JP2007225125A - Scattering asbestos melting treatment device - Google Patents

Scattering asbestos melting treatment device Download PDF

Info

Publication number
JP2007225125A
JP2007225125A JP2006031626A JP2006031626A JP2007225125A JP 2007225125 A JP2007225125 A JP 2007225125A JP 2006031626 A JP2006031626 A JP 2006031626A JP 2006031626 A JP2006031626 A JP 2006031626A JP 2007225125 A JP2007225125 A JP 2007225125A
Authority
JP
Japan
Prior art keywords
heat medium
combustion
furnace
heated
heated object
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
JP2006031626A
Other languages
Japanese (ja)
Inventor
Masahito Sasaki
雅仁 佐々木
Hideo Ota
英夫 太田
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.)
Individual
Original Assignee
Individual
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 Individual filed Critical Individual
Priority to JP2006031626A priority Critical patent/JP2007225125A/en
Publication of JP2007225125A publication Critical patent/JP2007225125A/en
Pending legal-status Critical Current

Links

Images

Landscapes

  • Incineration Of Waste (AREA)
  • Processing Of Solid Wastes (AREA)
  • Vertical, Hearth, Or Arc Furnaces (AREA)

Abstract

<P>PROBLEM TO BE SOLVED: To provide a scattering asbestos melting treatment device capable of simultaneously melting substances different in melting points, improving energy efficiency, and reducing construction cost so that a furnace is not blocked by preventing the fusion of a melted heated object to a heat medium, related to scattering asbestos treatment in an internal-combustion fluid bed furnace. <P>SOLUTION: The unfluidized heat medium is placed in a combustion atmosphere by a mixture gas of gas and air, and melting treatment is performed by allowing the heated object to pass through the heat medium heated to a high temperature. A furnace temperature is controlled at high accuracy so that the heat medium and a furnace wall are not melted and damaged by excess combustion and abnormal combustion. The heated object is finely granulated so that high heat energy can be efficiently applied to the heated object. <P>COPYRIGHT: (C)2007,JPO&INPIT

Description

本発明は、飛散性アスベストを溶融無害化したり、その他の微粉体を溶融させたり、有毒ガスや悪臭を無害化無臭化する内燃式熱媒体燃焼炉に関する。  The present invention relates to an internal combustion type heat medium combustion furnace that melts detoxified asbestos, melts other fine powders, detoxifies toxic gases and odors, and does not bromide.

微粒中空ガラス球の製造装置として内燃式流動床炉があり、セラミック系熱媒体から発する輻射熱により微粉体を高温加熱する装置である。熱媒体を流動化状態にして、それを通過する被加熱体を瞬間高温加熱する。  There is an internal combustion fluidized bed furnace as an apparatus for producing fine hollow glass spheres, which heats fine powders at a high temperature by radiant heat generated from a ceramic heat medium. The heating medium is fluidized, and the heated object passing through it is instantaneously heated to a high temperature.

高温に加熱された固体の熱媒体からは大量の熱エネルギ−が被加熱体に与えられ、電気炉や、加熱バ−ナ−のような気体雰囲気による加熱よりも、被加熱体の融点を低くすることができる。  A solid heat medium heated to a high temperature gives a large amount of heat energy to the object to be heated, and the melting point of the object to be heated is lower than that in a gas atmosphere such as an electric furnace or a heating burner. can do.

なお、本発明に関連する公知技術として次の特許文献1を挙げることができる。  In addition, the following patent document 1 can be mentioned as a well-known technique relevant to this invention.

特開平11−011960  JP 11-011960 A

内燃式流動床炉は、熱媒体を流動化させるので熱媒体に溶融した被加熱体が融着した場合、熱媒体の流動が止まり、かつ炉の燃焼が止まったり炉が閉塞したりする。炉内温度設定や炉内温度自体が被加熱体の融点を超えた場合に、この現象は起こる。したがって飛散性アスベスト製品のような多種多様な物質で構成される被加熱体を内燃式流動床炉で同時に溶融処理することは困難である。また、最適溶融炉内温度の決定も困難である。  In the internal combustion fluidized bed furnace, since the heat medium is fluidized, when the heated object melted in the heat medium is fused, the flow of the heat medium stops, and the combustion of the furnace stops or the furnace closes. This phenomenon occurs when the furnace temperature setting or the furnace temperature itself exceeds the melting point of the object to be heated. Therefore, it is difficult to simultaneously melt the heated object composed of a wide variety of substances such as the scattering asbestos product in the internal combustion fluidized bed furnace. In addition, it is difficult to determine the optimum melting furnace temperature.

