JP2000337616A - Melting method and furnace for combustible waste - Google Patents

Melting method and furnace for combustible waste

Info

Publication number
JP2000337616A
JP2000337616A JP11149312A JP14931299A JP2000337616A JP 2000337616 A JP2000337616 A JP 2000337616A JP 11149312 A JP11149312 A JP 11149312A JP 14931299 A JP14931299 A JP 14931299A JP 2000337616 A JP2000337616 A JP 2000337616A
Authority
JP
Japan
Prior art keywords
melting
combustible waste
furnace
water
main chamber
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.)
Pending
Application number
JP11149312A
Other languages
Japanese (ja)
Inventor
Satoshi Wada
聰 和田
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 JP11149312A priority Critical patent/JP2000337616A/en
Publication of JP2000337616A publication Critical patent/JP2000337616A/en
Pending legal-status Critical Current

Links

Abstract

PROBLEM TO BE SOLVED: To accelerate combustion of combustible wastes and miniaturize a melting furnace in melting method and furnace for supplying wastes including combustible ones to the melting furnace as processing objects, introducing the same into a main chamber for melting treatment, and heating the same in a slightly oxidizing atmosphere therein until they are melt at the surface F thereof and formed into melt slag. SOLUTION: A processing object supply section 10 for supplying processing objects 15 to a main chamber 9 is provided with a water supply system 14 for supplying moisture to the processing objects 15 to let combustible wastes 17 hold the moisture in advance so as to induce water-gas shift reaction in the main chamber 9 between carbon in the combustible wastes 17 and the moisture held therein. Combustible gas generated by the water-gas reaction is burnt on the surface F of the processing objects 15 and in the neighborhood thereof.

Description

【発明の詳細な説明】DETAILED DESCRIPTION OF THE INVENTION

【0001】[0001]

【発明の属する技術分野】本発明は、可燃性廃棄物の溶
融処理方法及び溶融処理炉に関し、詳しくは、可燃性廃
棄物を含む廃棄物を被処理物として溶融炉に供給する第
一工程と、前記供給された被処理物を溶融処理する主室
に導く第二工程と、前記被処理物を弱酸化性雰囲気内で
加熱して、前記被処理物の表面を溶融させて溶融スラグ
を形成する第三工程とからなる可燃性廃棄物の溶融処理
方法、及び可燃性廃棄物を含む被処理物を蓄積する堆積
部と、前記堆積部から供給される被処理物を弱酸化性雰
囲気下で加熱溶融する主室と、前記主室の底部に、前記
被処理物の表面が溶融して生成した溶融スラグを排出す
るスラグ排出部とを設けてある可燃性廃棄物の溶融処理
炉に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method and a furnace for melting combustible waste, and more particularly to a first step of supplying waste containing combustible waste to a melting furnace as an object to be treated. And a second step of guiding the supplied workpiece to a main chamber for melting and heating the workpiece in a weakly oxidizing atmosphere to melt the surface of the workpiece to form a molten slag. A method of melting the combustible waste comprising a third step, and a deposition section for accumulating the article to be treated including the combustible waste, and treating the article supplied from the deposition section in a weakly oxidizing atmosphere. The present invention relates to a flammable waste melting processing furnace provided with a main chamber for heating and melting, and a slag discharge section provided at the bottom of the main chamber for discharging molten slag generated by melting the surface of the object.

【0002】[0002]

【従来の技術】従来、可燃性廃棄物の溶融処理装置にお
いては、例えば図6に示すように、溶融炉1は、固定さ
れた内筒2と、前記内筒2と同軸心回りに回転駆動自在
で、底部8を備える外筒7とで構成してあり、前記内筒
2に備える炉天井部3と前記底部8との間に、堆積部S
から供給される被処理物15を弱酸化性雰囲気下で加熱
溶融する主室9を形成して、前記主室9の底部8に、前
記被処理物15の擂り鉢型に形成される表面Fが溶融し
て生成した溶融スラグ24を排出するスラグ排出部8a
とを設けてあった。前記炉天井部3には、前記主室9内
に一次空気を供給する空気ノズル5と、前記主室9内に
燃料を供給して、供給した燃料を燃焼させるバーナ4と
が設けられており、燃料供給路18を前記バーナ4に接
続し、空気供給路19を、前記バーナ4と前記空気ノズ
ル5とに夫々接続してあって、供給された燃料の燃焼熱
により前記主室9内の空間が加熱され、その熱により前
記表面Fにおける被処理物15を溶融させるように構成
されている。このために、前記燃料供給路18に備える
燃料調節弁21と、前記バーナ4への空気供給路19に
備えるバーナ空気調節弁22と、前記空気ノズル5への
空気供給路19に備える主室空気調節弁23とが、夫々
炉内温度調節手段20によって調節されるように構成し
てある。尚、前記被処理物15中の可燃性廃棄物17も
炉内の熱と、一次空気とにより燃焼するが、その熱によ
り炉内の温度を維持するには、前記可燃性廃棄物17の
燃焼速度が低く、十分な熱量を発生しない。前記堆積部
Sは、前記内筒2と前記外筒7との間の環状空間を経て
供給される可燃性廃棄物17を含む前記被処理物15を
前記底部8上に蓄積するように構成され、前記環状空間
の上を封じる環状天井部6に前記被処理物15を前記環
状空間内に投入する投入部11を設け、前記主室9に対
する表面Fに前記被処理物15を供給する堆積部Sと、
前記投入部11とで被処理物供給部10を形成してあっ
た。前記堆積部Sからは、前記内筒2の下端部2aに設
けられた切出羽根13によって、前記堆積部S内の被処
理物15が前記主室9に向けて掻き出される。
2. Description of the Related Art Conventionally, in a combustible waste melting apparatus, as shown in FIG. 6, for example, a melting furnace 1 has a fixed inner cylinder 2 and a rotary drive around a coaxial center with the inner cylinder 2. The outer cylinder 7 is freely provided and has a bottom 8, and a stacking section S is provided between the furnace ceiling 3 provided in the inner cylinder 2 and the bottom 8.
A main chamber 9 for heating and melting the object 15 supplied from the furnace under a weakly oxidizing atmosphere is formed on the bottom 8 of the main chamber 9 to form a mortar-shaped surface F of the object 15. Discharging section 8a for discharging molten slag 24 generated by melting
And was provided. The furnace ceiling 3 is provided with an air nozzle 5 for supplying primary air into the main chamber 9 and a burner 4 for supplying fuel to the main chamber 9 and burning the supplied fuel. The fuel supply passage 18 is connected to the burner 4, and the air supply passage 19 is connected to the burner 4 and the air nozzle 5, respectively. The space is heated, and the heat is used to melt the object 15 on the surface F. To this end, a fuel control valve 21 provided in the fuel supply path 18, a burner air control valve 22 provided in the air supply path 19 to the burner 4, and a main chamber air provided in the air supply path 19 to the air nozzle 5 The control valves 23 are configured to be controlled by the in-furnace temperature control means 20, respectively. The combustible waste 17 in the object 15 is also burned by the heat in the furnace and the primary air. To maintain the temperature in the furnace by the heat, the combustion of the combustible waste 17 is required. The speed is low and does not generate enough heat. The stacking unit S is configured to accumulate on the bottom 8 the object 15 including the combustible waste 17 supplied through an annular space between the inner cylinder 2 and the outer cylinder 7. An input section 11 for inputting the processing object 15 into the annular space in the annular ceiling section 6 which seals the annular space; and a deposition section for supplying the processing object 15 to the surface F with respect to the main chamber 9. S and
The processing object supply unit 10 was formed by the charging unit 11. From the stacking section S, a processing object 15 in the stacking section S is scraped out toward the main chamber 9 by a cutting blade 13 provided at a lower end 2 a of the inner cylinder 2.

