CA2041855C - Incinerator and incinerating method employing the same - Google Patents
Incinerator and incinerating method employing the sameInfo
- Publication number
- CA2041855C CA2041855C CA002041855A CA2041855A CA2041855C CA 2041855 C CA2041855 C CA 2041855C CA 002041855 A CA002041855 A CA 002041855A CA 2041855 A CA2041855 A CA 2041855A CA 2041855 C CA2041855 C CA 2041855C
- Authority
- CA
- Canada
- Prior art keywords
- refuse
- furnace
- ashes
- incinerator according
- discharge
- 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 - Fee Related
Links
- 238000000034 method Methods 0.000 title claims description 10
- 239000002956 ash Substances 0.000 claims abstract description 78
- 238000002485 combustion reaction Methods 0.000 claims abstract description 39
- 235000002918 Fraxinus excelsior Nutrition 0.000 claims abstract description 38
- 239000002440 industrial waste Substances 0.000 claims abstract description 4
- 238000001816 cooling Methods 0.000 claims description 10
- 239000000567 combustion gas Substances 0.000 claims description 9
- 239000007789 gas Substances 0.000 claims description 5
- 230000002441 reversible effect Effects 0.000 claims description 5
- 238000005422 blasting Methods 0.000 claims description 3
- 238000001035 drying Methods 0.000 description 3
- 230000000694 effects Effects 0.000 description 3
- 238000009423 ventilation Methods 0.000 description 3
- 238000010276 construction Methods 0.000 description 2
- 238000002309 gasification Methods 0.000 description 2
- 239000000463 material Substances 0.000 description 2
- 238000012986 modification Methods 0.000 description 2
- 230000004048 modification Effects 0.000 description 2
- 230000035699 permeability Effects 0.000 description 2
- 229920003023 plastic Polymers 0.000 description 2
- 239000004033 plastic Substances 0.000 description 2
- 230000001954 sterilising effect Effects 0.000 description 2
- 238000004659 sterilization and disinfection Methods 0.000 description 2
- 230000002411 adverse Effects 0.000 description 1
- 230000001174 ascending effect Effects 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 238000000354 decomposition reaction Methods 0.000 description 1
- 230000003247 decreasing effect Effects 0.000 description 1
- 150000002013 dioxins Chemical group 0.000 description 1
- 239000002906 medical waste Substances 0.000 description 1
- 238000002844 melting Methods 0.000 description 1
- 239000002184 metal Substances 0.000 description 1
- 229910052751 metal Inorganic materials 0.000 description 1
- 150000002739 metals Chemical class 0.000 description 1
- 230000000717 retained effect Effects 0.000 description 1
- 230000035939 shock Effects 0.000 description 1
Classifications
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23G—CREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
- F23G5/00—Incineration of waste; Incinerator constructions; Details, accessories or control therefor
Landscapes
- Engineering & Computer Science (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Gasification And Melting Of Waste (AREA)
- Incineration Of Waste (AREA)
Abstract
An incinerator for combustion of general refuse and industrial wastes having a pair of ash discharge plates and a pair of refuse supporting plates. The ash discharge plates are disposed at the bottom of a furnace in such a manner that it can be freely opened and closed for timely discharge of ashes that accumulate on the bottom. The refuse supporting plates are disposed at a lower level of the furnace in such a manner that it can be freely displaced in a horizontal direction out of and into the furnace projecting into an upper layer of the piled up ashes at the time of discharge of ashes by the ash discharge plates to support the refuse and ashes disposed thereabove.
Description
- 1- 2Q4185~
INCINERATOR AND INCINERATING METHOD EMPLOYING THE SAME
BACKGRO~ND OF THE INVENTION
l. Field of the Invention The present invention relates to an incinerator for combustion of general refuse and industrial wastes, and an incinerating method employing the same.
INCINERATOR AND INCINERATING METHOD EMPLOYING THE SAME
BACKGRO~ND OF THE INVENTION
l. Field of the Invention The present invention relates to an incinerator for combustion of general refuse and industrial wastes, and an incinerating method employing the same.
2. Description of the Prior Art Heretofore proposed is a vertical incinerator having a plurality of grates dividing a furnace into a plurality of stages in such a manner that said grates can be freely opened and closed, whereby the refuse charged from the top of the furnace piles up on the grate in the first stage in a sufficient thickness thereon and is then transferred successively to the grate in the succeeding stage or stages while it is burned until it has been finally turned to ashes for discharge from the bottom of the furnace.
