JPH0335575B2 - - Google Patents
Info
- Publication number
- JPH0335575B2 JPH0335575B2 JP62197113A JP19711387A JPH0335575B2 JP H0335575 B2 JPH0335575 B2 JP H0335575B2 JP 62197113 A JP62197113 A JP 62197113A JP 19711387 A JP19711387 A JP 19711387A JP H0335575 B2 JPH0335575 B2 JP H0335575B2
- Authority
- JP
- Japan
- Prior art keywords
- incinerator
- grate
- combustion
- waste
- garbage
- 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 - Lifetime
Links
- 239000002699 waste material Substances 0.000 claims description 23
- 238000001816 cooling Methods 0.000 claims description 9
- 239000002440 industrial waste Substances 0.000 claims description 3
- 238000002485 combustion reaction Methods 0.000 description 67
- 239000000428 dust Substances 0.000 description 21
- 239000000567 combustion gas Substances 0.000 description 15
- 239000004576 sand Substances 0.000 description 10
- 239000000463 material Substances 0.000 description 7
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 7
- 238000000034 method Methods 0.000 description 6
- 239000007789 gas Substances 0.000 description 3
- 230000035699 permeability Effects 0.000 description 3
- 239000012809 cooling fluid Substances 0.000 description 2
- 238000007599 discharging Methods 0.000 description 2
- 239000012530 fluid Substances 0.000 description 2
- 238000002309 gasification Methods 0.000 description 2
- 238000003780 insertion Methods 0.000 description 2
- 230000037431 insertion Effects 0.000 description 2
- 238000002844 melting Methods 0.000 description 2
- 230000008018 melting Effects 0.000 description 2
- 238000002203 pretreatment Methods 0.000 description 2
- 239000000654 additive Substances 0.000 description 1
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 1
- 238000007664 blowing Methods 0.000 description 1
- 238000009841 combustion method Methods 0.000 description 1
- 230000006835 compression Effects 0.000 description 1
- 238000007906 compression Methods 0.000 description 1
- 238000013016 damping Methods 0.000 description 1
- 238000001035 drying Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 239000003063 flame retardant Substances 0.000 description 1
- 239000000446 fuel Substances 0.000 description 1
- 238000000265 homogenisation Methods 0.000 description 1
- 238000009434 installation Methods 0.000 description 1
- 239000001301 oxygen Substances 0.000 description 1
- 229910052760 oxygen Inorganic materials 0.000 description 1
- 239000002245 particle Substances 0.000 description 1
- 238000005192 partition Methods 0.000 description 1
- 230000001737 promoting effect Effects 0.000 description 1
- 238000000197 pyrolysis Methods 0.000 description 1
- 230000035939 shock Effects 0.000 description 1
- 238000005979 thermal decomposition reaction Methods 0.000 description 1
Landscapes
- Gasification And Melting Of Waste (AREA)
Description
【発明の詳細な説明】
(産業上の利用分野)
本発明は、一般廃棄物や産業廃棄物などのごみ
を焼却する竪型焼却炉に関する。DETAILED DESCRIPTION OF THE INVENTION (Field of Industrial Application) The present invention relates to a vertical incinerator for incinerating garbage such as general waste and industrial waste.
(従来の技術)
従来、焼却装置としては、一般にストーカ炉が
用いられており、このストーカ炉は、略水平方向
に移動する火格子にごみをのせ、この火格子を移
動させながらごみを焼却するように構成されたも
のである。しかし、このストーカ炉では、前記火
格子を略水平方向に移動させるため、火格子の面
積が広くなり、設備の据付面積が大きくなるとと
もに、燃焼時に発生する燃焼ガスの持つエネルギ
ーを有効に十分利用できていない。(Prior art) Conventionally, a stoker furnace has been generally used as an incinerator. In this stoker furnace, garbage is placed on a grate that moves approximately horizontally, and the garbage is incinerated while moving the grate. It is structured as follows. However, in this stoker furnace, since the grate is moved approximately horizontally, the area of the grate becomes wider, the installation area of the equipment becomes larger, and the energy of the combustion gas generated during combustion is effectively and fully utilized. I haven't been able to do it.
そこで、このような問題を解決するものとし
て、竪型焼却炉をあげることができる。竪型焼却
炉としては、流動床方式のものが主流をしめてお
り、第2図はこの流動床方式の竪型焼却炉の概略
構成を示している。 Therefore, a vertical incinerator can be used as a solution to such problems. The mainstream of vertical incinerators is a fluidized bed type incinerator, and FIG. 2 shows a schematic configuration of this fluidized bed type vertical incinerator.