【0003】上述のように、前記被処理物供給部10か
らは、可燃性廃棄物17も投入されるのであるが、通常
は、予め熱分解処理が施された前記可燃性廃棄物17の
熱分解残さであるチャーが投入される。
[0003] As described above, the combustible waste 17 is also supplied from the article supply unit 10, but usually, the heat of the combustible waste 17 which has been subjected to a thermal decomposition process is usually used. The char which is the decomposition residue is thrown in.

【0004】[0004]

【発明が解決しようとする課題】ところで、上記従来の
廃棄物の溶融処理炉においては、前記可燃性廃棄物17
を溶融処理するに際しての事前の熱分解処理によって得
られたチャーを、被処理物15として炉内に投入するも
ので、前記チャーは炉内で固体燃焼するから、燃焼速度
が低く、炉内温度を前記被処理物15中の不燃物を溶融
させるに十分な温度に維持できるものではなく、また、
前記可燃性廃棄物17の炉内滞留時間が足りなければ、
前記チャーが未燃分として前記スラグ排出部8aから排
出されることもあるという問題を有している。さらに、
ダイオキシン排出防止の観点から、未燃分を排出させな
いために前記被処理物15の炉内滞留時間を十分に確保
しようとすれば、溶融処理炉のサイズが大きくなるとい
う問題も有している。この対策として、前記主室9にお
ける前記被処理物15の表面Fで水性ガス化反応を誘発
せしめるべく、前記主室9内に水蒸気を投入することを
先に提案した(特願平8−232166号)。つまり、
図7に示すように、溶融炉1に水蒸気供給機構25を設
けて、その水蒸気ノズル26を、前記炉天井部3に配置
したものである。これによって前記可燃性廃棄物17の
燃焼速度は改善されたが、前記主室9内の高温ガス中に
水蒸気を吹き込むから、前記可燃性廃棄物17中の炭素
分と接触するには、前記水蒸気の炉内雰囲気中での拡散
を必要とし、前記可燃性廃棄物17の燃焼速度が、満足
できる水準にまで高まるには至らなかった。
In the above-mentioned conventional waste melting furnace, the combustible waste 17 is used.
The char obtained by the prior pyrolysis treatment at the time of melting treatment is charged into the furnace as the object to be treated 15, and the char performs solid combustion in the furnace, so that the burning rate is low and the furnace temperature is low. Cannot be maintained at a temperature sufficient to melt the incombustibles in the processing object 15, and
If the residence time of the combustible waste 17 in the furnace is not enough,
There is a problem that the char may be discharged from the slag discharge section 8a as unburned matter. further,
From the viewpoint of preventing dioxin emission, there is also a problem that the size of the melting furnace increases if an attempt is made to ensure a sufficient residence time of the workpiece 15 in the furnace so as not to discharge unburned components. As a countermeasure, it has been previously proposed that steam be injected into the main chamber 9 in order to induce a water gasification reaction on the surface F of the object 15 in the main chamber 9 (Japanese Patent Application No. 8-232166). issue). That is,
As shown in FIG. 7, a steam supply mechanism 25 is provided in the melting furnace 1, and a steam nozzle 26 is arranged on the furnace ceiling 3. Although the combustion rate of the flammable waste 17 was improved by this, steam was blown into the high-temperature gas in the main chamber 9. Therefore, the burning rate of the combustible waste 17 did not increase to a satisfactory level.

【0005】そこで、本発明の目的は、上記の問題点を
解決し、可燃性廃棄物の燃焼を促進し、溶融炉の小型化
を可能とする手段を提供することにある。
Accordingly, an object of the present invention is to solve the above-mentioned problems, to provide means for promoting the combustion of combustible waste, and making the melting furnace compact.

【0006】[0006]

【課題を解決するための手段】〔各特徴手段〕上記の目
的のための本発明の廃棄物の溶融処理方法の第1特徴手
段は、請求項1に記載の如く、可燃性廃棄物を含む廃棄
物を被処理物として溶融炉に供給する第一工程と、前記
供給された被処理物を溶融処理する主室に導く第二工程
と、前記被処理物を弱酸化性雰囲気内で加熱して、前記
被処理物の表面を溶融させて溶融スラグを形成する第三
工程とからなる可燃性廃棄物の溶融処理方法において、
前記第二工程に先立ち、少なくとも前記可燃性廃棄物
に、予め水分を保有させる加湿工程と、前記第三工程に
おいて、前記主室内で前記可燃性廃棄物中の炭素と前記
保有させた水分との間の水性ガス化反応を誘発する水性
ガス化工程とを含み、前記水性ガス化反応に伴い生成し
た可燃性ガスを前記被処理物の表面及びその近傍で燃焼
させる点にある。つまり、前記第一工程に先立ち、或い
は前記第一工程と共に、又は、前記第一工程の後に前記
第二工程に先立ち、前記加湿工程を実施して、前記第三
工程に先だって、水分を、少なくとも前記可燃性廃棄物
に保有させておくのである。上記の目的のための本発明
の廃棄物の溶融処理方法の第2特徴手段は、請求項2に
記載の如く、前記第1特徴手段において、加湿工程を、
第一工程の後に、被処理物の全体に対して水を噴霧供給
し、前記被処理物に水分を保有させるようにしてある点
にある。つまり、前記被処理物に水分を保有させること
で、前記可燃性廃棄物に水分を保持させることを可能に
するのである。
Means for Solving the Problems The first characteristic means of the waste melting method of the present invention for the above purpose includes a combustible waste as defined in claim 1. A first step of supplying waste to the melting furnace as a treatment object, a second step of leading the supplied treatment object to a main chamber for melting treatment, and heating the treatment object in a weakly oxidizing atmosphere. And a third step of melting the surface of the object to form a molten slag, the method comprising:
Prior to the second step, at least the flammable waste, a humidifying step of retaining moisture in advance, and in the third step, the carbon in the combustible waste and the retained moisture in the main chamber in the main chamber A water gasification step of inducing a water gasification reaction between the two, wherein the combustible gas generated by the water gasification reaction is burned on the surface of the object to be treated and in the vicinity thereof. That is, prior to the first step, or together with the first step, or prior to the second step after the first step, performing the humidification step, prior to the third step, moisture, at least It is kept in the combustible waste. According to a second aspect of the present invention, there is provided a method of melting waste according to the first aspect, wherein the humidification step comprises:
After the first step, water is sprayed and supplied to the whole of the object to be treated, so that the object to be treated retains moisture. That is, it is possible to retain the moisture in the combustible waste by retaining the moisture in the object to be treated.