飛散性アスベスト製品には、セメントやロックウ−ルのようなアスベストよりも融点の低い物質が混合されて使用されている。アスベスト溶融温度に設定された炉内ではアスベストよりも先にセメントやロックウ−ル等が溶融し、流動化状態にある熱媒体に付着して炉の燃焼が止まり、炉が閉塞する。  A material having a melting point lower than that of asbestos, such as cement and rock wool, is used in the scattering asbestos product. In the furnace set at the asbestos melting temperature, cement, rock wall, etc. are melted before asbestos, adhere to the fluidized heat medium, stop the furnace combustion, and the furnace is closed.

内燃式熱媒体燃焼炉に飛散性アスベスト製品を投入するためには、飛散性アスベスト製品を、前処理として微粒に粉砕する必要がある。アスベストは硬度が高いので歯の着いたタイプの粉砕機では歯の磨耗が激しく、また吹き付けアスベストのような製品は綿状で流動性が悪いのでボ−ルミルでは粉砕が進まない。さらに装置外部への飛散の防止をするよう密閉性を保ちながら、炉の処理容量に適した被加熱体の投入量を制御する必要がある。  In order to introduce the scatterable asbestos product into the internal combustion heat medium combustion furnace, it is necessary to pulverize the scatterable asbestos product into fine particles as a pretreatment. Asbestos has high hardness, tooth wear is severe in a toothed type pulverizer, and products such as sprayed asbestos are cottony and have poor fluidity, so that pulverization does not proceed in a ball mill. Furthermore, it is necessary to control the input amount of the heated object suitable for the processing capacity of the furnace while maintaining hermeticity so as to prevent scattering outside the apparatus.

飛散性アスベスト製品に有機系の塗料や溶剤が混合されていた場合、それらが熱媒体で加熱され可燃性ガス化し、異常燃焼でフリ−ボ−ド内が異常高温になり炉が損傷する。  When organic paints and solvents are mixed in the flyable asbestos product, they are heated with a heat medium to become flammable gas, and abnormal combustion causes the inside of the free board to become abnormally hot and damages the furnace.

本発明は、この内燃式流動床炉の飛散性アスベスト処理に関する融着と云う本質的な問題点を解決する新規の内燃式熱媒体燃焼炉である。  The present invention is a novel internal combustion type heat medium combustion furnace that solves the essential problem of fusing asbestos treatment in the internal combustion fluidized bed furnace.

内燃式流動床炉は、熱媒体を流動させるために炉の下部から燃料ガスと空気と被加熱体を投入するが、本発明では熱媒体を流動させる必要がないので炉の如何なる方向からも燃料ガスと空気と被加熱体を投入できる。熱媒体を2枚の目皿で挟み固定し、空気圧縮装置と排ガスブロワ−との圧力差、即ち上部目皿の上下の差圧により被加熱体、溶融した被加熱体および再固化した被加熱体は輸送される。  In an internal combustion fluidized bed furnace, fuel gas, air, and an object to be heated are introduced from the bottom of the furnace in order to cause the heat medium to flow. However, in the present invention, it is not necessary to cause the heat medium to flow. Gas, air and heated object can be charged. The heating medium is sandwiched between two plates and fixed, and the heated object, the molten material to be heated, and the solidified heated object due to the pressure difference between the air compressor and the exhaust gas blower, that is, the pressure difference between the upper and lower plates. The body is transported.

飛散性アスベスト製品の主成分は、セラミック系であるのでセラミック系熱媒体に融着し易く炉が閉塞する。これを避ける為に、熱媒体にはセラミック系被加熱体と融着し難い、融点の高い金属系の熱媒体を使用する。融着しない被加熱体の場合はセラミック系熱媒体も使用できる。  Since the main component of the diffusible asbestos product is ceramic, it is easily fused to the ceramic heat medium and the furnace is closed. In order to avoid this, as the heat medium, a metal-based heat medium that has a high melting point and is difficult to be fused with the ceramic-based heated object is used. In the case of an object to be heated which is not fused, a ceramic heat medium can also be used.

