JPS5840088B2 - Industrial waste incineration method - Google Patents
Industrial waste incineration methodInfo
- Publication number
- JPS5840088B2 JPS5840088B2 JP54058821A JP5882179A JPS5840088B2 JP S5840088 B2 JPS5840088 B2 JP S5840088B2 JP 54058821 A JP54058821 A JP 54058821A JP 5882179 A JP5882179 A JP 5882179A JP S5840088 B2 JPS5840088 B2 JP S5840088B2
- Authority
- JP
- Japan
- Prior art keywords
- combustion chamber
- waste
- pulverized coal
- industrial waste
- combustion
- 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
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
- F23G5/08—Incineration of waste; Incinerator constructions; Details, accessories or control therefor having supplementary heating
- F23G5/085—High-temperature heating means, e.g. plasma, for partly melting the waste
Landscapes
- Engineering & Computer Science (AREA)
- Physics & Mathematics (AREA)
- Plasma & Fusion (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Combustion Of Fluid Fuel (AREA)
- Gasification And Melting Of Waste (AREA)
- Processing Of Solid Wastes (AREA)
Description
【発明の詳細な説明】
本発明は、都市ゴミやその熱処理物、あるいは下水等の
水処理により発生する汚泥の成型乾燥物等の各種産業廃
棄物を焼却処理する方法に関するものである。DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a method for incinerating various industrial wastes, such as municipal waste, heat-treated waste thereof, and molded and dried sludge generated from water treatment such as sewage.
この種の焼却処理方法においては、焼却に際しての燃料
の節約を考慮して輻射伝熱を有効に利用するように炉を
構成してはいるが、炉自体の構成によっては自と限界が
あり、燃料を大幅に節約するまでには至っていない。In this type of incineration treatment method, the furnace is configured to effectively utilize radiation heat transfer in consideration of saving fuel during incineration, but there are limitations depending on the configuration of the furnace itself. This has not led to significant fuel savings.
そこで、本発明は火炎輝度の増加によって輻射熱量を大
きくするに際して、微粉炭を産業廃棄物に混在させた状
態で燃焼室に供給し、燃焼室での廃棄物燃焼に伴って微
粉炭が燃焼しながら炎中に浮遊すべく構成することによ
って、輻射熱量が極めて大きい火炎輝度の高い輝炎を形
成することにより、燃料の大幅な節約をはかり得ると共
に、その微粉炭の供給に際して、バーナノズルに目詰り
などを生じさせることなく供給できるようにすることを
目的とする。Therefore, in order to increase the amount of radiant heat by increasing the flame brightness, the present invention supplies pulverized coal mixed with industrial waste to the combustion chamber, and combusts the pulverized coal as the waste burns in the combustion chamber. By constructing the pulverized coal so that it floats in the flame, it forms a bright flame with an extremely large amount of radiant heat, which can significantly save fuel, and prevents clogging of the burner nozzle when supplying the pulverized coal. The purpose is to enable supply without causing problems such as
本発明による産業廃棄物の焼却処理方法は、都市ゴ□や
その他の乾燥廃棄物からなる産業廃棄物に対して、燃焼
室への投入工程で微粉炭を混入させる点にあり、かかる
構成から次の作用効果を奏する。The method for incinerating industrial waste according to the present invention consists in mixing pulverized coal into the industrial waste consisting of city garbage and other dry waste in the process of feeding it into the combustion chamber, and from this structure, the following steps are taken: It has the following effects.