【0007】〔各特徴手段の作用効果〕上記第1特徴手
段によれば、可燃性廃棄物の燃焼速度を高めることがで
き、溶融炉の小型化が可能となる。つまり、高温度に維
持した弱酸化性雰囲気内で、廃棄物中の炭素分と保有水
分との間で水性ガス化反応を誘起すれば、生成する可燃
性ガスの燃焼速度は速く、その可燃性ガスが直ちに燃焼
を開始するから、その可燃性ガスの燃焼火炎に包囲され
る前記炭素分は急速に燃焼するようになる。従って、可
燃性廃棄物の燃焼速度を高めることができ、前記可燃性
廃棄物の炉内滞留時間を短くできる。その結果、前記可
燃性廃棄物が、燃焼速度が低い、乾留残さであるチャー
のみであっても、急速に燃焼させることが可能であり、
前記被処理物の炉内滞留時間を大きくする必要がなく、
前記堆積部の反応表面積も大きくする必要がないのであ
る。尚、上記第2特徴構成によれば、上記第1特徴構成
の作用効果を奏する中で、加湿工程の作業か簡単にな
る。つまり、可燃性廃棄物を選別して加湿する必要がな
いのである。また、溶融炉内において加湿されるから、
被処理物全体が雰囲気温度により加熱され、不燃性の被
処理物の保有する水分も蒸発し、前記可燃性廃棄物の保
有する水分と共に蒸気として前記可燃性廃棄物を包囲す
るようになる。さらに、炉内の閉鎖された空間内で加湿
されるから、前記被処理物は、加湿された状態を良好に
維持できるのである。その結果、前記水分が前記可燃性
廃棄物中の炭素分と容易に接触して、水性ガス化反応が
誘発されるのである。
[Function and Effect of Each Characteristic Means] According to the first characteristic means, the burning rate of combustible waste can be increased, and the melting furnace can be reduced in size. In other words, if a water gasification reaction is induced between the carbon content in the waste and the retained water in a weakly oxidizing atmosphere maintained at a high temperature, the burning rate of the flammable gas generated is high, Since the gas starts burning immediately, the carbon content surrounded by the combustion flame of the combustible gas rapidly burns. Therefore, the burning rate of the combustible waste can be increased, and the residence time of the combustible waste in the furnace can be shortened. As a result, the combustible waste has a low burning rate, even if it is only char that is a carbonized residue, it is possible to burn rapidly.
It is not necessary to increase the residence time of the object in the furnace,
It is not necessary to increase the reaction surface area of the deposition section. According to the second feature configuration, the operation of the humidification process is simplified while the operation and effect of the first feature configuration are exhibited. That is, there is no need to sort and humidify combustible waste. Also, because it is humidified in the melting furnace,
The entire object to be treated is heated by the ambient temperature, and the moisture contained in the non-combustible object evaporates, so that the combustible waste is surrounded as vapor together with the moisture contained in the combustible waste. Further, since the object is humidified in a closed space in the furnace, the object to be treated can be maintained in a humidified state. As a result, the water easily comes into contact with the carbon content in the combustible waste, and a water gasification reaction is induced.

【0008】〔各特徴構成〕上記の目的のための本発明
の廃棄物の溶融処理炉の第1特徴構成は、請求項3に記
載の如く、可燃性廃棄物を含む被処理物を蓄積する堆積
部と、前記堆積部から供給される被処理物を弱酸化性雰
囲気下で加熱溶融する主室と、前記主室の底部に、前記
被処理物の表面が溶融して生成した溶融スラグを排出す
るスラグ排出部とを設けてある可燃性廃棄物の溶融処理
炉において、前記被処理物を前記主室に供給する被処理
物供給部に、前記被処理物に水分を供給する水供給機構
を設けてある点にある。つまり、前記水供給機構から前
記被処理物に水分を供給することで、前記被処理物中の
前記可燃性廃棄物に対して水分を供給可能に構成してあ
る。尚、前記被処理物を区分けして前記可燃性廃棄物の
みに前記水分を供給するように前記水供給機構を構成す
ることもできる。尚、廃棄物の溶融処理炉の第2特徴構
成として、請求項4に記載の如く、前記第1特徴構成に
おける被処理物供給部を、堆積部に被処理物を投入する
投入部と前記堆積部とで構成し、前記投入部に水供給機
構を設けてあることが好ましい。また、溶融処理炉の第
3特徴構成として、請求項5に記載の如く、前記第1特
徴構成における溶融炉を、固定された内筒と、前記内筒
と同軸心回りに回転駆動自在で、底部を備える外筒とで
構成し、前記内筒に備える炉天井部と前記外筒に備える
前記底部との間に主室を形成して、前記内筒と前記外筒
との間の環状空間の天井部に前記投入部を設けると共
に、前記天井部に堆積部に向けて水を噴霧して被処理物
に水分を供給する水噴霧機構を設けて、前記水供給機構
を構成してあればさらによい。
According to a first aspect of the present invention, there is provided a waste melting treatment furnace for accumulating an object to be treated including combustible waste. A deposition section, a main chamber that heats and melts the object to be supplied supplied from the deposition section under a weakly oxidizing atmosphere, and a molten slag generated by melting the surface of the object to be processed at the bottom of the main chamber. A slag discharge unit for discharging the flammable waste in a melting processing furnace provided with a slag discharge unit, and a water supply mechanism for supplying moisture to the processing object to a processing object supply unit for supplying the processing object to the main chamber. Is provided. That is, by supplying water to the object to be treated from the water supply mechanism, water can be supplied to the combustible waste in the object to be treated. In addition, the water supply mechanism may be configured to divide the object to be treated and supply the moisture only to the combustible waste. As a second characteristic configuration of the waste melting furnace, the processing object supply unit in the first characteristic configuration may be a charging unit for charging a processing object into a deposition unit and the deposition unit. And a water supply mechanism is preferably provided in the charging section. As a third characteristic configuration of the melting processing furnace, as described in claim 5, the melting furnace in the first characteristic configuration can be rotatably driven around a fixed inner cylinder and a coaxial center with the inner cylinder, A main chamber is formed between a furnace ceiling provided in the inner cylinder and the bottom provided in the outer cylinder, and an annular space is provided between the inner cylinder and the outer cylinder. In addition to providing the charging section on the ceiling portion, and providing a water spray mechanism for supplying water to the object to be processed by spraying water toward the deposition section on the ceiling portion, if the water supply mechanism is configured Even better.