However, the refuse generally includes hardly combustible materials such as rich in moisture and air-impermeable lamps or hardly crushable masses, so that the combustion may not be completed in the upper combustion zone but continue in the lower combustion zone or the plastics melt and drip down, and then ignite in the lower zone of the ~5 furnace. For these reasons, the grates supporting the refuse in the upper combustion zone are exposed to intense heat from the reverse surfaces and cannot be sufficiently cooled by blasting cold air against the grates, with the result that the grates tend to be thermally strained or damaged.
Furthermore, the ventilation holes in the grates may be ~`
plugged with ashes and foreign matter to interfere with the free passage of combustion gases and combustion air or clinkers may be melted and stuck to the ventilation holes to impede the opening and closing of the grates.
SUMMARY OF THE INVENTION
The present invention has been accomplished for overcoming the above-mentioned disadvantages of the conventional vertical incinerator. It is, therefore, an object of the invention to provide an incinerator and an incinerating method employing the same, wherein the layer of ashes accumulated in the lower zone of a furnace is utilized as an equivalent of the grate to dispense with the grate and, thereby, simplify the equipment and insure effective utilization of combustion energy without the risk of burning out and thermal straining of the parts and the consequent troubles, thus effecting savings in running cost.
It is another object of the invention to provide an incinerator and an incinerating method employing the same, wherein both the refuse supporting means and the ash discharge means are simplified in construction to preclude insufficient operation due to intricate structure of the equipment.
It is a further object of the invention to provide an incinerator and an incinerating method employing the same, wherein refuse supporting means project into a furnace so as to effect breaking of clinker masses which tend to form on the refuse supporting means in the incineration of high calory refuse, thereby insuring complete combustion and an increased ease of discharge of the ashes.
20~ 1 85~
However, the refuse generally includes hardly combustible materials such as rich in moisture and air-impermeable lamps or hardly crushable masses, so that the combustion may not be completed in the upper combustion zone but continue in the lower combustion zone or the plastics melt and drip down, and then ignite in the lower zone of the ~5 furnace. For these reasons, the grates supporting the refuse in the upper combustion zone are exposed to intense heat from the reverse surfaces and cannot be sufficiently cooled by blasting cold air against the grates, with the result that the grates tend to be thermally strained or damaged.
Furthermore, the ventilation holes in the grates may be ~`
plugged with ashes and foreign matter to interfere with the free passage of combustion gases and combustion air or clinkers may be melted and stuck to the ventilation holes to impede the opening and closing of the grates.
SUMMARY OF THE INVENTION
The present invention has been accomplished for overcoming the above-mentioned disadvantages of the conventional vertical incinerator. It is, therefore, an object of the invention to provide an incinerator and an incinerating method employing the same, wherein the layer of ashes accumulated in the lower zone of a furnace is utilized as an equivalent of the grate to dispense with the grate and, thereby, simplify the equipment and insure effective utilization of combustion energy without the risk of burning out and thermal straining of the parts and the consequent troubles, thus effecting savings in running cost.
It is another object of the invention to provide an incinerator and an incinerating method employing the same, wherein both the refuse supporting means and the ash discharge means are simplified in construction to preclude insufficient operation due to intricate structure of the equipment.
It is a further object of the invention to provide an incinerator and an incinerating method employing the same, wherein refuse supporting means project into a furnace so as to effect breaking of clinker masses which tend to form on the refuse supporting means in the incineration of high calory refuse, thereby insuring complete combustion and an increased ease of discharge of the ashes.
20~ 1 85~
The above and further objects, features and advantages of the invention will more fully appear from the following description with reference to the accompanying drawings. It is to be expressly understood, however, that the drawings are for purpose of illustration only and are not intended as a definition of the limits of the invention.
BRIFF DESCRIPTION OF THE DRAWINGS
Fig. 1 is a schematic longitudinal section view showing the construction of an incinerator according to the invention;
Figs. 2 and 3 each shows an example of the refuse supporting means; Fig. 2 is a longitudinal sectional elevation view showing the refuse supporting means in retreated position and Fig. 3 is a longitudinal sectional elevation view showing the same swung into the furnace;
Fig. 4 is a perspective view showing another example of a refuse supporting means, which is in the form of a grate;
and Fig. 5 is a sectional view showing another example of an ash discharge means, which is an inclined reversible grate.
DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS
Fig. 1 is a schematic view of the incinerator according to the invention.
In Fig. 1, the reference numeral 1 indicates a hopper.
The refuse storaged in a refuse pit (not shown) is mixed well -until it is crumbled to a certain extent and, then, charged into this hopper l by means of crane (not shown). The hopper l communicates with a refuse feeding port 3l installed to an upper position of a furnace 3 through a feeder 2. The refuse charged into the hopper l is fed into the furnace 3 by the feeder 2 at a predetermined rate.
The furnace 3 is equipped with a pair of refuse supporting plates 4, 4 which constitute a refuse supporting means, and a pair of ash discharge plates 5, 5 which constitute an ash discharge means, in an upper position and a lower position, respectively.
The refuse supporting plates 4,4 are displaceably installed within the furnace body 3; that is to say each is normally located in the retreated position away from the furnace 3 as illustrated. However, these plates 4,4 are operated to project into an upper part of a layer of ashes l54 in the furnace 3 as indicated by a dot-dash line only at the time when the ash discharge plates 5,5 are opened to discharge the ashes, thus supporting the refuse and ashes located above.
A pair of compartments 6,6 for accommodating the refuse supporting plates 4, 4 drawn away from the furnace 3 are located on both sides of the furnace 3 at the level where the plates 4, 4 are disposed. These compartments 6, 6 are supplied with cooling air 7l from a normal temperature air source 7. This cooling air 7l blows out into the furnace 3 from clearances 8, 8 formed between the furnace 3 and the respective compartments 6, 6 to cool the refuse supporting plates 4, 4 and, at the same time, prevent entry of ashes into the compartments 6, 6 through the clearances 8, 8.
2 0 A l 8 ~ ~
The ash discharge plates 5, 5 are each disposed rotatablely through the angle from the horizontal position to the vertical position indicated by a dot-dash line to open and close the ash discharge port at the bottom of the furnace 3. The refuse supporting plates 4, 4 then support the refuse and ashes above the upper part of the layer of ashes 154 in the lower zone of the furnace 3. Thereafter, the ash discharge plates 5, 5 are swung down to discharge the ashes into an ash transport means 9 disposed below the furnace 3.
Thus, said refuse supporting plates 4, 4 are provided to assist in smooth discharge of ashes by said ash discharge plates 5, 5.
ht its upper, intermediate and low levels, the furnace 3 is supplied with combustion air 101, 102 and 103t all of adjusted temperature, through dampers 111, 112 and 113 respectively. These combustion air are adjusted at the optimum temperature suited for the refuse character.
Disposed on the side opposite to the refuse feeding port 31 of the furnace 3 is an ignition burner 12 which is used for igniting the refuse at the start of operation and assisting in combustion during temperature drop in the furnace 3. Disposed at top of the furnace 3 is a gas exhaust port 13 for exitof combustion gases.
The incinerating method employing the above incinerator is now described~
In normal operation, the interior of the furnace 3 is divided, in correspondence with the combusting condition of the refuse, into a flame layer 151, a refuse layer 152, a combustion layer 153 and an ash layer 154 from the top to the bottom First, the refuse charged in the hopper 1 is fed, at a predetermined rate, into the furnace 3 by the feeder 2 through the refuse feeding port 31. At the beginning of operation, the refuse are piled up on the ash layer 154 in the bottom zone of the furnace 3 and is ignited by the ignition burner 12. The refuse then starts burning with the aid of combustion air 101, 102 and the portion of refuse which is more easily combustible is turned to ashes. The ashes are accumulated together with the hardly combustible portion of the refuse and are charged to said combustion layer 153, retaining fire seeds.
As the refuse is fed by the feeder 2 in this condition, the refuse are piled up to the refuse layer 152, gets ignited by the heat from the combustion layer 153 and the combustion air 111 and the combustion then spreads throughout the refuse layer 152 to place the furnace into a normal operating condition.
In this combustion state, the combustion gases produced in the combustion layer 153 and the lower part of the refuse layer 152 ascend through the refuse layer 152. In this prosess of ascent, the hot combustion gases promote ignition and gasification of the refuse in the upper layer and dry the raw refuse.