すたわち、都市ゴ□や乾燥廃棄物などからなる産業廃棄
物に対して、それらが一般に比較的乾燥状態にある燃焼
室への投入工程で微粉炭を混入させることにより、この
微粉炭が廃棄物中の水分を吸湿して廃棄物中に溶は込み
、ケーキ状に一体化してしまうことを避は得る結果、燃
焼室内での燃焼時に、前記微粉炭が燃焼バーナーの燃焼
ガス噴出圧などで煽られて舞い上がり、燃焼炎中に輝炎
を形成することとなり、これに伴って、燃焼室内での高
温ガスから処理物への輻射伝熱を極めて効率良く行わせ
ることができるようになり、従って、外部から熱を与え
るために要する燃料を大巾に少rx <でき、経済性が
重視される廃棄物処理に有用な方法を得られるに至った
。In other words, by mixing pulverized coal into industrial waste such as urban garbage and dry waste during the process of feeding it into the combustion chamber, which is generally in a relatively dry state, this pulverized coal is This prevents moisture from absorbing moisture from the waste and dissolving it into the waste, resulting in a cake-like formation.As a result, when the pulverized coal is burned in the combustion chamber, the pulverized coal has a lower combustion gas ejection pressure from the combustion burner. It is stirred up by the flame and rises up, forming a bright flame within the combustion flame, and as a result, radiation heat transfer from the high-temperature gas in the combustion chamber to the processed material can be carried out extremely efficiently. Therefore, the amount of fuel required to apply heat from the outside can be significantly reduced, and a method useful for waste treatment, where economic efficiency is important, has been obtained.
また、前記産業廃棄物に微粉炭を混入させるに際して、
例えば燃焼用バーナーへの空気供給路に微粉炭を供給し
て行うことも考えられるが、このようなものに比しても
本発明は、微粉炭の燃焼ガスがバーナーノズルに付着し
て詰りを生じる等の欠点を避は得る点で有利である。In addition, when mixing pulverized coal into the industrial waste,
For example, it is conceivable to supply pulverized coal to the air supply path to the combustion burner, but compared to such a method, the present invention prevents the combustion gas of pulverized coal from adhering to the burner nozzle and clogging it. This is advantageous in that it avoids disadvantages such as those that occur.
以下に、本発明の実施例を図面に基いて説明する。Embodiments of the present invention will be described below based on the drawings.
まず、本発明方法に用いられる装置について説明すると
1円錐面状の熱反射壁1とその中央に下向きに配置した
バーナ2とを有する燃焼室3に、その全周にわたって被
処理物の自重下降供給路4を接続し、その供給路4の上
部に複数個の投入ホッパ5を設け、もって、都市ゴミや
その熱処理物、あるいは下水等の水処理により発生する
汚泥の成型乾燥物等の各種産業廃棄物を、供給路4にお
いて充填下降させたから燃焼室3に供給すべく構成しで
ある。First, to explain the apparatus used in the method of the present invention, a material to be treated is supplied under its own weight to a combustion chamber 3 having a conical heat reflecting wall 1 and a burner 2 disposed downward in the center thereof. A plurality of input hoppers 5 are installed at the upper part of the supply channel 4, and various industrial wastes such as municipal waste, heat-treated waste thereof, and molded dried sludge generated from water treatment such as sewage can be collected. The structure is such that the material is charged and lowered in the supply path 4 and then supplied to the combustion chamber 3.
微粉状可燃・物質としての微粉炭を、ホッパ5に供給し
て供給路4の廃棄物に混入する装置6を設けて、燃焼室
3での廃棄物燃焼に伴って微粉状可燃物質が燃焼したか
ら炎中に浮遊して、輻射能が極めて大きい輝炎が形成さ
れるように構成し、もって、廃棄物を自燃によってのみ
溶融させたり、あるいは、バーナ2からの発熱量を大巾
に少たくした状態で溶融させたりするように構成しであ
る。A device 6 is provided to supply pulverized coal as a pulverized combustible material to a hopper 5 and mix it into the waste in the supply path 4, so that the pulverized combustible material is combusted as the waste is burned in the combustion chamber 3. It is configured so that it floats in the flame and forms a bright flame with extremely high radiation ability, thereby melting the waste only by self-combustion, or greatly reducing the amount of heat generated from the burner 2. The structure is such that it can be melted in a molten state.