【0009】〔各特徴構成の作用効果〕上記第1特徴構
成によれば、上記第1特徴手段のもたらす作用効果を実
現できる。つまり、被処理物供給部に水供給機構を設け
てあるから、主室内で可燃性廃棄物中の炭素と、前記水
供給機構から供給して少なくとも前記可燃性廃棄物に保
有させた水分との間の水性ガス化反応を誘発する水性ガ
ス化工程を前記主室内で実施できるのである。当然、前
記可燃性廃棄物以外の前記被処理物の保有する水分も炉
内で蒸発して水蒸気となり、この水蒸気が前記水性ガス
化反応にあずかり得るのである。従って、前記主室にお
ける高温度に維持した弱酸化性雰囲気内で、廃棄物中の
炭素分と前記被処理物の保有水分との間で水性ガス化反
応を誘起すれば、生成する可燃性ガスの燃焼速度は速
く、その可燃性ガスが直ちに燃焼を開始するから、その
可燃性ガスの燃焼火炎に包囲される前記炭素分は急速に
燃焼するのである。その結果、可燃性廃棄物の燃焼速度
を高めることができ、前記可燃性廃棄物の炉内滞留時間
を短くでき、前記被処理物の堆積部における前記主室に
おける反応表面積を大きくする必要がなく、溶融炉の小
型化が可能となるのである。尚、上記第2特徴構成によ
れば、上記第1特徴手段のもたらす作用効果を奏する中
で、第一工程に先立って加湿工程を実施することが可能
となる。つまり、投入部に水供給機構を設けることで、
堆積部への被処理物の投入に先立って前記被処理物に水
分を供給することができ、加湿した前記被処理物を炉内
に投入して、予め水分を保有させた前記被処理物からな
る前記堆積部を形成できる。従って、投入前の被処理物
の性状に適合した含水量に調整でき、上記第1特徴手段
における水性ガス化工程を円滑に進行させることが可能
になる。さらに、上記第3特徴構成によれば、前記第2
特徴手段の奏する作用効果を実現できる。つまり、堆積
部上方の、前記堆積部に対して相対回転する天井部に水
供給機構としての水噴霧機構を設けてあるから、前記堆
積部に対して満遍なく水分を噴霧供給でき、前記堆積部
の全周にわたって、被処理物が良好に加湿された状態を
維持できる。前記水噴霧機構は、前記天井部の一カ所に
設けられてあってもよいが、複数箇所に設けてあれば、
前記堆積部の全周にわたって、均一な加湿状態とするこ
とができる。従って、上記第2特徴手段における作用効
果を発揮させ得るのである。
[Functions and Effects of Each Characteristic Configuration] According to the first characteristic configuration, the functions and effects provided by the first characteristic means can be realized. That is, since the water supply mechanism is provided in the processing object supply unit, the carbon in the combustible waste in the main chamber and the water supplied from the water supply mechanism and held in at least the combustible waste A water gasification step for inducing a water gasification reaction during the reaction can be performed in the main chamber. Naturally, the water content of the object to be treated other than the combustible waste is also evaporated in the furnace to form steam, and this steam can participate in the water gasification reaction. Therefore, if a water gasification reaction is induced between the carbon content of the waste and the water content of the object to be treated in a weakly oxidizing atmosphere maintained at a high temperature in the main chamber, the flammable gas generated Since the combustion speed of the combustible gas is high and the combustible gas starts burning immediately, the carbon content surrounded by the combustion flame of the combustible gas burns rapidly. As a result, the burning rate of combustible waste can be increased, the residence time of the combustible waste in the furnace can be shortened, and it is not necessary to increase the reaction surface area in the main chamber in the deposition section of the object to be treated. Thus, the size of the melting furnace can be reduced. According to the second characteristic configuration, the humidifying step can be performed prior to the first step, while the operation and effect provided by the first characteristic means are exhibited. In other words, by providing a water supply mechanism in the charging section,
Moisture can be supplied to the object to be processed prior to the input of the object to the deposition unit, and the humidified object to be processed is charged into the furnace, and the humidified object is stored in advance. The said deposition part can be formed. Therefore, the water content can be adjusted to a property suitable for the property of the object before being charged, and the water gasification step in the first characteristic means can smoothly proceed. Further, according to the third characteristic configuration, the second
The operation and effect of the characteristic means can be realized. In other words, since a water spray mechanism as a water supply mechanism is provided on the ceiling above the stacking section and relatively rotated with respect to the stacking section, water can be uniformly sprayed and supplied to the stacking section. It is possible to maintain the state in which the object to be processed is well humidified over the entire circumference. The water spray mechanism may be provided at one place of the ceiling, but if provided at a plurality of places,
A uniform humidified state can be achieved over the entire circumference of the deposition section. Therefore, the operation and effect of the second characteristic means can be exhibited.

【0010】[0010]

【発明の実施の形態】上記本発明の廃棄物の溶融処理方
法及び溶融処理装置の実施の形態の一例について、以下
に、図面を参照しながら説明する。図1は本発明に係る
溶融炉の一例を示す要部の縦断面図であり、図2はその
炉操業の一例を示す工程説明図である。尚、前記従来の
技術において説明した要素と同じ要素並びに同等の機能
を有する要素に関しては、先の図6及び図7に付したと
同一の符号を付し、詳細の説明の一部は省略する。
BRIEF DESCRIPTION OF THE DRAWINGS FIG. 1 is a block diagram showing an embodiment of a waste treatment method and a waste treatment apparatus according to the present invention. FIG. 1 is a longitudinal sectional view of an essential part showing an example of a melting furnace according to the present invention, and FIG. 2 is a process explanatory view showing an example of the furnace operation. The same elements as those described in the related art and elements having the same functions are denoted by the same reference numerals as those in FIGS. 6 and 7, and a part of the detailed description is omitted. .