Then, the hot combustion gases reaching up to the flame layer 151 is recombusted by secondary air 72 from a normal temperature air source 7 and exhausted from the exhaust gas outlet 13 to the next process. The radiant heat produced by this combustion effects preliminary drying of the refuse in the refuse layer 152 and promotes burning of the paper and plastics with low ignition points to grow to fire seeds.
In this manner, the refuse descended in sequence is combusted in the refuse layer 152 and the unburnt combustibles remaining together with hardly combustible materials are completely combusted into ashes in the combustion layer 153 and retained in the ash layer 154.
In the ash layer 154, the combustion air 103 helps to complete the final burning of the unburnt combustibles remaining in the upper layer of the ash layer 154 and, at the same time, cools the ashes and metals having a low-melting point from below.
In this process, the air and hot combustion gases ascending from the ash layer 154 flow through the combustion layer 153 and refuse layer 152 to facilitate combustion of the refuse at the upper layer and further accelerate the drying, ignition and gasification of raw refuse.
Thus, the ash layer 154 plays the duty of the conventional fire grate.
Upon completion of this combustion of ashes, the refuse supporting plates 4, 4 are caused to project into the upper position of the ash layer 154 within the furnace 3 to support the refuse and ashes in the refuse layer 152, combustion layer 153 and ash layer 154 which are disposed above. At this time of projection, the combustion of refuse has already been completed at the level of the refuse supporting plates 4, 4.
Therefore, the ref~se supporting plates 4, 4 need not be provided with the ventilation holes which are required for the conventional fire grate. Moreover, because of low resistance by the refuse, the refuse supporting plates 4, 4 are allowed to project smoothly.
After the refuse supporting plates 4, 4 have thus been caused to project, the ash discharge plates 5, 5 are swung down to let the ashes below the refuse supporting plates 4, 4 fall down into the ash transport means 9.
After discharge of the ashes, the ash discharge plates 5, 5 are returned into the upper position and the refuse supporting plates 4, 4 are caused to retreat away from the furnace 3 to let the remaining ashes and the incinerator residues in the combustion layer 153 on the refuse supporting plates 4, 4 fall down onto the furnace bottom and the refuse layer 152 fall down.
The shock of this fall not only improves the air permeability in the ash layer 154 but disintegrates the unburnt mases in the combustion layer 153 and refuse layer 152 so that the whole layer becomes more permeable to air.
15Therefore, as the high-temperature combustion air 102, 103 is dupplied, the unburnt combustibles in the ashes is easily glowed by the remaining fire seeds.
The feeding pressure of the combustion air 102, 103 need not be high because of the improved air permeability of 20the combustion layer 153 and ash layer 154, and the resulting improved drying efficiency helps reduce the excess air ratio.
The incinerator thus constructed not only insures almost uniform combustion of refuse at high temperature but, as aforesaid, helps reduce the excess air ratio, with the result that the volume of exhaust gas is decreased to prolong the residence time of combustion gases. This result is effective in sterilization and decomposition of dioxins. The sterilization effect, in particular, is beneficial for the incineration of medical wastes.
30Furthermore, the time of projection of the refuse supporting plates 4, 4 into the furnace 3 when the temperature of the ash layer 154 has dropped and is also short in duration. Therefore, there is no risk of thermal strain and burning out due to high temperature. Moreover, the ash discharge plates 5, 5 are not adversely affected by high temperature, for the upper surfaces of the plates 5, 5 are in contact with the ashes cooled by the combustion air 103 while their lower surfaces are cooled by the atmospheric air.
It should be understood that the refuse supporting plates 4, 4 need not be those described in the foregoing embodiment but may be those each rotatable about a pivot 41 as illustrated in Figs. 2 and 3. Moreover, the refuse supporting plates 4, 4 may also have a grate-like structure as illustrated in Fig. 4.
The ash discharge plates 5, 5 need not be those described above in the foregoing embodiment, either, but may be an inclined reversible grate rotatable about a pivot 51 as illustrated in Fig. 5.
While there has been described what is at present considered to be preferred embodiments of the invention, it will be understood that various modifications may be made therein, and it is intended to cover in the appended claims all such modifications as fall within the true spirit and scope of the invention.