燃焼室3から供給路4下部にわたる炉底壁7の中央に、
ガス排出路兼溶融物取出路8を接続し、炉底内面7aを
中央側はど低くなる円錐面状に形成し、炉底壁7を駆動
装置9によって自転させるべく構成し、もって、供給路
4からの廃棄物を、炉底内面7aに沿って燃焼室3中夫
に移動させながら、燃焼させた後溶融させるべく構成す
ると共に、溶融物及び燃焼ガスを下方に排出させるよう
に構成しである。In the center of the furnace bottom wall 7 extending from the combustion chamber 3 to the lower part of the supply path 4,
A gas discharge path/melt removal path 8 is connected, the furnace bottom inner surface 7a is formed into a conical shape with the center side being lower, and the furnace bottom wall 7 is configured to rotate by a drive device 9. The waste material from the combustion chamber 3 is moved along the inner surface 7a of the furnace bottom to the combustion chamber 3, and the waste material is combusted and then melted, and the molten material and combustion gas are discharged downward. be.
補助バーナ10を備えた後燃焼室11を前記取出路8に
接続し、後燃焼室11に横向き煙道12を接続し、後燃
焼室11の下方に冷却用水槽13を設け、もって、燃焼
ガス及び未燃浮遊物を完全燃焼させた後煙道12に送る
と共に、溶融物を冷却固化させるように構成しである。A post-combustion chamber 11 equipped with an auxiliary burner 10 is connected to the outlet passage 8, a horizontal flue 12 is connected to the post-combustion chamber 11, a cooling water tank 13 is provided below the post-combustion chamber 11, and the combustion gas is The unburned suspended matter is completely combusted and then sent to the flue 12, and the molten matter is cooled and solidified.
第2図に示すように後燃焼室11の内周面を円形あるい
はそれに近い形状に構成すると共に、補助バーナ10の
噴出方向をその内周面の接線方向に近い方向にして、後
燃焼室11内での旋回流動により燃焼室3からのガス及
び未燃浮遊物の完全燃焼をより一層確実に行えるように
構成し、さらに、第3図に示すように、煙道120入口
近くにチェッカー14を設けて、より完べきにガス及び
未燃浮遊物の完全燃焼を行わせるように構成し、全体と
して排ガスの大気放出に伴う悪臭公害及び粉塵公害発生
を確実に防止できるように構成しである。As shown in FIG. 2, the inner peripheral surface of the after-combustion chamber 11 is configured to have a circular shape or a shape close to it, and the ejection direction of the auxiliary burner 10 is set close to the tangential direction of the inner peripheral surface. The structure is configured to further ensure complete combustion of gas and unburned suspended matter from the combustion chamber 3 by swirling flow within the combustion chamber 3, and as shown in FIG. 3, a checker 14 is installed near the entrance of the flue 120. The structure is such that gas and unburned suspended matter are more completely combusted, and as a whole, odor pollution and dust pollution caused by exhaust gas being released into the atmosphere can be reliably prevented.
冷却田水槽13にその水面近くに下面が沈んだ状態で平
板状受止め具15を設けると共に、その受止め具15を
駆動装置16により横向き軸17周りで回動自在に構威
して、溶融物を受止め具15上で徐冷する事によって固
化物の微細化を抑制すると共に、後燃焼室11からの輻
射熱による水槽13からの蒸気発生を抑制するように構
威し、さらに、受止め具15に固化物が適当量留まると
、固化物を水槽13内に落下できるように構成しである
。A plate-shaped catch 15 is provided in the cooling field water tank 13 with its lower surface sunk near the water surface, and the catch 15 is configured to be rotatable around a horizontal shaft 17 by a drive device 16 to melt the water. By slowly cooling the object on the catcher 15, it is possible to suppress the fineness of the solidified material and to suppress the generation of steam from the water tank 13 due to the radiant heat from the post-combustion chamber 11. The structure is such that when an appropriate amount of solidified material remains on the tool 15, the solidified material can be dropped into the water tank 13.