【0011】廃棄物の溶融処理炉においては、図1に示
すように、溶融炉1を、固定された内筒2と、前記内筒
2と同軸心回りに回転駆動自在で、前記底部8を備える
外筒7とで構成し、前記内筒2に備える炉天井部3と前
記外筒7に備える前記底部8との間に前記主室9を形成
する。前記内筒2と前記外筒7との間の環状空間の、前
記主室9の底部8上に、可燃性廃棄物17を含む被処理
物15を蓄積する堆積部Sと、前記内筒2と前記外筒7
との間の環状空間の環状天井部6に、前記被処理物15
を前記堆積部Sに供給する投入部11を設けて、前記投
入部11と前記堆積部Sとで、前記被処理物15を前記
主室9に供給する被処理物供給部10を形成する。前記
底部8には、前記被処理物15が溶融して生成した溶融
スラグ24を排出するスラグ排出部8aとを設ける。前
記主室9では、前記堆積部Sから供給される被処理物1
5の擂り鉢形に形成される表面Fを、弱酸化性雰囲気下
で加熱溶融する。前記表面Fが溶融して生成した溶融ス
ラグ24は、前記スラグ排出部8aから下方に設けられ
たスラグピット(図示省略)に向けて滴下する。
In the waste melting furnace, as shown in FIG. 1, a melting furnace 1 is rotatably driven around a fixed inner cylinder 2 and a coaxial center with the inner cylinder 2, and the bottom portion 8 is The main chamber 9 is formed between the furnace ceiling 3 provided in the inner cylinder 2 and the bottom 8 provided in the outer cylinder 7. A stacking section S for accumulating a treatment object 15 including a combustible waste 17 on a bottom portion 8 of the main chamber 9 in an annular space between the inner cylinder 2 and the outer cylinder 7; And the outer cylinder 7
The object to be treated 15 is placed on the annular ceiling 6 of the annular space between
Is provided to the deposition unit S, and the workpiece supply unit 10 that supplies the workpiece 15 to the main chamber 9 is formed by the charging unit 11 and the deposition unit S. The bottom portion 8 is provided with a slag discharge portion 8a for discharging a molten slag 24 generated by melting the workpiece 15. In the main chamber 9, the workpiece 1 supplied from the deposition section S
The surface F formed in the mortar shape of No. 5 is heated and melted in a weakly oxidizing atmosphere. The molten slag 24 generated by melting the surface F is dropped from the slag discharge portion 8a toward a slag pit (not shown) provided below.

【0012】前記被処理物供給部10には水供給機構1
4を設けるが、これは、前記被処理物15中の前記可燃
性廃棄物17に水分を保有させるためのもので、前記水
供給機構14は、前記堆積部Sに水を噴霧供給する水噴
霧機構14Aを前記環状天井部6に設けて構成してある
ことが好ましい。これは、本発明に係る溶融炉1におい
ては、前記内筒2が固定してあり、前記外筒7が前記内
筒の2の軸心回りに回転駆動されるから、前記環状天井
部6が前記堆積部S上を相対回転するので、前記水噴霧
機構14Aを前記環状天井部6に固定して配置してある
ことで、前記堆積部Sの投入部11側の環状に形成され
る受入側表面16に満遍なく水分が供給されるのであ
る。しかも、前記堆積部Sが閉鎖された空間内に保持さ
れているから、供給された水分による保湿条件を維持で
きるのである。尚、前記水供給機構14からの水供給量
は、前記投入部11に設けた被処理物供給装置12に付
設した計量機構12aによって前記被処理物15の投入
量を検量し、その投入量に適合する水供給量を設定する
水供給量調節手段14aを設けておくことが好ましい。
前記水供給量は、前記可燃性廃棄物17としてチャー即
ち固定炭素を供給する場合には、そのチャーに対して、
5〜10%とすることが望ましい。これより少ない水を
供給した場合には、前記チャーが完全に水性ガス化反応
にあずからず、未燃炭素分を残存させる場合があり、ま
た、前記水分量が多すぎれば、その過剰な水分の蒸発潜
熱を奪われて炉内温度の低下を招き、水性ガス化反応が
安定して起こらなくなる場合がある。因みに、5乃至1
0%の水分を含有するチャーは、団塊化しにくく、且
つ、さらさらとした小さな固まりの集まりとなって取り
扱いやすい状態になる。
A water supply mechanism 1 is provided in the workpiece supply section 10.
4 is provided for keeping the combustible waste 17 in the object 15 to retain water, and the water supply mechanism 14 is used to supply and supply water to the accumulation section S. It is preferable that a mechanism 14A is provided on the annular ceiling 6. This is because, in the melting furnace 1 according to the present invention, since the inner cylinder 2 is fixed and the outer cylinder 7 is driven to rotate around the axis of the inner cylinder 2, the annular ceiling 6 is Since the water spray mechanism 14A is fixed to the annular ceiling 6 so as to relatively rotate on the stacking section S, the receiving side of the stacking section S is formed in an annular shape on the input section 11 side. Water is evenly supplied to the surface 16. In addition, since the deposition portion S is held in the closed space, it is possible to maintain the moisturizing condition by the supplied moisture. The amount of water supplied from the water supply mechanism 14 is determined by measuring the input amount of the processing object 15 by a measuring mechanism 12a attached to the processing object supply device 12 provided in the input section 11, and calculating the input amount. It is preferable to provide a water supply amount adjusting means 14a for setting a suitable water supply amount.
When supplying the char, that is, fixed carbon as the combustible waste 17, the water supply amount is:
It is desirable to set it to 5 to 10%. If less water is supplied, the char may not completely participate in the water gasification reaction and may leave unburned carbon, and if the amount of water is too large, the excess water In some cases, the latent heat of vaporization is deprived and the temperature inside the furnace is lowered, and the water gasification reaction may not stably occur. By the way, 5 to 1
The char containing 0% of water is hard to agglomerate, and becomes a state of easy to handle as a collection of small clumps.

【0013】以上のように構成される廃棄物の溶融処理
炉においては、例えば図2に示すように、被処理物供給
部10の投入部11に設けた被処理物供給装置12によ
って可燃性廃棄物17を含む廃棄物を被処理物15とし
て溶融炉1の堆積部Sに供給する第一工程と、前記供給
された被処理物15を、前記堆積部Sから溶融処理する
主室9に導く第二工程と、前記主室9内において前記被
処理物15を弱酸化性雰囲気内で加熱して、前記被処理
物15の表面Fを溶融させて溶融スラグを形成する第三
工程とが、順次連続的に実施される。
In the waste melting furnace configured as described above, for example, as shown in FIG. 2, flammable waste is supplied by a workpiece supply device 12 provided at an input section 11 of a workpiece supply section 10. A first step of supplying the waste containing the object 17 as the object to be processed 15 to the deposition section S of the melting furnace 1, and guiding the supplied object to be processed 15 from the deposition section S to the main chamber 9 for performing the melting process. A second step, and a third step of heating the workpiece 15 in a weakly oxidizing atmosphere in the main chamber 9 to melt the surface F of the workpiece 15 to form a molten slag; It is performed sequentially and continuously.