BRIFF DESCRIPTION OF THE DRAWINGS
Fig. 1 is a schematic longitudinal section view showing the construction of an incinerator according to the invention;
Figs. 2 and 3 each shows an example of the refuse supporting means; Fig. 2 is a longitudinal sectional elevation view showing the refuse supporting means in retreated position and Fig. 3 is a longitudinal sectional elevation view showing the same swung into the furnace;
Fig. 4 is a perspective view showing another example of a refuse supporting means, which is in the form of a grate;
and Fig. 5 is a sectional view showing another example of an ash discharge means, which is an inclined reversible grate.
DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS
Fig. 1 is a schematic view of the incinerator according to the invention.
In Fig. 1, the reference numeral 1 indicates a hopper.
The refuse storaged in a refuse pit (not shown) is mixed well -until it is crumbled to a certain extent and, then, charged into this hopper l by means of crane (not shown). The hopper l communicates with a refuse feeding port 3l installed to an upper position of a furnace 3 through a feeder 2. The refuse charged into the hopper l is fed into the furnace 3 by the feeder 2 at a predetermined rate.
The furnace 3 is equipped with a pair of refuse supporting plates 4, 4 which constitute a refuse supporting means, and a pair of ash discharge plates 5, 5 which constitute an ash discharge means, in an upper position and a lower position, respectively.
The refuse supporting plates 4,4 are displaceably installed within the furnace body 3; that is to say each is normally located in the retreated position away from the furnace 3 as illustrated. However, these plates 4,4 are operated to project into an upper part of a layer of ashes l54 in the furnace 3 as indicated by a dot-dash line only at the time when the ash discharge plates 5,5 are opened to discharge the ashes, thus supporting the refuse and ashes located above.
A pair of compartments 6,6 for accommodating the refuse supporting plates 4, 4 drawn away from the furnace 3 are located on both sides of the furnace 3 at the level where the plates 4, 4 are disposed. These compartments 6, 6 are supplied with cooling air 7l from a normal temperature air source 7. This cooling air 7l blows out into the furnace 3 from clearances 8, 8 formed between the furnace 3 and the respective compartments 6, 6 to cool the refuse supporting plates 4, 4 and, at the same time, prevent entry of ashes into the compartments 6, 6 through the clearances 8, 8.
2 0 A l 8 ~ ~
The ash discharge plates 5, 5 are each disposed rotatablely through the angle from the horizontal position to the vertical position indicated by a dot-dash line to open and close the ash discharge port at the bottom of the furnace 3. The refuse supporting plates 4, 4 then support the refuse and ashes above the upper part of the layer of ashes 154 in the lower zone of the furnace 3. Thereafter, the ash discharge plates 5, 5 are swung down to discharge the ashes into an ash transport means 9 disposed below the furnace 3.
Thus, said refuse supporting plates 4, 4 are provided to assist in smooth discharge of ashes by said ash discharge plates 5, 5.
ht its upper, intermediate and low levels, the furnace 3 is supplied with combustion air 101, 102 and 103t all of adjusted temperature, through dampers 111, 112 and 113 respectively. These combustion air are adjusted at the optimum temperature suited for the refuse character.
Disposed on the side opposite to the refuse feeding port 31 of the furnace 3 is an ignition burner 12 which is used for igniting the refuse at the start of operation and assisting in combustion during temperature drop in the furnace 3. Disposed at top of the furnace 3 is a gas exhaust port 13 for exitof combustion gases.
The incinerating method employing the above incinerator is now described~
In normal operation, the interior of the furnace 3 is divided, in correspondence with the combusting condition of the refuse, into a flame layer 151, a refuse layer 152, a combustion layer 153 and an ash layer 154 from the top to the bottom First, the refuse charged in the hopper 1 is fed, at a predetermined rate, into the furnace 3 by the feeder 2 through the refuse feeding port 31. At the beginning of operation, the refuse are piled up on the ash layer 154 in the bottom zone of the furnace 3 and is ignited by the ignition burner 12. The refuse then starts burning with the aid of combustion air 101, 102 and the portion of refuse which is more easily combustible is turned to ashes. The ashes are accumulated together with the hardly combustible portion of the refuse and are charged to said combustion layer 153, retaining fire seeds.