被加熱体を内燃式熱媒体燃焼炉の目皿を通過させ、熱媒体より効率的に熱エネルギ−を被加熱体に与える為には飛散性アスベスト製品を出来るだけ細かく粉砕することが重要である。非常に微粒に飛散性アスベスト製品を粉砕するにはロッド式振動ミルを使用する。装置外部へのアスベストの漏れは危険であるので、ミルと燃焼炉は直結する。このロッド式振動ミルの出口には一時的に被加熱体を貯めるバッファ−タンクを結合する。  It is important to pulverize the asbestos product as finely as possible in order to pass the object to be heated through the eye plate of the internal combustion heat medium combustion furnace and to give the heat energy to the object to be heated more efficiently than the heat medium. . A rod-type vibration mill is used to pulverize asbestos products with very fine particles. Since the leakage of asbestos outside the equipment is dangerous, the mill and the combustion furnace are directly connected. A buffer tank for temporarily storing an object to be heated is coupled to the outlet of the rod type vibration mill.

粉砕された被加熱体の投入量を制御する為に、バッファ−タンクの出口には回転制御されるモ−タ−を持ったスクリュ−タイプフィ−ダ−を搭載する。バッファ−タンクにはレベルセンサ−を装着し、バッファ−タンクに溜まる粉砕された被加熱体が規定量を超えた場合には、センサ−から運転停止信号がミルに送られミルは自動的に運転を止める。  In order to control the input amount of the pulverized heated object, a screw type feeder having a motor whose rotation is controlled is mounted at the outlet of the buffer tank. When a level sensor is installed in the buffer tank and the pulverized heated object accumulated in the buffer tank exceeds the specified amount, an operation stop signal is sent from the sensor to the mill and the mill automatically operates. Stop.

有機混合物の可燃ガス化による異常燃焼は、熱媒体下部の温度やフリ−ボ−ド内の温度を検出し、燃料ガス量を制御することで、炉の安定した燃焼を行う。  Abnormal combustion due to combustible gasification of the organic mixture detects the temperature of the lower part of the heat medium and the temperature in the free board, and controls the amount of fuel gas to perform stable combustion of the furnace.

熱媒体を流動さぜずに目皿に挟み固定することで被加熱物を上からも投入でき、融点の低い飛散性アスベスト製品のアスベスト以外の混合物が、融点の高いアスベストの溶融の妨げにならない。即ち、この方式で融点の違う物質の同時溶融処理が可能になる。  By sandwiching and fixing the heat medium in the eye plate without flowing, the heated object can be put in from the top. Mixtures other than the asbestos of the low melting point asbestos product do not hinder the melting of the high melting point asbestos. . That is, this method enables simultaneous melting treatment of substances having different melting points.

金属熱媒体を用いることで、溶融したアスベストや溶融した飛散性アスベスト製品の他のセラミック系混合物の熱媒体への融着がし難くなり、炉が閉塞することなく長時間の運転転が可能になる。融点が高いの球形のセラミック系熱媒体は、金属系のものより融着という点からは劣るが、ある程度の使用は可能である。  By using a metal heating medium, it becomes difficult to fuse molten asbestos and other scattered ceramic mixture to the heating medium, enabling long-term operation without clogging the furnace. Become. A spherical ceramic heat medium having a high melting point is inferior to the metal one in terms of fusion, but can be used to some extent.

ロッド式振動ミルの使用により含有した硬いアスベストも極めて微粒に粉砕でき、また軽くて綿状な為に、通常のミル内では流動性せずに粉砕できなかった飛散性アスベスト製品も、ロッド式振動ミルのロッドが飛散性アスベスト製品を粉砕しながら出口に輸送させることが出来る。また過剰な被加熱体の投入を防ぎ適性量を投入することで安定した炉の燃焼状態を保つことができる。  Hard asbestos contained by using a rod type vibration mill can be pulverized into extremely fine particles, and because it is light and fluffy, scatterable asbestos products that could not be pulverized without fluidity in ordinary mills are also The mill rod can be transported to the outlet while pulverizing the asbestos product. Moreover, a stable furnace combustion state can be maintained by preventing an excessive amount of the object to be heated and introducing an appropriate amount.