【0014】ここで、水供給機構14として水噴霧機構
14Aを前記堆積部S上方の環状天井部6に設けてある
から、前記第一工程の後、前記被処理物15の全体に対
して、前記第二工程に先立ち水を噴霧供給し、前記被処
理物15に前記水分を保有させることで、少なくとも可
燃性廃棄物17に、予め水分を保有させる加湿工程が実
施されるようになる。また、前記堆積部Sの前記主室9
内の表面Fに、こうして前記可燃性廃棄物17が水分を
保有した状態で供給されることで、前記第三工程におい
て、前記主室9内で前記可燃性廃棄物17中の炭素と前
記保有させた水分との間の水性ガス化反応を誘発する水
性ガス化工程が実施され、前記水性ガス化反応に伴い生
成した可燃性ガスを前記被処理物15の表面F及びその
近傍で燃焼させることができる。尚、前記可燃性廃棄物
17が揮発成分を含有する場合には、前記加湿工程にお
いて、前記被処理物15に保有させる水分量は、前記可
燃性廃棄物17中の乾留後の炭素分に対して5〜10%
の水分に相当する量であればよい。
Here, a water spray mechanism 14A is provided as a water supply mechanism 14 on the annular ceiling section 6 above the accumulation section S, so that after the first step, the entire processing object 15 is By spraying and supplying water prior to the second step and causing the object 15 to retain the moisture, the humidifying step of retaining the moisture in at least the combustible waste 17 is performed. Further, the main chamber 9 of the deposition section S
The combustible waste 17 is supplied to the inner surface F in this manner while retaining moisture, so that in the third step, the carbon in the combustible waste 17 and the retained carbon are contained in the main chamber 9. A water gasification step for inducing a water gasification reaction with the let-off moisture is performed, and combustible gas generated by the water gasification reaction is burned on the surface F of the article 15 to be processed and its vicinity. Can be. In the case where the combustible waste 17 contains a volatile component, the amount of water held in the treatment target 15 in the humidification step is based on the carbon content of the combustible waste 17 after carbonization in the combustible waste 17. 5-10%
The amount may be any amount corresponding to the water content.

【0015】以上の構成により、前記可燃性廃棄物17
が熱分解されて生成する固形炭素分を取り巻いて、前記
可燃性ガスが燃焼するから、前記固形炭素分の燃焼が促
進され、溶融処理速度がきわめて高くなる。従って、前
記堆積部Sにおける前記被処理物13の反応表面である
前記表面Fの面積を小さくでき、その結果、前記溶融処
理速度が高いことと相俟って、前記溶融炉1は小型に形
成できるのである。
With the above configuration, the combustible waste 17
Since the flammable gas burns around the solid carbon generated by thermal decomposition, the combustion of the solid carbon is promoted, and the melting processing speed becomes extremely high. Therefore, the area of the surface F, which is the reaction surface of the workpiece 13 in the deposition section S, can be reduced, and as a result, the melting furnace 1 is formed in a small size in combination with the high melting processing speed. You can.

【0016】次に、本発明の他の実施の形態について説
明する。 〈1〉上記実施の形態に於いては、溶融炉1を、固定さ
れた内筒2と、前記内筒2と同軸心回りに回転駆動自在
で、前記底部8を備える外筒7とで構成し、前記内筒2
に備える炉天井部3と前記外筒7に備える前記底部8と
の間に前記主室9を形成する例について説明したが、前
記外筒7も前記内筒2に対して固定されたものであって
もよい。但しこの場合には、水供給機構14は、堆積部
Sに満遍なく水を供給できるように構成するか、被処理
物供給部10の投入部11の前に設けることが好まし
い。 〈2〉上記実施の形態に於いては、投入部11に被処理
物供給装置12を設ける例について図示説明したが、前
記被処理物供給装置12に代えて、単にシールダンパの
みを備える受入ホッパを設けてあるだけでもよい。 〈3〉上記実施の形態に於いては、堆積部Sに水を噴霧
供給する水噴霧機構14Aを環状天井部6に設けて、水
供給機構14を構成する例について説明したが、前記水
供給機構14は、堆積部Sに水を滴下供給するように構
成してあってもよい。また、例えば図3に示すように、
前記水供給機構14を被処理物供給部10の投入部11
に備える被処理物供給装置12に設けて、投入される被
処理物15の全体に水分を供給して、可燃性廃棄物17
のみならず不燃性の被処理物にも水分を保有させるよう
にしてもよい。さらに、前記被処理物供給装置12に至
るまでに前記被処理物15に水分を添加しておいてもよ
い。このようにすれば、前記不燃性の被処理物15の保
有する水分が炉内の熱により蒸発し、水蒸気となって前
記可燃性廃棄物17を包囲することになり、水性ガス化
反応を促進できる場合がある。さらに、前記可燃性廃棄
物17をバッチ投入する場合には、上記第一工程に先立
ち、前記被処理物供給部10の前段に前記水供給機構1
4を配置して、前記可燃性廃棄物17を湿潤させておい
て、前記投入部11に供給することも可能である。この
ように構成すれば、前記可燃性廃棄物17を区分して、
前記可燃性廃棄物17のみに水分を添加することも可能
であり、前記可燃性廃棄物17に保有させる水分の調整
が容易になる。 〈4〉つまり、上記実施の形態に於いては、第一工程と
第二工程との間に加湿工程を実施する例について説明し
たが、前記加湿工程は、前記第二工程の前であればよい
のであって、例えば図3に示した溶融炉を用いて、図4
に示すように、前記第一工程の中で前記加湿工程を実施
してもよく、また、例えば図5に示すように、前記第一
工程に先立って前記加湿工程を実施してもよいのであ
る。
Next, another embodiment of the present invention will be described. <1> In the above embodiment, the melting furnace 1 is composed of the fixed inner cylinder 2 and the outer cylinder 7 that is rotatable around the same axis as the inner cylinder 2 and that has the bottom 8. And the inner cylinder 2
Although the example in which the main chamber 9 is formed between the furnace ceiling 3 provided in the above and the bottom 8 provided in the outer cylinder 7 has been described, the outer cylinder 7 is also fixed to the inner cylinder 2. There may be. However, in this case, it is preferable that the water supply mechanism 14 be configured to supply water evenly to the deposition unit S, or to be provided before the charging unit 11 of the workpiece supply unit 10. <2> In the above embodiment, the example in which the workpiece supply device 12 is provided in the charging section 11 has been illustrated and described. However, instead of the workpiece supply device 12, a receiving hopper including only a seal damper is provided. May be provided. <3> In the above embodiment, an example was described in which the water supply mechanism 14 was configured by providing the water spray mechanism 14A for spraying and supplying water to the deposition section S on the annular ceiling section 6; The mechanism 14 may be configured to supply water dropwise to the deposition unit S. Also, for example, as shown in FIG.
The water supply mechanism 14 is connected to the input section 11 of the workpiece supply section 10.
Is provided in the processing object supply device 12 provided in the apparatus, and supplies moisture to the whole of the processing object 15 to be thrown in.
In addition, moisture may be retained in the nonflammable workpiece. Further, moisture may be added to the workpiece 15 before reaching the workpiece supply device 12. In this way, the moisture contained in the non-combustible object 15 evaporates due to the heat in the furnace and becomes steam, which surrounds the combustible waste 17 and promotes the water gasification reaction. May be possible. Further, when the combustible waste 17 is batch-injected, the water supply mechanism 1 is provided upstream of the workpiece supply unit 10 prior to the first step.
It is also possible to dispose the fuel tank 4 and to supply the combustible waste 17 to the charging section 11 while keeping the combustible waste 17 wet. With this configuration, the combustible waste 17 is divided and
It is possible to add water only to the flammable waste 17, and it is easy to adjust the water to be retained in the flammable waste 17. <4> That is, in the above embodiment, an example in which the humidification step is performed between the first step and the second step has been described. However, the humidification step may be performed before the second step. For example, using the melting furnace shown in FIG.
As shown in FIG. 5, the humidification step may be performed in the first step, or, for example, as shown in FIG. 5, the humidification step may be performed prior to the first step. .