As the refuse is fed by the feeder 2 in this condition, the refuse are piled up to the refuse layer 152, gets ignited by the heat from the combustion layer 153 and the combustion air 111 and the combustion then spreads throughout the refuse layer 152 to place the furnace into a normal operating condition.
In this combustion state, the combustion gases produced in the combustion layer 153 and the lower part of the refuse layer 152 ascend through the refuse layer 152. In this prosess of ascent, the hot combustion gases promote ignition and gasification of the refuse in the upper layer and dry the raw refuse.
Then, the hot combustion gases reaching up to the flame layer 151 is recombusted by secondary air 72 from a normal temperature air source 7 and exhausted from the exhaust gas outlet 13 to the next process. The radiant heat produced by this combustion effects preliminary drying of the refuse in the refuse layer 152 and promotes burning of the paper and plastics with low ignition points to grow to fire seeds.
In this manner, the refuse descended in sequence is combusted in the refuse layer 152 and the unburnt combustibles remaining together with hardly combustible materials are completely combusted into ashes in the combustion layer 153 and retained in the ash layer 154.
In the ash layer 154, the combustion air 103 helps to complete the final burning of the unburnt combustibles remaining in the upper layer of the ash layer 154 and, at the same time, cools the ashes and metals having a low-melting point from below.
In this process, the air and hot combustion gases ascending from the ash layer 154 flow through the combustion layer 153 and refuse layer 152 to facilitate combustion of the refuse at the upper layer and further accelerate the drying, ignition and gasification of raw refuse.
Thus, the ash layer 154 plays the duty of the conventional fire grate.
Upon completion of this combustion of ashes, the refuse supporting plates 4, 4 are caused to project into the upper position of the ash layer 154 within the furnace 3 to support the refuse and ashes in the refuse layer 152, combustion layer 153 and ash layer 154 which are disposed above. At this time of projection, the combustion of refuse has already been completed at the level of the refuse supporting plates 4, 4.
Therefore, the ref~se supporting plates 4, 4 need not be provided with the ventilation holes which are required for the conventional fire grate. Moreover, because of low resistance by the refuse, the refuse supporting plates 4, 4 are allowed to project smoothly.
After the refuse supporting plates 4, 4 have thus been caused to project, the ash discharge plates 5, 5 are swung down to let the ashes below the refuse supporting plates 4, 4 fall down into the ash transport means 9.
After discharge of the ashes, the ash discharge plates 5, 5 are returned into the upper position and the refuse supporting plates 4, 4 are caused to retreat away from the furnace 3 to let the remaining ashes and the incinerator residues in the combustion layer 153 on the refuse supporting plates 4, 4 fall down onto the furnace bottom and the refuse layer 152 fall down.
The shock of this fall not only improves the air permeability in the ash layer 154 but disintegrates the unburnt mases in the combustion layer 153 and refuse layer 152 so that the whole layer becomes more permeable to air.
15Therefore, as the high-temperature combustion air 102, 103 is dupplied, the unburnt combustibles in the ashes is easily glowed by the remaining fire seeds.
The feeding pressure of the combustion air 102, 103 need not be high because of the improved air permeability of 20the combustion layer 153 and ash layer 154, and the resulting improved drying efficiency helps reduce the excess air ratio.
The incinerator thus constructed not only insures almost uniform combustion of refuse at high temperature but, as aforesaid, helps reduce the excess air ratio, with the result that the volume of exhaust gas is decreased to prolong the residence time of combustion gases. This result is effective in sterilization and decomposition of dioxins. The sterilization effect, in particular, is beneficial for the incineration of medical wastes.
30Furthermore, the time of projection of the refuse supporting plates 4, 4 into the furnace 3 when the temperature of the ash layer 154 has dropped and is also short in duration. Therefore, there is no risk of thermal strain and burning out due to high temperature. Moreover, the ash discharge plates 5, 5 are not adversely affected by high temperature, for the upper surfaces of the plates 5, 5 are in contact with the ashes cooled by the combustion air 103 while their lower surfaces are cooled by the atmospheric air.
It should be understood that the refuse supporting plates 4, 4 need not be those described in the foregoing embodiment but may be those each rotatable about a pivot 41 as illustrated in Figs. 2 and 3. Moreover, the refuse supporting plates 4, 4 may also have a grate-like structure as illustrated in Fig. 4.