有機混合物の可燃ガス化によって得られたガスは、熱媒体内でさらに燃料ガスとして再利用され、炉のエネルギ−効率を高める。  The gas obtained by combustible gasification of the organic mixture is further reused as fuel gas in the heat medium, increasing the energy efficiency of the furnace.

以下、本発明の実施の形態を図面に基づき詳細に説明する。  Hereinafter, embodiments of the present invention will be described in detail with reference to the drawings.

図1は、内燃式熱媒体加熱炉本体8の断面図とその周辺機器で構成され、飛散性アスベスト溶融装置全体を表しており、図2は、前処理装置として飛散性アスベスト製品の粉砕装置2の構成を表している。  FIG. 1 is composed of a cross-sectional view of an internal combustion type heating medium heating furnace body 8 and its peripheral devices, and represents the entire scattering asbestos melting apparatus, and FIG. 2 is a pulverizing apparatus 2 for a scattering asbestos product as a pretreatment apparatus. Represents the configuration.

空気圧縮装置1は、燃焼空気と燃料ガスタンク3からの燃料ガスと粉砕装置2で粉砕された被加熱体を燃焼炉8に輸送する。被加熱体投入口30から投入された被加熱体はロッド式振動ミル31で微粉砕されバッファ−タンク34に一旦集積される。バッファ−タンク34にはレベルセンサ−33が付帯されており、集積した粉砕被加熱体が予め設定した量を超えた場合、レベルセンサ−33からミル運転装置32へ運転停止の信号が送られロッド式振動ミルは運転を止める。逆にバッファ−タンク内の集積量が減った場合はレベルセンサ−からミル運転装置に運転開始の信号を送り、ミルは運転を開始する。  The air compressor 1 transports the combustion air, the fuel gas from the fuel gas tank 3, and the heated object pulverized by the pulverizer 2 to the combustion furnace 8. The heated object charged from the heated object charging port 30 is finely pulverized by the rod type vibration mill 31 and once accumulated in the buffer tank 34. A level sensor 33 is attached to the buffer tank 34. When the accumulated pulverized heated body exceeds a preset amount, a signal for stopping the operation is sent from the level sensor 33 to the mill operation device 32. The vibration mill stops operation. On the other hand, when the accumulation amount in the buffer tank decreases, an operation start signal is sent from the level sensor to the mill operation device, and the mill starts operation.

バッファ−タンク34からの粉砕被加熱体はスクリュ−フィ−ダ−36で燃焼炉8に送られる。スクリュ−フィ−ダ−36は回転数制御装置37で制御されたモ−タ−35で回転しており、燃焼炉8に適切な量の粉砕被加熱体を送る。粉砕被加熱体が装置外部へ漏れないように、このミル全体システム2は燃焼炉8にパイプで直結する。  The object to be crushed from the buffer tank 34 is sent to the combustion furnace 8 by a screw feeder 36. The screw feeder 36 is rotated by a motor 35 controlled by a rotation speed control device 37 and sends an appropriate amount of pulverized heated body to the combustion furnace 8. The entire mill system 2 is directly connected to the combustion furnace 8 with a pipe so that the pulverized heated body does not leak outside the apparatus.

粉砕被加熱体と空気と燃料ガスは、逆火防止の為に設置された防爆セラミック4と上部目皿5を通過して熱媒体6に供給される。炉内温度は被加熱体の溶融に最低限必要な温度に設定され、燃焼炉は制御装置13の働きで最適燃焼される。  The pulverized heated body, air, and fuel gas are supplied to the heat medium 6 through the explosion-proof ceramic 4 and the upper pan 5 installed for preventing backfire. The temperature in the furnace is set to a minimum necessary temperature for melting the heated object, and the combustion furnace is optimally burned by the action of the control device 13.

被加熱体に有機系の塗料や溶剤が混合されていた場合、これらは熱媒体により加熱され可燃性ガス化しフリ−ボ−ド内温度が異常高温になる場合がある。この場合、熱電対で異常な温度を検知し、燃料ガスを調整して炉内温度の異常を制御する。  When an organic paint or solvent is mixed with the object to be heated, these may be heated by a heat medium to become flammable gas and the freeboard temperature may become abnormally high. In this case, an abnormal temperature is detected by a thermocouple, and the fuel gas is adjusted to control the abnormal temperature in the furnace.