まず、ごみピツト(図示省略)に貯留されたご
みはクレーン(図示省略)によつてホツパaに投
入され、破砕機あるいは破袋機bで細かく砕かれ
た後、フイーダcによつて焼却炉本体d内に投入
される。焼却炉本体d内の底部には空気分散板e
が設けられており、この空気分散板eの上に高温
の砂fが堆積されている。そして、空気分散板e
の下方から砂fに向けて高温の燃焼用空気gを高
圧で吹き出すことにより、砂fが吹き上げられて
焼却炉本体d内を流動する流動状態になる。よつ
て、この流動状態になされた焼却炉本体d内に細
分化されたごみが投下されると、ごみは流動して
いる高温の砂fによつて瞬時に着火して焼却炉本
体d内の上部フリーボードd1で燃焼する。この燃
焼時に発生する燃焼ガスは焼却炉本体d内の頂部
d2からダストとともに、この頂部d2に連通された
図示しない集塵装置、ガス冷却装置および熱交換
器側に排出される。また、ダストとして排出され
なかつた重い不燃物は砂fとともに下方の不燃物
分離装置hに取り出され、この不燃物分離装置h
で砂fと分離されて外部に排出される。分離され
た砂fは循環装置iによつて再び焼却炉本体d内
に戻される。 First, the garbage stored in the garbage pit (not shown) is loaded into the hopper a by a crane (not shown), crushed into small pieces by a crusher or bag breaker b, and then transferred to the incinerator body by a feeder c. It is thrown into d. There is an air distribution plate e at the bottom of the incinerator body d.
is provided, and hot sand f is deposited on this air distribution plate e. And air distribution plate e
By blowing out high-temperature combustion air g at high pressure toward the sand f from below, the sand f is blown up and becomes a fluid state in which it flows inside the incinerator body d. Therefore, when the fragmented waste is dropped into the incinerator body d which is in a fluidized state, the waste is instantly ignited by the flowing high-temperature sand f and the waste inside the incinerator body d is ignited. Burn on top freeboard d 1 . The combustion gas generated during this combustion is at the top of the incinerator body d.
From d2 , the dust is discharged along with the dust to a dust collector, gas cooling device, and heat exchanger (not shown) that are connected to the top d2 . In addition, heavy incombustibles that have not been discharged as dust are taken out together with sand f to the incombustibles separator h located below.
It is separated from the sand f and discharged outside. The separated sand f is returned to the incinerator main body d by the circulation device i.
(発明が解決しようとする問題点)
しかしながら、上述した流動方式の竪型焼却炉
において、ごみを焼却炉本体内で円滑に燃焼させ
るためには、前処理を行う装置(例えば、ごみを
細かく砕く破砕機、あるいはごみ袋を破つて塊を
ほぐす破袋機)や砂を焼却炉本体内で流動させる
押込送風機等の設備が必要になるとともに、この
押込送風機によつて焼却炉本体内に送り込む燃焼
用空気の圧力を大幅に高くする必要があるため、
電力の消費量が多くなる。また、集塵装置側に燃
焼ガスとともに排出されるダスト量が非常に大量
であるため、集塵装置が大掛りになるとともに、
この大量のダストに起因するガス冷却装置や熱交
換器のトラブルが起こり易くなる。さらに、高圧
の燃焼用空気が焼却炉本体内に圧送されているの
で、焼却炉本体の内圧が正圧になる危険性が高い
ため、ごみ挿入口等のシールが必要になるととも
に、燃焼ガスおよびダストを焼却炉本体内から集
塵装置側に排出するための誘引装置の吸引力を大
きくする考慮が必要になる。その他、砂循環とい
う余分の工程が必要になる。(Problems to be Solved by the Invention) However, in the above-mentioned fluidized vertical incinerator, in order to smoothly burn waste within the incinerator main body, a device for pre-treatment (for example, Equipment such as a crusher (or a bag-breaking machine that tears open garbage bags to loosen clumps) and a forced air blower that moves the sand inside the incinerator are required, and this forced air blower is used to blow the combustion air into the incinerator. Because it is necessary to significantly increase the air pressure,
Power consumption increases. In addition, since the amount of dust discharged together with the combustion gas to the dust collector side is extremely large, the dust collector becomes large-scale and
Troubles with gas cooling devices and heat exchangers are likely to occur due to this large amount of dust. Furthermore, since high-pressure combustion air is forced into the incinerator body, there is a high risk that the internal pressure of the incinerator body will become positive pressure. Consideration must be given to increasing the suction force of the attracting device for discharging dust from the incinerator main body to the dust collector side. Additionally, an extra process called sand circulation is required.