また、第4図に示すように、受止め具15に、それを水
槽13の液位変化に伴って昇降させるフロート18を連
設すると共に、受止め具15と1駆動装置160間隔変
更を、両者15.16を連動する巻掛伝動具19に対す
るテンション用輪体20の作用で許容させるべく構成し
て、水槽13の液位いかんにかかわらず受止め具15に
よって常に前述の固化物微細化抑制及び蒸気発生抑制が
良好に行われるように構成しである。In addition, as shown in FIG. 4, a float 18 is connected to the catch 15 to raise and lower it according to changes in the liquid level in the water tank 13, and the distance between the catch 15 and one drive device 160 can be changed. Both 15 and 16 are configured to be allowed by the action of the tension wheel 20 on the interlocking winding transmission 19, and the above-mentioned solidified matter atomization is always suppressed by the catch 15 regardless of the liquid level in the water tank 13. and is configured to effectively suppress steam generation.
さらに、水槽13内の固化物を容器24に回収するため
に、ベルトコンベギ21及びホッパ22を設けである。Furthermore, a belt conveyor 21 and a hopper 22 are provided to collect the solidified material in the water tank 13 into a container 24.
上記の装置を用いて焼却処理を行うには、まず、都市ゴ
ミやその熱処理物、あるいは下水等の水処理により発生
する汚泥の成型乾燥物等の各種廃棄物を、前記供給路4
の上部に設けられた投入ホッパ5に投入し、他方、前記
供給路4の廃棄物に微粉炭を混入する装置6に微粉炭を
装填し、この微粉炭と前記産業廃棄物とを混入させた状
態で同時的に供給路4を下降させ、燃焼室1にこれらを
送り込み、燃焼させるものである。To perform incineration using the above-mentioned apparatus, first, various types of waste such as municipal garbage, heat-treated waste thereof, or molded dried sludge generated from water treatment such as sewage are transferred to the supply channel 4.
On the other hand, the pulverized coal was loaded into a device 6 for mixing the pulverized coal into the waste in the supply path 4, and the pulverized coal was mixed with the industrial waste. In this state, the supply path 4 is simultaneously lowered, and these are fed into the combustion chamber 1 and combusted.
図面は本発明に係る産業廃棄物の焼却処理方法に用いら
れる装置を示し、第1図は概略縦断面図、第2図は後燃
焼室の横断面図、第3図は煙道の要部斜視図、第4図は
冷却装置の縦断面図、である。
3・・・・・・燃焼室、4・・・供給路、6・・・微粉
炭混入装置。The drawings show an apparatus used in the industrial waste incineration treatment method according to the present invention, in which Fig. 1 is a schematic vertical cross-sectional view, Fig. 2 is a cross-sectional view of the after-combustion chamber, and Fig. 3 is a main part of the flue. FIG. 4 is a perspective view, and FIG. 4 is a longitudinal sectional view of the cooling device. 3... Combustion chamber, 4... Supply path, 6... Pulverized coal mixing device.
Claims (1)
に対して、燃焼室への投入工程で微粉炭を混入させるこ
とを特徴とする産業廃棄物の焼却処理方法。1. A method for incinerating industrial waste, which is characterized by mixing pulverized coal into industrial waste consisting of municipal garbage and other dry waste during the process of feeding it into a combustion chamber.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP54058821A JPS5840088B2 (en) | 1979-05-14 | 1979-05-14 | Industrial waste incineration method |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP54058821A JPS5840088B2 (en) | 1979-05-14 | 1979-05-14 | Industrial waste incineration method |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS55152585A JPS55152585A (en) | 1980-11-27 |
| JPS5840088B2 true JPS5840088B2 (en) | 1983-09-03 |
Family
ID=13095288
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP54058821A Expired JPS5840088B2 (en) | 1979-05-14 | 1979-05-14 | Industrial waste incineration method |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS5840088B2 (en) |
Families Citing this family (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN114593429A (en) * | 2022-02-16 | 2022-06-07 | 段强 | An environmentally friendly waste incineration device |
Family Cites Families (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS5551124B2 (en) * | 1974-06-04 | 1980-12-22 |
-
1979
- 1979-05-14 JP JP54058821A patent/JPS5840088B2/en not_active Expired
Also Published As
| Publication number | Publication date |
|---|---|
| JPS55152585A (en) | 1980-11-27 |
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