JPS5840089B2 - waste melting furnace - Google Patents

waste melting furnace

Info

Publication number
JPS5840089B2
JPS5840089B2 JP54059811A JP5981179A JPS5840089B2 JP S5840089 B2 JPS5840089 B2 JP S5840089B2 JP 54059811 A JP54059811 A JP 54059811A JP 5981179 A JP5981179 A JP 5981179A JP S5840089 B2 JPS5840089 B2 JP S5840089B2
Authority
JP
Japan
Prior art keywords
combustion chamber
waste
melting furnace
water treatment
supply path
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
Application number
JP54059811A
Other languages
Japanese (ja)
Other versions
JPS55152586A (en
Inventor
清一 阿部
栄彰 石原
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Kubota Corp
Original Assignee
Kubota Corp
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Kubota Corp filed Critical Kubota Corp
Priority to JP54059811A priority Critical patent/JPS5840089B2/en
Publication of JPS55152586A publication Critical patent/JPS55152586A/en
Publication of JPS5840089B2 publication Critical patent/JPS5840089B2/en
Expired legal-status Critical Current

Links

Classifications

    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23GCREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
    • F23G5/00Incineration of waste; Incinerator constructions; Details, accessories or control therefor
    • F23G5/08Incineration of waste; Incinerator constructions; Details, accessories or control therefor having supplementary heating
    • F23G5/085High-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)
  • Gasification And Melting Of Waste (AREA)
  • Processing Of Solid Wastes (AREA)

Description

【発明の詳細な説明】 本発明は、燃焼室に、その全周にわたって被処理物供給
路を接続すると共に、前記燃焼室の底部中央に、ガス排
出路兼溶融物取出路を接続した廃棄物溶融炉に関する。
DETAILED DESCRIPTION OF THE INVENTION The present invention provides a combustion chamber with a waste material supply path connected to the entire circumference of the combustion chamber, and a gas discharge path and molten material removal path connected to the bottom center of the combustion chamber. Regarding melting furnaces.

上記炉は、燃焼室内の高温ガスからの幅対伝熱を主体に
して廃棄物を燃焼溶融さぐるように構成したものである
が、本発明は、その輻射伝熱効果を極めて合理的かつ経
済的に向上さぞて、大巾な燃料節約を図れるようにし、
筐た、その輻射伝熱効果を高める手段に、本来焼却処理
されるべき水処理汚泥そのものを有効に利用して、汚泥
の処理と消費燃料の節減との両効果を得て、廃棄物処理
に訃いて極めて重要な経済的操炉な可能にする事を目的
とする。
The above-mentioned furnace is configured to burn and melt waste mainly through width-based heat transfer from high-temperature gas in the combustion chamber, but the present invention utilizes the radiation heat transfer effect in an extremely rational and economical manner. By improving fuel efficiency, we will be able to achieve significant fuel savings.
As a means to enhance the radiant heat transfer effect, the water treatment sludge itself, which should normally be incinerated, can be effectively used to achieve both sludge treatment and fuel consumption savings, thereby improving waste treatment. The purpose is to enable the extremely important economic operation of the reactor.

本発明による廃棄物溶融炉の特徴とする構成は、前記燃
焼室内で輝炎を形成させるために、前記被処理物供給路
の廃棄物に乾燥微粉状水処理汚泥を混入する装置を設け
た点にあり、かかる構成から次の作用効果を奏する。
A characteristic feature of the waste melting furnace according to the present invention is that in order to form a bright flame in the combustion chamber, a device is provided for mixing dry and pulverized water treatment sludge into the waste in the material supply path. This configuration provides the following effects.

すなわち、乾燥微粉状にした水処理汚泥を廃棄物に対し
て混入させる装置を設けたものであるから、廃棄物とと
もに燃焼室内に投入された微粉状の水処理汚泥が、バー
ナーの火炎に煽られて舞い上り、しかも、その水処理汚
泥の成分が一般に多量の有機成分を含むものであること
と相俟ってこの微粉状の水処理汚泥が燃焼炎中に輝炎を
形成することとなり、その結果、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事が
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なくでき、経済性が重視される廃
棄物処理のための溶融炉として極めて有用なものが得ら
れるに至った。
In other words, since the device is equipped with a device that mixes dry, pulverized water treatment sludge with waste, the pulverized water treatment sludge, which is thrown into the combustion chamber along with the waste, is fanned by the flame of the burner. In addition to the fact that the water treatment sludge generally contains a large amount of organic components, this fine powder water treatment sludge forms a bright flame in the combustion flame, and as a result, Radiation heat transfer from the high-temperature gas in the combustion chamber to the processed material can now be carried out extremely efficiently, and therefore the amount of fuel required to provide heat from the outside can be greatly reduced, placing emphasis on economic efficiency. An extremely useful melting furnace for waste treatment has now been obtained.