一方、竪型焼却炉には、上記流動方式の他に、
熱分解方式や溶融方式がある。しかしながら、熱
分解方式では、燃焼用空気および燃焼ガスが厚い
ごみ層を通過するためには押込送風機よつて焼却
炉本体内に送り込む燃焼用空気の圧力を高くしな
ければならず、ごみ質の変動によつては焼却炉本
体内が正圧になる危険性があり、流動方式と同様
にごみ挿入口等のシールが必要になる。また、焼
却炉本体内の下部はごみの荷重がもろにかかるた
め、焼却炉本体内の下部に堆積した焼却灰を焼却
炉本体の下方に排出する排出装置に特別の工夫が
必要であり、装置が複雑になる。次に、溶融方式
は、不燃物の高温の溶融状態で排出されるため取
扱が危険である。また、添加剤が必要になるとと
もに電力の消費量が多くなるため、コストが嵩み
経済的でない。 On the other hand, in addition to the above-mentioned fluidized incinerator, vertical incinerators include
There are thermal decomposition methods and melting methods. However, in the pyrolysis method, in order for the combustion air and combustion gas to pass through the thick layer of garbage, the pressure of the combustion air sent into the incinerator body using a forced fan must be increased, resulting in fluctuations in the quality of the garbage. Depending on the type of incinerator, there is a risk of positive pressure building up inside the incinerator, and similar to the flow type method, seals such as the waste insertion port are required. In addition, since the load of garbage is applied to the lower part of the incinerator body, a special device is required to discharge the incinerated ash accumulated at the lower part of the incinerator body to the lower part of the incinerator body. becomes complicated. Secondly, in the melting method, nonflammable materials are discharged in a high-temperature molten state, which is dangerous to handle. Further, since additives are required and power consumption increases, the cost increases and it is not economical.
さらに、特公昭49−17709号公報に記載のもの
に見られるように、焼却炉内の同一平面上に亘つ
て複数に分割された火格子が上下方向に複数段配
設され、同一平面上に位置する各火格子を火格子
傾斜装置により物質支持位置から物質落下位置へ
傾斜させることで、ごみ(燃焼物質)を順次下方
へ落下させるように構成したものが提供されてい
る。 Furthermore, as seen in the one described in Japanese Patent Publication No. 49-17709, a grate divided into multiple parts is arranged vertically in multiple stages on the same plane inside the incinerator. There has been provided a structure in which garbage (combustible material) is caused to sequentially fall downward by tilting each located grate from a material supporting position to a material falling position using a grate tilting device.
しかしながら、上記焼却炉は、燃焼用空気の大
部分は焼却炉の頂部及び底部に配設された空気開
口部付近の火格子群の間を水平方向に通過して2
次燃焼域に達するだけで、一部分が分割された火
格子単品間を上下に流れるに過ぎない。従つて、
中間部のごみは燃焼に必要な酸素の供給が不足
し、燃焼は主として頂部及び底部のごみの表面だ
けで行われることになる。このため、この焼却炉
で完全燃焼させるためには、各火格子に堆積させ
るごみの厚みをできるだけ薄くして空気に触れや
すくして燃焼させ、残りのごみを順次下方に落下
させる多段式燃焼方式が必要である。よつて、こ
のような焼却炉において、各火格子上で発生した
燃焼ガスは、近接する上段の火格子裏面に当た
り、火格子内部を流動する冷却流体で冷やされ
る。このため、燃焼ガスの持つエネルギーを余り
利用することができず燃焼効率が悪く着火、助燃
及び2次燃焼の全段階に亘つて、多数の助燃装置
が必要であり、運転経費の増大を招くと言う問題
があつた。また、同一平面上に位置する各火格子
を同時に傾斜させる火格子傾斜装置が必要であ
り、装置全体の構成が複雑になるため、故障の起
こる虞も高くなる。さらに、この焼却炉において
は、火格子内に冷却用流体を循環させることによ
り火格子の表面温度を制御しているが、火格子上
に堆積するごみ層が薄いため、各火格子上のごみ
の性状により燃焼状態が大きく変化することにな
り、これに伴い火格子の温度も急変する。このた
め、たとえ高圧の水を大量に流して冷却効率を高
めようとしても、部分的に水蒸気が発生するとこ
の水蒸気が水の流動を阻害し、火格子の焼損や熱
歪を招くとともに、高圧水を流す場合には、高圧
による接続部分での破損などの故障が起こる虞も
高くなり補修費用が増大するとともに、全体とし
て安定した運転を継続することが困難であつた。 However, in the above-mentioned incinerator, most of the combustion air passes horizontally between the grate groups near the air openings arranged at the top and bottom of the incinerator.