The ash discharge plates 5, 5 need not be those described above in the foregoing embodiment, either, but may be an inclined reversible grate rotatable about a pivot 51 as illustrated in Fig. 5.
While there has been described what is at present considered to be preferred embodiments of the invention, it will be understood that various modifications may be made therein, and it is intended to cover in the appended claims all such modifications as fall within the true spirit and scope of the invention.
Claims (19)
1. An incinerator for combustion of general refuse and industrial wastes comprising;
a furnace having a gas exhaust port at top and an ash discharge port at bottom, a refuse feeder means communicating with said furnace and feeding refuse into an upper zone of said furnace, a discharge means disposed at the bottom of said furnace in such a manner that it can be freely opened and closed for timely discharge of ashes that accumulate on the bottom, a refuse supporting means disposed at a lower level of said furnace in such a manner that it can be freely displaced in a horizontal direction out of and into said furnace projecting into an upper layer of said piled up ashes at the time of discharge of ashes by said ash discharge means to support the refuse and ashes piled up thereabove, and an air supply means for supplying combustion air into said furnace.
a furnace having a gas exhaust port at top and an ash discharge port at bottom, a refuse feeder means communicating with said furnace and feeding refuse into an upper zone of said furnace, a discharge means disposed at the bottom of said furnace in such a manner that it can be freely opened and closed for timely discharge of ashes that accumulate on the bottom, a refuse supporting means disposed at a lower level of said furnace in such a manner that it can be freely displaced in a horizontal direction out of and into said furnace projecting into an upper layer of said piled up ashes at the time of discharge of ashes by said ash discharge means to support the refuse and ashes piled up thereabove, and an air supply means for supplying combustion air into said furnace.
2. An incinerator for combustion of general refuse and industrial wastes comprising;
a furnace having a gas exhaust port at top and an ash discharge port at bottom, a refuse feeder means communicating with said furnace and feeding refuse into an upper zone of said furnace, a discharge means disposed at the bottom of said furnace in such a manner that it can be freely opened and closed for timely discharge of ashes that accumulate on the bottom, a refuse supporting means disposed in a lower zone of said furnace in such a manner that it can be freely swung into an upper part of an ash layer piled up of said ashes at the time of discharge by said ash discharge means to support the refuse and ashes piled up thereabove, and an air supply means for supplying combustion air into said furnace.
a furnace having a gas exhaust port at top and an ash discharge port at bottom, a refuse feeder means communicating with said furnace and feeding refuse into an upper zone of said furnace, a discharge means disposed at the bottom of said furnace in such a manner that it can be freely opened and closed for timely discharge of ashes that accumulate on the bottom, a refuse supporting means disposed in a lower zone of said furnace in such a manner that it can be freely swung into an upper part of an ash layer piled up of said ashes at the time of discharge by said ash discharge means to support the refuse and ashes piled up thereabove, and an air supply means for supplying combustion air into said furnace.
3. An incinerator according to claim 1 wherein said refuse feeder means comprises a hopper for charging refuse and a feeder adapted to feed the refuse from said hopper into an upper zone of said furnace at a predetermined rate.
4. An incinerator according to claim 2 wherein said refuse feeder means comprises a hopper for charging refuse and a feeder adapted to feed the refuse from said hopper into an upper zone of said furnace at a predetermined rate.
5. An incinerator according to claim 3 which is provided with a refuse supporting plate cooling means for blasting cooling air against said refuse supporting means.
6. An incinerator according to claim 4 which is provided with a refuse supporting plate cooling means for blasting cooling air against said rufuse supporting means.
7. An incinerator according to claim 5 further comprising a compartment for accomodating said refuse supporting means on a side wall of said furnace, said compartment communicating with said refuse supporting plate cooling means so that cooling air may be blasted against the refuse supporting means via said compartment.
8. An incinerator according to claim 6 further comprising a compartment for accomodating said refuse supporting means on a side wall of said furnace, said compartment communicating with said refuse supporting plate cooling means so that cooling air may be blasted against the refuse supporting means via said compartment.
9. An incinerator according to claim 7 further comprising an ignition burner disposed in an opposite side to said refuse feeder means.
10. An incinerator according to claim 8 further comprising an ignition burner disposed in an opposite side to said refuse feeder means.