【0017】尚、特許請求の範囲の項に図面との対照を
便利にするために符号を記すが、該記入により本発明は
添付図面の構成に限定されるものではない。
In the claims, reference numerals are provided for convenience of comparison with the drawings, but the present invention is not limited to the configuration shown in the attached drawings.

【図面の簡単な説明】[Brief description of the drawings]

【図1】本発明に係る溶融処理炉の一例を示す要部縦断
面図
FIG. 1 is a longitudinal sectional view of an essential part showing an example of a melting furnace according to the present invention.

【図2】本発明に係る廃棄物の溶融処理方法の一例を説
明する流れ図
FIG. 2 is a flowchart illustrating an example of a waste melting method according to the present invention.

【図3】本発明に係る溶融処理炉の他の例を示す要部縦
断面図
FIG. 3 is a longitudinal sectional view showing a main part of another example of the melting furnace according to the present invention.

【図4】本発明に係る廃棄物の溶融処理方法の他の例を
説明する流れ図
FIG. 4 is a flowchart illustrating another example of the waste melting method according to the present invention.

【図5】本発明に係る廃棄物の溶融処理方法の他の例を
説明する流れ図
FIG. 5 is a flowchart illustrating another example of the waste melting method according to the present invention.

【図6】従来の溶融処理炉の一例を示す要部の一部切り
欠き斜視図
FIG. 6 is a partially cutaway perspective view of an essential part showing an example of a conventional melting processing furnace.

【図7】従来の溶融処理炉の他の例を示す要部の一部切
り欠き斜視図
FIG. 7 is a partially cutaway perspective view of a main part showing another example of a conventional melting processing furnace.

【符号の説明】[Explanation of symbols]

1 溶融炉 2 内筒 3 炉天井部 4 環状天井部 5 外筒 6 底部 6a スラグ排出部 7 主室 8 被処理物供給部 9 投入部 12 水供給機構 13 被処理物 15 可燃性廃棄物 F 被処理物の表面 S 堆積部 DESCRIPTION OF SYMBOLS 1 Melting furnace 2 Inner cylinder 3 Furnace ceiling part 4 Annular ceiling part 5 Outer cylinder 6 Bottom part 6a Slag discharge part 7 Main chamber 8 Treatment supply part 9 Input part 12 Water supply mechanism 13 Treatment part 15 Combustible waste F Cover Surface of treated material S Deposit

Claims (5)