When it reaches the next combustion zone, it only partially flows up and down between the separate pieces of the grate. Therefore,
The waste in the middle part lacks the supply of oxygen necessary for combustion, and combustion occurs mainly only on the surface of the waste in the top and bottom parts. For this reason, in order to achieve complete combustion in this incinerator, a multi-stage combustion method is used in which the thickness of the garbage deposited on each grate is made as thin as possible so that it can be easily exposed to air, and then the remaining garbage is allowed to fall downward one after another. is necessary. Therefore, in such an incinerator, the combustion gas generated on each grate hits the back surface of the adjacent upper grate and is cooled by the cooling fluid flowing inside the grate. For this reason, it is not possible to utilize much of the energy contained in the combustion gas, resulting in poor combustion efficiency and a large number of auxiliary combustion devices being required for all stages of ignition, auxiliary combustion, and secondary combustion, leading to increased operating costs. I had a problem. Furthermore, a grate tilting device is required to simultaneously tilt each grate located on the same plane, which complicates the overall configuration of the device, increasing the risk of failure. Furthermore, in this incinerator, the surface temperature of the grate is controlled by circulating a cooling fluid within the grate, but since the layer of waste that accumulates on the grate is thin, the waste on each grate is The combustion state changes greatly depending on the properties of the fuel, and the temperature of the grate changes rapidly accordingly. For this reason, even if you try to increase cooling efficiency by flowing a large amount of high-pressure water, if water vapor is generated locally, this water vapor will obstruct the flow of water, causing burnout and thermal distortion of the grate, and the high-pressure water When flowing water, there is a high risk that failures such as damage to the connecting parts due to high pressure will occur, increasing repair costs and making it difficult to maintain stable operation as a whole.
(問題点を解決するための手段)
本発明の竪型焼却炉は、一般廃棄物や産業廃棄
物などのごみを焼却する焼却炉であつて、焼却炉
本体内には、この焼却炉本体内を上下に複数段の
部屋に仕切る複数の火格子が開閉自在に設けら
れ、これら複数の火格子のうち少なくとも一つの
火格子が焼却炉本体内に出没自在に設けられると
ともに、この火格子が位置する焼却炉本体の側部
には該火格子が焼却炉本体内から没した時にこの
火格子を収納する収納室が設けられ、さらに収納
室には出没する火格子に吹きつける冷却用の空気
が供給されてなり、焼却炉本体の上部に投入され
たごみは、前記火格子上に堆積して十分な厚みを
有するごみ層を形成し、最上段から順次下方に燃
焼しながら送られて焼却炉の下端から順次排出す
るように構成されたものである。(Means for Solving the Problems) The vertical incinerator of the present invention is an incinerator that incinerates garbage such as general waste and industrial waste, and inside the incinerator body there is a A plurality of grates are provided that can be opened and closed to partition the incinerator into multiple rooms vertically, and at least one of the plurality of grate is provided so as to be able to appear and retract into the incinerator body, and this grate is A storage chamber is provided on the side of the incinerator body to store the grate when the grate is submerged from within the incinerator body, and the storage chamber also contains cooling air that is blown onto the recessed grate. The garbage that is supplied and thrown into the upper part of the incinerator body accumulates on the grate to form a sufficiently thick layer of garbage, and is sequentially sent downward while burning from the top stage to the incinerator. The structure is such that the water is discharged sequentially from the bottom end.
(作用)
焼却炉本体内に投入されたごみは、複数段に仕
切られた部屋を火格子の開閉動作によつて上方か
ら下方に順次落下しながら燃焼する。この落下時
に、未燃物の塊がほぐれ、ごみ層の通気性が良く
なり、燃焼を促進する。また、燃焼室の下方で発
生した燃焼ガスはすべて上方にあるごみ層を通過
することで、上方のごみの乾燥や着火を促進さ
せ、燃焼時のエネルギーを有効に利用する。(Function) Garbage thrown into the incinerator body is burned as it falls sequentially from the top to the bottom through the opening and closing operations of the grate through a room partitioned into multiple stages. During this fall, the unburnt particles are loosened and the dust layer becomes more permeable, promoting combustion. In addition, all the combustion gas generated below the combustion chamber passes through the dust layer above, which accelerates the drying and ignition of the dust above, making effective use of energy during combustion.
(実施例)
以下、本発明の一実施例を図面を参照して説明
する。(Example) Hereinafter, an example of the present invention will be described with reference to the drawings.
第1図は、本発明に係る竪型焼却炉の概略構成
を示している。 FIG. 1 shows a schematic configuration of a vertical incinerator according to the present invention.
図において、1はホツパで、ごみピツト(図示
省略)に貯留されたごみが均質化のため撹拌され
てある程度破袋された後、クレーン(図示省略)
でこのホツパ1に投入される。ホツパ1は、フイ
ーダ2を介して焼却炉本体3内の上部に連通され
ており、ホツパ1に投入されたごみはフイーダ2
によつて焼却炉本体3内に一定量ずつ送り込まれ
る。 In the figure, 1 is a hopper, where the garbage stored in a garbage pit (not shown) is stirred for homogenization and the bags are broken to some extent, and then the garbage is picked up by a crane (not shown).
Then it is put into this hopper 1. The hopper 1 is connected to the upper part of the incinerator main body 3 via the feeder 2, and the waste thrown into the hopper 1 is transferred to the feeder 2.
A fixed amount is fed into the incinerator main body 3 by the following.