11. An incinerator according to claim 7 wherein said refuse supporting means consists of a pair of plates capable of closing the furnace in a horizontal direction.
12. An incinerator according to claim 8 wherein said refuse supporting means consists of a pair of plates capable of closing the furnace in a horizontal direction.
13. An incinerator according to claim 7 wherein said refuse supporting means is in the form of a grate.
14. An incinerator according to claim 8 wherein said refuse supporting means is in the form of a grate.
15. An incinerator according to claim 7 which is further provided with means for supplying secondary air at normal temperature for recombustion of combustion gases into an upper zone of said furnace.
16. An incinerator according to claim 8 which is further provided with means for supplying secondary air at normal temperature for recombustion of combustion gases into an upper zone of said furnace.
17. An incinerator according to claim 7 wherein said ash discharge means is an inclined reversible grate.
18. An incinerator according to claim 8 wherein said ash discharge means is an inclined reversible grate.
19. An incinerating method comprising;
a step of feeding refuse from a refuse feeder means into an upper zone of a furnace, a step of combusting the charged refuse and letting the refuse descent under its own weight and form an ash layer in a lower zone of the furnace, a step of causing a refuse supporting means to project into an upper part of said ash layer to support the refuse and ashes located thereabove and opening the bottom of the furnace to discharge the ashes located below the refuse supporting means from the furnace, and a step of closing the bottom of the furnace after discharge of ashes and causing the refuse supporting means to retreat from the furnace to let the refuse and ashes supported by said refuse supporting means fall down into a lower zone of the furnace to form an ash layer.
a step of feeding refuse from a refuse feeder means into an upper zone of a furnace, a step of combusting the charged refuse and letting the refuse descent under its own weight and form an ash layer in a lower zone of the furnace, a step of causing a refuse supporting means to project into an upper part of said ash layer to support the refuse and ashes located thereabove and opening the bottom of the furnace to discharge the ashes located below the refuse supporting means from the furnace, and a step of closing the bottom of the furnace after discharge of ashes and causing the refuse supporting means to retreat from the furnace to let the refuse and ashes supported by said refuse supporting means fall down into a lower zone of the furnace to form an ash layer.
Applications Claiming Priority (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP2286667A JP2603364B2 (en) | 1990-10-23 | 1990-10-23 | Vertical incinerator and its incineration method |
| JP2-286667 | 1990-10-23 |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CA2041855A1 CA2041855A1 (en) | 1992-04-24 |
| CA2041855C true CA2041855C (en) | 1995-10-31 |
Family
ID=17707400
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CA002041855A Expired - Fee Related CA2041855C (en) | 1990-10-23 | 1991-05-06 | Incinerator and incinerating method employing the same |
Country Status (3)
| Country | Link |
|---|---|
| JP (1) | JP2603364B2 (en) |
| KR (1) | KR920008407A (en) |
| CA (1) | CA2041855C (en) |
Families Citing this family (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP3759116B2 (en) | 2003-03-28 | 2006-03-22 | 株式会社プランテック | Vertical waste incinerator for waste incineration and control method thereof |
| US7284550B2 (en) * | 2004-03-17 | 2007-10-23 | Bixby Energy Systems, Inc. | Burn pot for furnace |
| JP4593688B1 (en) | 2010-03-18 | 2010-12-08 | 株式会社プランテック | Method of supplying combustion air in vertical waste incinerator and vertical waste incinerator |
| JP6748697B2 (en) * | 2018-12-19 | 2020-09-02 | 株式会社プランテック | Combustion control method |
Family Cites Families (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS6239130U (en) * | 1985-08-21 | 1987-03-09 |
-
1990
- 1990-10-23 JP JP2286667A patent/JP2603364B2/en not_active Expired - Lifetime
-
1991
- 1991-05-06 KR KR1019910007300A patent/KR920008407A/en not_active Application Discontinuation
- 1991-05-06 CA CA002041855A patent/CA2041855C/en not_active Expired - Fee Related
Also Published As
| Publication number | Publication date |
|---|---|
| JP2603364B2 (en) | 1997-04-23 |
| KR920008407A (en) | 1992-05-28 |
| JPH04158110A (en) | 1992-06-01 |
| CA2041855A1 (en) | 1992-04-24 |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| EEER | Examination request | ||
| MKLA | Lapsed |