しかも、このように輝炎を形成するための手段として、
特別な燃焼用の助剤を用いるのではなく、本来、焼却処
理されるべき水処理汚泥そのものを有効に利用するもの
であるから、前述の消費燃料の節減を一層高めるととも
に、汚泥の処理も同時的に行える利点がある。
Moreover, as a means to form a luminous flame in this way,
Rather than using special combustion aids, the water treatment sludge itself, which should normally be incinerated, is effectively used, which not only further reduces the amount of fuel consumed, but also treats the sludge at the same time. It has the advantage of being able to be done.

さらにまた、前記廃棄物に水処理汚泥を混入させるに際
して、例えば燃焼用バーナーへの空気供給路に微粉状の
水処理汚泥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ハ、水処理汚泥の熱焼カスが
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。
Furthermore, when mixing water treatment sludge with the waste, it is also possible to supply fine powder water treatment sludge to the air supply path to the combustion burner, for example, but compared to such a method, The present invention is also advantageous in that it can avoid drawbacks such as the occurrence of clogging due to the adhesion of thermally burned residue of water treatment sludge to the burner nozzle.

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.

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□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にか
いて充填下降さぞなから燃焼室3に供給すべく構成しで
ある。
A combustion chamber 3 having a conical heat reflecting wall 1 and a burner 2 disposed downward in the center thereof is connected with a supply path 4 for descending the weight of the material to be processed over its entire circumference. A plurality of input hoppers 5 are provided, and various industrial wastes such as city garbage, its heat-treated products, or molded dried sludge generated from water treatment such as sewage are filled and lowered into the supply channel 4. It is configured to supply the fuel directly to the combustion chamber 3.

下水等の水処理により発生する汚泥を乾燥微粉状でホッ
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乾燥微粉状水処
理汚泥が発熱量の極めて犬なる状態で燃焼しながら炎中
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、本来溶融処理すべき廃棄物の一種
である水処理汚泥を有効利用した極めて合理的かつ経済
的な手段によって、廃棄物を自燃によってのみ溶融さぞ
たり、あるいは、バーナ2からの発熱量を大巾に少なく
した状態で溶融さぞたりするように構成しである。
A device 6 is provided for supplying sludge generated by water treatment such as sewage to a hopper 5 in the form of dry fine powder and mixing it with the waste in the supply path 4. The treated sludge is constructed so that it burns with an extremely high calorific value and floats in the flame, forming a bright flame with extremely high radioactivity, making it a type of waste that should originally be melted and treated. By an extremely rational and economical means that makes effective use of water treatment sludge, it is configured to melt waste only by self-combustion, or to melt it while greatly reducing the amount of heat generated from burner 2. It is.

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1aを
中央側はど低くなる円錐面状に形状に形成し、炉底壁7
を駆動装置9によって自転すせるべく構成し、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中夫に移動さぞながら、燃焼さぜた後溶融でぜるべく
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,
The gas discharge path/melt removal path 8 is connected, and the furnace bottom inner surface 1a is formed into a conical shape with the center side lowered, and the furnace bottom wall 7 is connected.
is configured to rotate by a drive device 9, and thereby,
The waste from the supply path 4 is moved along the inner surface 7a of the furnace bottom into the combustion chamber 3, where it is burned and then melted to be destroyed, and the molten material and combustion gas are discharged downward. It is configured as follows.

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拵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L−サらに、第3図に示すように、煙道12の入
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4遊物の完全燃焼を行わぞるように構成し、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 illustrated in FIG.
The direction of ejection is set close to the tangential direction of the inner circumference,
As shown in FIG. A checker 14 is provided near the inlet of the exhaust gas to ensure complete combustion of gas and unburned substances, thereby ensuring that odor pollution and dust pollution caused by exhaust gas discharge into the atmosphere are prevented as a whole. It is constructed in such a way that it can be prevented.