焼却炉本体3には、開閉自在な第1火格子5,
5および第2火格子6,6が上下に設けられてお
り、焼却炉本体3内を2段に仕切つている。 The incinerator body 3 includes a first grate 5 that can be opened and closed.
5 and second grate 6, 6 are provided above and below, and the inside of the incinerator main body 3 is partitioned into two stages.
第1火格子5,5は、焼却炉本体3の左右両側
に水平方向に移動可能に配設されている。この第
1火格子5,5は、通常、焼却炉本体3内を閉塞
するように焼却炉本体3内に突出されており、こ
の第1火格子5,5によつてホツパ1から投入さ
れたごみを支持する。このように、第1火格子
5,5によつて閉塞された焼却炉本体3内の上部
が第1燃焼室3aになされている。また、第1火
格子5,5が位置する焼却炉本体3の両側には、
第1火格子5,5が焼却炉本体3内から没した時
に、この第1火格子5,5を収納する収納室7,
7が設けられている。収納室7,7には常温空気
8が供給されている。この常温空気8は、焼却炉
本体3と収納室7との間に形成された隙間9,9
から焼却炉本体3内に吹き出し、第1火格子5,
5の冷却を行うとともに、この隙間9,9から焼
却炉本体3内の焼却灰が収納室7側に侵入しない
ように防止している。また、常温空気8は第1燃
焼室3aの上部にも2次空気として供給されてい
る。 The first grates 5, 5 are disposed on both left and right sides of the incinerator main body 3 so as to be movable in the horizontal direction. These first grates 5, 5 normally protrude into the incinerator body 3 so as to close the inside of the incinerator body 3, and the first grates 5, 5 allow the incinerator to be fed from the hopper 1. Support garbage. In this way, the upper part of the incinerator main body 3 that is closed by the first fire grates 5, 5 forms the first combustion chamber 3a. In addition, on both sides of the incinerator main body 3 where the first grate 5, 5 is located,
A storage chamber 7 that stores the first grates 5, 5 when the first grates 5, 5 are sunk from inside the incinerator main body 3;
7 is provided. Room temperature air 8 is supplied to the storage chambers 7, 7. This room temperature air 8 flows through gaps 9, 9 formed between the incinerator main body 3 and the storage chamber 7.
Air blows out into the incinerator main body 3 from the first grate 5,
5, and prevents the incinerated ash in the incinerator body 3 from entering the storage chamber 7 through the gaps 9, 9. Further, the normal temperature air 8 is also supplied to the upper part of the first combustion chamber 3a as secondary air.
第2火格子6,6は、焼却炉本体3内におい
て、水平位置から2点鎖線に示す垂直位置まで回
動自在に設けられている。この第2火格子6,6
と前記第1火格子5,5とで仕切られた部屋が第
2燃焼室3bになされている。そして、第2火格
子6,6を下方に回動することによつて、第2燃
焼室3b内の焼却灰を焼却炉本体3の下方に設け
られた灰搬出装置10に排出することができる。 The second fire grates 6, 6 are provided rotatably within the incinerator main body 3 from a horizontal position to a vertical position shown by a two-dot chain line. This second grate 6,6
A second combustion chamber 3b is defined as a second combustion chamber 3b. By rotating the second grate 6, 6 downward, the incinerated ash in the second combustion chamber 3b can be discharged to the ash discharging device 10 provided below the incinerator main body 3. .
ここで、前記第1火格子5,5の焼却炉本体3
に対する取付位置は、この第1火格子5,5上に
堆積されるごみが十分な厚みのごみ層を形成する
ように配置されている。 Here, the incinerator main body 3 of the first grate 5, 5
The mounting positions for the first fire grates 5, 5 are arranged so that the dust deposited on the first fire grates 5 forms a dust layer of sufficient thickness.
前記第1燃焼室3a、第2燃焼室3bおよび第
2火格子6,6の下方には、それぞれ温度調節さ
れた燃焼用空気11a,11b,11cがダンパ
ー12a,12b,12cを介して供給されてい
る。これら燃焼用空気11a,11b,11cは
ごみ質に応じて最適の温度に調節するが、焼却炉
本体3内の下方に供給するものはおき燃焼させる
ため、常時高温に保持されている。 Temperature-controlled combustion air 11a, 11b, 11c is supplied below the first combustion chamber 3a, second combustion chamber 3b, and second grate 6, 6 via dampers 12a, 12b, 12c, respectively. ing. The combustion air 11a, 11b, 11c is adjusted to an optimum temperature depending on the type of waste, but the air supplied to the lower part of the incinerator main body 3 is kept at a high temperature at all times in order to be combusted.
次に、このように構成された竪型焼却炉によつ
てごみを焼却する場合について説明する。 Next, a case will be described in which garbage is incinerated using the vertical incinerator configured as described above.