【特許請求の範囲】[Claims] 【請求項1】 可燃性廃棄物(17)を含む廃棄物を被
処理物(15)として溶融炉(1)に供給する第一工程
と、前記供給された被処理物(15)を溶融処理する主
室(9)に導く第二工程と、前記被処理物(15)を弱
酸化性雰囲気内で加熱して、前記被処理物(15)の表
面(F)を溶融させて溶融スラグを形成する第三工程と
からなる可燃性廃棄物の溶融処理方法であって、 前記第二工程に先立ち、少なくとも前記可燃性廃棄物
(17)に、予め水分を保有させる加湿工程と、前記第
三工程において、前記主室(9)内で前記可燃性廃棄物
(17)中の炭素と前記保有させた水分との間の水性ガ
ス化反応を誘発する水性ガス化工程とを含み、前記水性
ガス化反応に伴い生成した可燃性ガスを前記被処理物
(15)の表面(F)及びその近傍で燃焼させる可燃性
廃棄物の溶融処理方法。
1. A first step of supplying waste containing combustible waste (17) to a melting furnace (1) as an object to be treated (15), and melting the supplied object to be treated (15). A second step of leading to the main chamber (9) to be treated, and heating the object (15) in a weakly oxidizing atmosphere to melt the surface (F) of the object (15) to remove molten slag. A humidifying method for melting a combustible waste, comprising: a humidifying step of preliminarily holding moisture in at least the combustible waste (17) prior to the second step. A water gasification step of inducing a water gasification reaction between the carbon in the combustible waste (17) and the retained moisture in the main chamber (9). The combustible gas generated by the conversion reaction is transferred to the surface (F) of the object (15) and the Melt processing method of the combustible waste is burned in the vicinity.
【請求項2】 前記第一工程の後、前記加湿工程とし
て、前記被処理物(15)の全体に対して水を噴霧供給
し、前記被処理物(15)に前記水分を保有させる請求
項1記載の可燃性廃棄物の溶融処理方法。
2. After the first step, as the humidification step, water is spray-supplied to the entire object to be treated (15) so that the object (15) retains the moisture. A method for melting combustible waste according to claim 1.
【請求項3】 可燃性廃棄物(17)を含む被処理物
(15)を蓄積する堆積部(S)と、前記堆積部(S)
から供給される被処理物(15)を弱酸化性雰囲気下で
加熱溶融する主室(9)と、前記主室(9)の底部
(8)に、前記被処理物(15)の表面(F)が溶融し
て生成した溶融スラグを排出するスラグ排出部(8a)
とを設けてある可燃性廃棄物の溶融処理炉であって、 前記被処理物(15)を前記主室(9)に供給する被処
理物供給部(10)に、前記被処理物(15)に水分を
供給する水供給機構(14)を設けてある可燃性廃棄物
の溶融処理炉。
3. A deposition section (S) for accumulating an object to be treated (15) containing combustible waste (17), and said deposition section (S).
A main chamber (9) for heating and melting an object to be treated (15) supplied from a weak oxidizing atmosphere and a bottom (8) of the main chamber (9) are provided on the surface ( A slag discharge section (8a) for discharging molten slag generated by melting F)
And a melting processing furnace for combustible waste provided with: a processing object supply section (10) for supplying the processing object (15) to the main chamber (9); A) a combustible waste melting processing furnace provided with a water supply mechanism (14) for supplying water to the combustible waste.
【請求項4】 前記被処理物供給部(10)を、前記堆
積部(S)に前記被処理物(15)を投入する投入部
(11)と前記堆積部(S)とで構成し、前記投入部
(11)に前記水供給機構(14)を設けてある請求項
3記載の可燃性廃棄物の溶融処理炉。
4. The processing object supply section (10) includes an input section (11) for inputting the processing object (15) into the deposition section (S) and the deposition section (S), The furnace for melting combustible waste according to claim 3, wherein the water supply mechanism (14) is provided in the charging section (11).
【請求項5】 前記溶融炉(1)を、固定された内筒
(2)と、前記内筒(2)と同軸心回りに回転駆動自在
で、前記底部(8)を備える外筒(7)とで構成し、前
記内筒(2)に備える炉天井部(3)と前記外筒(7)
に備える前記底部(8)との間に前記主室(9)を形成
して、前記内筒(2)と前記外筒(7)との間の環状空
間の環状天井部(6)に前記投入部(11)を設け、前
記堆積部(S)に水を噴霧供給する水噴霧機構(14
A)を前記環状天井部(6)に設けて、前記水供給機構
(14)を構成してある請求項3記載の可燃性廃棄物の
溶融処理炉。
5. An outer cylinder (7) having a fixed inner cylinder (2) and a rotatable drive around a coaxial center with the inner cylinder (2) and having the bottom (8). ), And a furnace ceiling part (3) provided in the inner cylinder (2) and the outer cylinder (7).
The main chamber (9) is formed between the inner chamber (2) and the outer cylinder (7), and the main chamber (9) is formed between the inner cylinder (2) and the outer cylinder (7). A water spray mechanism (14) for providing an injection section (11) and spraying and supplying water to the deposition section (S);
The furnace for melting combustible waste according to claim 3, wherein A) is provided on the annular ceiling (6) to constitute the water supply mechanism (14).
JP11149312A 1999-05-28 1999-05-28 Melting method and furnace for combustible waste Pending JP2000337616A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP11149312A JP2000337616A (en) 1999-05-28 1999-05-28 Melting method and furnace for combustible waste

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP11149312A JP2000337616A (en) 1999-05-28 1999-05-28 Melting method and furnace for combustible waste

Publications (1)

Publication Number Publication Date
JP2000337616A true JP2000337616A (en) 2000-12-08

Family

ID=15472380

Family Applications (1)

Application Number Title Priority Date Filing Date
JP11149312A Pending JP2000337616A (en) 1999-05-28 1999-05-28 Melting method and furnace for combustible waste

Country Status (1)

Country Link
JP (1) JP2000337616A (en)

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US7465018B2 (en) 2003-01-13 2008-12-16 Only The First Limited Technium Digital Printing system
JP2010216733A (en) * 2009-03-17 2010-09-30 Kubota Corp Waste treatment facility and waste treatment method
JP2012232864A (en) * 2011-04-28 2012-11-29 Kubota Corp Method for producing fertilizer and rotary surface melting furnace used in the same
EP3124864A4 (en) * 2014-03-28 2017-11-15 Kubota Corporation Surface melting furnace and method for operating surface melting furnace

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US7465018B2 (en) 2003-01-13 2008-12-16 Only The First Limited Technium Digital Printing system
JP2010216733A (en) * 2009-03-17 2010-09-30 Kubota Corp Waste treatment facility and waste treatment method
JP2012232864A (en) * 2011-04-28 2012-11-29 Kubota Corp Method for producing fertilizer and rotary surface melting furnace used in the same
EP3124864A4 (en) * 2014-03-28 2017-11-15 Kubota Corporation Surface melting furnace and method for operating surface melting furnace

Similar Documents

Publication Publication Date Title
US5005493A (en) Hazardous waste multi-sectional rotary kiln incinerator
JP6813249B2 (en) Carbonization equipment and carbonization method for woody biomass
JP3034467B2 (en) Direct-type incineration ash melting treatment equipment and treatment method
EA026470B1 (en) Method for supplying combustion air in vertical incinerator and vertical incinerator
JP6198572B2 (en) Hot-air generator with solid fuel as the main fuel
JPH11286684A (en) Continuous carbonization furnace
JP2000337616A (en) Melting method and furnace for combustible waste
JP2007322099A (en) Dry distillation gasification combustion furnace
CN100519698C (en) Continuously carbonating method and apparatus
US5836258A (en) Method and apparatus for incinerating waste material using oxygen injection
JPH06247784A (en) Rotary heat-treating furnace
JP5311810B2 (en) Radioactive miscellaneous solid waste incinerator
JP3852040B2 (en) Waste gasification incinerator combustion method
RU2265774C1 (en) Method and device for treating solid waste
JP3858250B2 (en) Method for melting waste pyrolysis residue or incineration residue containing combustible solid carbon
JP2022021448A (en) Method for inputting waste into incinerator
JP2880425B2 (en) Waste incineration method
JP2022021001A (en) Boiler sewage treatment method
JP2004044894A (en) Fire grate type waste incinerator and its operating method
JPS6158113B2 (en)
JPH08178239A (en) Melting furnace
JP2003194319A (en) Rotary combustion method, rotary combustion device and heat treatment facility
JPH11211033A (en) Waste disposal plant and combustion method thereof
JPH0814524A (en) Waste liquor treating apparatus
JPS63297910A (en) Nox control method in step incinerator

Legal Events

Date Code Title Description
A977 Report on retrieval

Free format text: JAPANESE INTERMEDIATE CODE: A971007

Effective date: 20051209

A131 Notification of reasons for refusal

Free format text: JAPANESE INTERMEDIATE CODE: A131

Effective date: 20051215

A02 Decision of refusal

Free format text: JAPANESE INTERMEDIATE CODE: A02

Effective date: 20060406