冷却用水槽13にその水面近くに沈んだ状態で受止め具
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11周りで回動自在に構成して、溶融物
を受止め具15上で可及的に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成し
、さらに、受止め具15上に固化物が適当量音源ると、
固化物を水槽13内に落下できるように構成しである。
A catch 15 is provided in the cooling water tank 13 in a state submerged near the water surface, and the catch 15 is moved by a drive device 16.
The molten material is configured to be rotatable around the horizontal axis 11, and the molten material is cooled as slowly as possible on the receiver 15, thereby suppressing the atomization of the solidified material, and also suppressing the fineness of the solidified material. It is configured to suppress the generation of steam from the water tank 13, and further, if a suitable amount of solidified material is a sound source on the receiver 15,
The structure is such that the solidified material can fall into the water tank 13.

寸た、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16の間隔変
更を、両者15,16を連動する巻掛伝動具13に対す
るテンション用輪体20の作用で許容さぐるべく構成し
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 the first drive device 16 is changed. is constructed so as to be permitted by the action of the tension wheel 20 on the winding transmission device 13 that interlocks both 15 and 16, and the above-mentioned solidified fine particles are always removed by the catch 15 regardless of the liquid level in the water tank 13. The structure is such that suppression of oxidation and vapor generation can be effectively performed.

さらに、水槽13内の固化物を容器24に回収するため
に、ベルトコンベア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.

【図面の簡単な説明】[Brief explanation of the drawing]

図面は本発明に係る廃棄物溶融炉の実施例を示し、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
図ぽ煙道の要部斜視図、第4図ぽ冷却装置の縦断面図で
ある。 3・・・・・・燃焼室、4・・・・・・被処理物供給路
、8・・・・・・ガス排出路兼溶融物取出路、6・・・
・・・乾燥微粉状水処理汚泥を混入する装置。
The drawings show an embodiment of the waste melting furnace according to the present invention.
The figure is a schematic longitudinal cross-sectional view, the second figure is a cross-sectional view of the after-combustion chamber, and the third figure is a cross-sectional view of the after-combustion chamber.
FIG. 4 is a perspective view of the main part of the flue, and FIG. 4 is a longitudinal cross-sectional view of the cooling device. 3... Combustion chamber, 4... Processing material supply path, 8... Gas discharge path/melt material removal path, 6...
...A device that mixes dry, pulverized water treatment sludge.

Claims (1)

【特許請求の範囲】[Claims] 1 燃焼室3に、その全周にわたって被処理物供給路4
を接続すると共に、前記燃焼室3の底部中央に、ガス排
出路兼溶融物取出路8を接続した廃棄物溶融炉であって
、前記燃焼室3内で輝炎を形成さぜるために、前記被処
理物供給路4の廃棄物に乾燥微粉状水処理汚泥を混入す
る装置6を設けである事を特徴とする廃棄物溶融炉。
1 A to-be-processed material supply path 4 is provided in the combustion chamber 3 over its entire circumference.
A waste melting furnace is provided in which a gas discharge passage and melt extraction passage 8 is connected to the bottom center of the combustion chamber 3, and in order to form a bright flame within the combustion chamber 3, A waste melting furnace characterized in that a device 6 for mixing dry, pulverized water treatment sludge into the waste in the material supply path 4 is provided.
JP54059811A 1979-05-15 1979-05-15 waste melting furnace Expired JPS5840089B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP54059811A JPS5840089B2 (en) 1979-05-15 1979-05-15 waste melting furnace

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP54059811A JPS5840089B2 (en) 1979-05-15 1979-05-15 waste melting furnace

Publications (2)

Publication Number Publication Date
JPS55152586A JPS55152586A (en) 1980-11-27
JPS5840089B2 true JPS5840089B2 (en) 1983-09-03

Family

ID=13123986

Family Applications (1)

Application Number Title Priority Date Filing Date
JP54059811A Expired JPS5840089B2 (en) 1979-05-15 1979-05-15 waste melting furnace

Country Status (1)

Country Link
JP (1) JPS5840089B2 (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH0327489U (en) * 1989-07-28 1991-03-19

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5795515A (en) * 1980-12-05 1982-06-14 Kubota Ltd Method of removal of melted waste material from melting furnace

Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS50154839A (en) * 1974-06-04 1975-12-13

Patent Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS50154839A (en) * 1974-06-04 1975-12-13

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH0327489U (en) * 1989-07-28 1991-03-19

Also Published As

Publication number Publication date
JPS55152586A (en) 1980-11-27

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