ホツパ1に貯留されたごみは、フイーダ2によ
つて焼却炉本体3の第1燃焼室3aに一定量ずつ
送り込まれ、第1火格子5,5上に堆積する。こ
のように第1火格子5,5上に堆積したごみは十
分な厚みを有するごみ層を形成する。そして、第
1燃焼室3aに供給されている燃焼用空気11a
によつて、第1燃焼室3aに堆積されたごみが燃
焼し始め、燃焼は徐々に第1燃焼室3a全体に拡
がる。これによつて、燃え易いごみは、この第1
燃焼室3aで完全に焼却されて焼却灰になる。こ
の燃焼時に発生した燃焼ガスは、第1燃焼室3a
を上昇する。すなわち、第1燃焼室3aの下部で
発生した燃焼ガスはすべて上部のごみ層を通つて
第1燃焼室3aを上昇する。この上昇時に燃焼ガ
スは、その熱で上部のごみの着火およびガス化を
促進するするとともに、生ごみの乾燥を行う。さ
らに、第1燃焼室3aの上部まで上昇した燃焼ガ
スは、この上部に供給されている2次空気8によ
つて再燃焼する。この燃焼時の放射熱によつて第
1燃焼室3aに投入されたごみの予備乾燥を行う
とともに、発火点の低い紙やプラスチツクを燃や
して火種になるのを促進する。次に、ある程度燃
焼が進んだ段階で、第1火格子5,5を焼却炉本
体3内から没して第1燃焼室3aの下部の焼却残
渣を第2燃焼室3bの容量分だけ第2火格子6,
6上に落下させる。この後、第1火格子5,5を
再び焼却炉本体3内に突出させて閉塞する。この
突出時において、第2燃焼室3bに落下した残渣
は一部の難燃物や未燃物を含んだ焼却灰でありご
みによる抵抗が少ないため、第1火格子5,5は
スムースに突出することができる。第2燃焼室3
bでは、第1火格子5,5が第1燃焼室3aに堆
積したごみの荷重を支持しているので、上部のご
みによる圧縮がないとともに、落下時のシヨツク
で未燃物の塊が崩壊されているため、第2燃焼室
3bに貯留された焼却灰の通気性が良くなつてい
る。そして、高温の燃焼用空気11b,11cを
供給すると、残留していた火種によつて焼却灰内
の未燃物が容易に燃える。燃焼用空気11b,1
1cの圧力は焼却灰の通気性が良いため、高くす
る必要がない。また、第2燃焼室3bでの燃焼時
に発生した燃焼ガスは上昇して第1燃焼室3aを
通過するので、第1燃焼室3aでの燃焼をさらに
促進させる。よつて、燃焼時のエネルギーを十分
に有効利用することができる。この後、第2火格
子6,6を下方に回動し、第2燃焼室3bの焼却
灰を灰搬出装置10に落下させる。このように、
焼却炉本体3内でごみを上方から下方に順次送つ
て燃焼を行う。 The garbage stored in the hopper 1 is fed by a feeder 2 into the first combustion chamber 3a of the incinerator main body 3 in a fixed amount, and is deposited on the first fire grates 5,5. The garbage accumulated on the first fire grates 5, 5 in this way forms a dust layer having a sufficient thickness. Combustion air 11a supplied to the first combustion chamber 3a
As a result, the garbage accumulated in the first combustion chamber 3a begins to burn, and the combustion gradually spreads throughout the first combustion chamber 3a. As a result, combustible garbage is
It is completely incinerated in the combustion chamber 3a and becomes incineration ash. The combustion gas generated during this combustion is transferred to the first combustion chamber 3a.
rise. That is, all the combustion gas generated in the lower part of the first combustion chamber 3a passes through the upper dust layer and ascends in the first combustion chamber 3a. During this rise, the combustion gas uses its heat to promote ignition and gasification of the garbage at the top, and also dries the garbage. Furthermore, the combustion gas that has risen to the upper part of the first combustion chamber 3a is re-combusted by the secondary air 8 that is supplied to this upper part. The radiant heat during combustion not only pre-dries the waste thrown into the first combustion chamber 3a, but also burns paper and plastic, which have low ignition points, and promotes them becoming ignition sources. Next, when the combustion has progressed to a certain extent, the first grates 5, 5 are lowered from inside the incinerator main body 3, and the incineration residue at the lower part of the first combustion chamber 3a is transferred to the second combustion chamber 3b by the capacity of the second combustion chamber 3b. grate 6,
6. Drop it on top. After that, the first grates 5, 5 are again projected into the incinerator body 3 and closed. At this time of ejection, the residue that has fallen into the second combustion chamber 3b is incineration ash containing some flame retardants and unburned materials, and there is little resistance from the garbage, so the first grates 5, 5 eject smoothly. can do. Second combustion chamber 3
In b, the first fire grates 5, 5 support the load of the garbage accumulated in the first combustion chamber 3a, so there is no compression due to the garbage on the upper part, and the chunks of unburned materials collapse due to the shock when they fall. Therefore, the permeability of the incinerated ash stored in the second combustion chamber 3b is improved. Then, when high-temperature combustion air 11b, 11c is supplied, unburned materials in the incineration ash are easily combusted by the remaining sparks. Combustion air 11b, 1
There is no need to increase the pressure of 1c because the incineration ash has good air permeability. Further, since the combustion gas generated during combustion in the second combustion chamber 3b rises and passes through the first combustion chamber 3a, combustion in the first combustion chamber 3a is further promoted. Therefore, the energy during combustion can be used effectively. Thereafter, the second fire grates 6, 6 are rotated downward to cause the incinerated ash in the second combustion chamber 3b to fall into the ash transport device 10. in this way,
Inside the incinerator body 3, garbage is sequentially sent from the top to the bottom for combustion.
