A CA1078260A (en) | 1977-02-28 | 1979-08-20 | Incinerator for burning combustible refuse |
Applications Claiming Priority (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CA272,765A CA1065195A (en) | 1977-02-28 | 1977-02-28 | Incinerator for combustible refuse |
| CA334,073A CA1078260A (en) | 1977-02-28 | 1979-08-20 | Incinerator for burning combustible refuse |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CA1078260A true CA1078260A (en) | 1980-05-27 |
Family
ID=25668464
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CA334,073A Expired CA1078260A (en) | 1977-02-28 | 1979-08-20 | Incinerator for burning combustible refuse |
Country Status (1)
| Country | Link |
|---|---|
| CA (1) | CA1078260A (en) |
-
1979
- 1979-08-20 CA CA334,073A patent/CA1078260A/en not_active Expired
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| US4009667A (en) | Incinerator for combustible refuse | |
| US4474117A (en) | Boiler using a solid granulated fuel | |
| US4479481A (en) | Wood fuel heating apparatus and combustion process | |
| US3961587A (en) | Combustion equipment in which humid combustible excreta and disposed materials such as livestock excreta, paper sludge can be burnt spontaneously | |
| US4586442A (en) | Gasifier method and apparatus | |
| CA1078260A (en) | Incinerator for burning combustible refuse | |
| WO1988002090A1 (en) | Installation for conductive drying of bulk materials | |
| US2554092A (en) | Apparatus for heating a fluid by means of solid fuel | |
| US1996585A (en) | Incinerator | |
| CA1065195A (en) | Incinerator for combustible refuse | |
| BE1006321A6 (en) | Device for burning waste. | |
| EP0334846A1 (en) | AIR REGULATION SUPPLYING AN INCINERATOR. | |
| RU2133409C1 (en) | Wood waste incinerator | |
| US4318355A (en) | Burner structure for particulate fuels | |
| CN217004419U (en) | Multi-fuel energy-saving steam generator | |
| US4572155A (en) | Convergent flow stove | |
| SU1177623A1 (en) | Plant for thermal processing of solid materials | |
| US4457494A (en) | Metal melting furnace | |
| US4295822A (en) | Producer gas fueled burner system and drying apparatus | |
| US1968581A (en) | Combined fluid fuel burning heater and incinerator | |
| RU218994U1 (en) | Organic waste destruction device | |
| US4653465A (en) | Heater | |
| KR102922211B1 (en) | Livestock manure pellet stove with two-stage combustion chamber | |
| US811089A (en) | Hot-air heating system. | |
| KR102880234B1 (en) | Dung Pellet Stove |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| MKEX | Expiry |