さらに、第2燃焼室3bの燃焼時には、第1火
格子5,5が高温にさらされるが、収納室7と焼
却炉本体3との隙間9,9から供給される常温空
気8によつて第1火格子5,5が冷却されるた
め、高温による第1火格子5,5の焼損を防止し
ている。また、この隙間9,9から収納室7側へ
侵入する焼却灰を防止する。 Furthermore, during combustion in the second combustion chamber 3b, the first grate 5, 5 is exposed to high temperature, but the room temperature air 8 supplied from the gap 9, 9 between the storage chamber 7 and the incinerator main body 3 Since the first grates 5, 5 are cooled, burning of the first grates 5, 5 due to high temperatures is prevented. Further, incineration ash is prevented from entering the storage chamber 7 side through the gaps 9, 9.
なお、本例では、2つの火格子によつて焼却炉
本体3を上下2段に仕切つたものを示したが、2
つ以上の火格子によつて焼却炉本体3内を2段以
上に仕切つてもよい。また、第1火格子5,5お
よび第2火格子6,6の開閉機構は本例に限ら
ず、例えば、第1火格子5,5は複数に分割した
ダンピングロストルを用いてもよく、第2火格子
6,6は傾斜反転火格子を用いてもよい。 Note that in this example, the incinerator body 3 is partitioned into two stages, upper and lower, by two grate;
The inside of the incinerator main body 3 may be partitioned into two or more stages by three or more grate. Further, the opening/closing mechanism of the first grates 5, 5 and the second grates 6, 6 is not limited to this example. For example, the first grates 5, 5 may use a damping throttle divided into plural parts, As the two grates 6, 6, an inclined inverted grate may be used.
(発明の効果)
以上述べたように、本発明によれば、流動方式
の竪型焼却炉に比べ、焼却炉本体内のごみは、各
階の火格子によつて支持されているからごみが下
方に圧縮されることなくごみ層の通気性が良いた
め、押込送風機によつて焼却炉本体内に送り込む
燃焼用空気の圧力を小さくできるとともに、ごみ
の前処理を行う装置や砂を焼却炉本体内で流動さ
せる押込送風機等の設備が不要になる。このた
め、電力の消費量が削減でき経済的である。ま
た、燃焼用空気の圧力を小さくできるため、焼却
炉本体内が正圧になる危険性が小さく、ごみ挿入
口等のシールが不要になる。さらに、集塵装置側
に燃焼ガスとともに排出されるダスト量が非常に
少量になるため、集塵装置の負担を軽減できると
ともに、ダストに起因するガス冷却装置や熱交換
器のトラブルを防止することができる。(Effects of the Invention) As described above, according to the present invention, compared to a fluidized vertical incinerator, the waste inside the incinerator is supported by the grate on each floor, so the waste is moved downwards. Because the waste layer has good air permeability without being compressed, the pressure of the combustion air sent into the incinerator body by the forced blower can be reduced, and the waste pre-treatment equipment and sand can be transported inside the incinerator body. No equipment such as a forced air blower is required. Therefore, power consumption can be reduced and it is economical. Furthermore, since the pressure of the combustion air can be reduced, there is less risk of positive pressure building up inside the incinerator body, and there is no need to seal the waste insertion port or the like. Furthermore, since the amount of dust discharged along with the combustion gas to the dust collector side is extremely small, the burden on the dust collector can be reduced, and troubles caused by dust to the gas cooling device and heat exchanger can be prevented. Can be done.
また、焼却炉本体内の下部で発生した燃焼ガス
が上昇して上部のごみ層を通過する際にこの上部
のごみの着火及びガス化を促進するとともに、生
ごみの乾燥を行い、燃焼を助長するため、燃焼ガ
スの持つエネルギーを無駄なく有効に利用するこ
とができる。 In addition, when the combustion gas generated in the lower part of the incinerator body rises and passes through the upper garbage layer, it promotes ignition and gasification of the garbage in the upper part, and also dries the garbage and promotes combustion. Therefore, the energy contained in the combustion gas can be used effectively without wasting it.
さらに、焼却炉本体内に出没自在に設けられた
火格子は、収納室を介して火格子に吹きつけられ
る冷却用の空気により冷却されるため、高温によ
る火格子の焼損を防止することができるととも
に、この空気は燃焼用の空気として有効に利用す
ることができる。また、収納室を介して火格子に
吹きつけられる冷却用の空気は焼却炉本体側から
収納室への焼却灰の侵入を阻止することができ、
この焼却灰により火格子の作動を妨げることがな
く、火格子の出没動作を円滑に行うことができ
る。しかも、構成が簡単であるため、故障が起こ
る虞も従来のものに比べ少ない。 Furthermore, the grate installed inside the incinerator body so that it can appear and retract freely is cooled by cooling air that is blown onto the grate through the storage chamber, which prevents the grate from burning out due to high temperatures. At the same time, this air can be effectively used as combustion air. In addition, the cooling air blown onto the grate through the storage chamber can prevent incinerated ash from entering the storage chamber from the incinerator main body side.
This incinerated ash does not interfere with the operation of the grate, allowing the grate to move in and out smoothly. Moreover, since the configuration is simple, there is less risk of failure compared to conventional ones.
第1図は本発明に係る竪型焼却炉の概略構成を
示す側面図、第2図は流動方式による竪型焼却炉
の概略構成を示す側面図である。
3……焼却炉本体、5,5……第1火格子、
6,6……第2火格子、7……収納室、8……常
温空気(冷却用の空気)。
FIG. 1 is a side view showing a schematic configuration of a vertical incinerator according to the present invention, and FIG. 2 is a side view showing a schematic configuration of a vertical incinerator using a fluid flow system. 3... Incinerator main body, 5, 5... First grate,
6, 6...Second grate, 7...Storage room, 8...Normal temperature air (air for cooling).
Claims (1)
る焼却炉であつて、 焼却炉本体内には、この焼却炉本体内を上下に
複数段の部屋に仕切る複数の火格子が開閉自在に
設けられ、これら複数の火格子のうち少なくとも
一つの火格子が焼却炉本体内に出没自在に設けら
れるとともに、この火格子が位置する焼却炉本体
の側部には該火格子が焼却炉本体内から没した時
にこの火格子を収納する収納室が設けられ、さら
に収納室には出没する火格子に吹きつける冷却用
の空気が供給されてなり、焼却炉本体の上部に投
入されたごみは、前記火格子上に堆積して十分な
厚みを有するごみ層を形成し、最上段から順次下
方に燃焼しながら送られて焼却炉の下端から順次
排出するように構成されたことを特徴とする竪型
焼却炉。[Scope of Claims] 1. An incinerator for incinerating garbage such as general waste and industrial waste, which has a plurality of fires inside the incinerator main body which are divided vertically into a plurality of rooms. A grate is provided so as to be openable and closable, and at least one of the plurality of grate is provided so as to be freely retractable into the incinerator main body, and a grate is provided on the side of the incinerator main body where the grate is located. A storage chamber is provided to store the grate when it sinks from inside the incinerator body, and the storage chamber is also supplied with cooling air that blows onto the sunken grate, which is injected into the upper part of the incinerator body. The waste is deposited on the grate to form a sufficiently thick layer of waste, and the waste is sequentially sent downward from the top layer while being burned, and is sequentially discharged from the bottom of the incinerator. A vertical incinerator characterized by
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP19711387A JPS6441709A (en) | 1987-08-06 | 1987-08-06 | Vertical type incinerator |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP19711387A JPS6441709A (en) | 1987-08-06 | 1987-08-06 | Vertical type incinerator |
Publications (2)
Publication Number | Publication Date |
---|---|
JPS6441709A JPS6441709A (en) | 1989-02-14 |
JPH0335575B2 true JPH0335575B2 (en) | 1991-05-28 |
Family
ID=16368946
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP19711387A Granted JPS6441709A (en) | 1987-08-06 | 1987-08-06 | Vertical type incinerator |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS6441709A (en) |
Families Citing this family (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH0740826Y2 (en) * | 1989-06-19 | 1995-09-20 | 株式会社プランテック | Vertical incinerator with gas rectifier |
US5127344A (en) * | 1990-02-12 | 1992-07-07 | Kabushiki Kaisha Plantec | Incinerator and incinerating method employing the same |
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 |
Citations (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS4917709A (en) * | 1972-06-07 | 1974-02-16 |
-
1987
- 1987-08-06 JP JP19711387A patent/JPS6441709A/en active Granted
Patent Citations (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS4917709A (en) * | 1972-06-07 | 1974-02-16 |
Also Published As
Publication number | Publication date |
---|---|
JPS6441709A (en) | 1989-02-14 |
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