下部目皿7を通過した被加熱体は冷却装置9で冷却され回収箱10かバグフィルタ−11で回収される。排ガスブロワ−12は、上部目皿5から下流を負圧にし全体の被加熱体の輸送を空気圧縮装置1ともに行う。  The heated object that has passed through the lower pan 7 is cooled by the cooling device 9 and recovered by the recovery box 10 or the bag filter 11. The exhaust gas blower 12 makes the downstream of the upper pan 5 negative and transports the entire heated body together with the air compressor 1.

金属熱媒体の形状は球状とは限らず、多層構造の金属メッシュの集合体でも可能である。  The shape of the metal heat medium is not limited to a spherical shape, and may be an assembly of metal meshes having a multilayer structure.

本発明は飛散性アスベスト溶融処理の他に、粉砕シリカの球状化やシラノ−ル基の除去に利用できる。  The present invention can be used for spheroidizing silica and removing silanol groups in addition to the fusible asbestos melting treatment.

ゴミ焼却炉や火葬場の焼却装置より排出されるダイオキシンの無害化に利用できる。  It can be used to detoxify dioxins emitted from garbage incinerators and cremation incinerators.

火葬場の焼却装置や畜産廃棄物や食品関連設備から排出される悪臭の無臭化を図れる。  Odorless odors emitted from incinerators, livestock wastes, and food-related equipment at cremation centers can be eliminated.

本発明は、その装置規模に制限されないので、市町村や中小企業でも利用され易い。  Since the present invention is not limited to the scale of the apparatus, it can be easily used by municipalities and small and medium enterprises.

内燃式熱媒体燃焼炉本体とその周辺設備で構成された、飛散性アスベスト溶融処理装置を表している。炉本体は断面図である。  The scattering asbestos melting processing apparatus comprised with the internal combustion type heat-medium combustion furnace main body and its peripheral equipment is represented. The furnace body is a cross-sectional view. 図1内で示される粉砕装置2の構成を表している。  The structure of the grinding | pulverization apparatus 2 shown in FIG. 1 is represented.

符号の説明Explanation of symbols

1 空気圧縮装置
2 投入量制御装置を付帯したロッド式振動ミル詳細図面2
3 燃料ガスタンク
4 防爆セラミックボ−ル
5 上部目皿
6 金属熱媒体
7 下部目皿
8 内燃式熱媒体燃焼炉
9 冷却装置
10 回収箱
11 バグフィルタ−
12 排気ブロワ−
13 炉内温度制御装置
14 空気流量検出器
15 空気流量自動調節弁
16 燃料流量自動調節弁
17 燃料流量検出器
18 熱電対
19 熱電対
20 着火バ−ナ−
30 被加熱体投入口
31 ロッド式振動ミル
32 ミル運転装置
33 レベルセンサ−
34 粉砕被加熱体バッファ−タンク
35 モ−タ−
36 スクリュ−フィ−ダ−
37 モ−タ−回転数制御装置
1 Air compressor 2 Rod type vibration mill with attached amount control device Detailed drawing 2
3 Fuel Gas Tank 4 Explosion Proof Ceramic Ball 5 Upper Pan 6 Metal Heating Medium 7 Lower Pan 8 Internal Combustion Heat Medium Combustion Furnace 9 Cooling Device 10 Collection Box 11 Bag Filter
12 Exhaust blower
13 In-furnace temperature controller 14 Air flow detector 15 Air flow automatic adjustment valve 16 Fuel flow automatic adjustment valve 17 Fuel flow detector 18 Thermocouple 19 Thermocouple 20 Ignition burner
30 Heater input port 31 Rod-type vibration mill 32 Mill operation device 33 Level sensor
34 Crushing heated object buffer tank 35 Motor
36 Screw feeder
37 Motor speed control device

Claims (4)

燃料ガスと空気の混合ガスを炉内で燃焼させ、燃焼雰囲気の中に流動しない熱媒体を置き高温加熱させ、その熱媒体で粉体を加熱したり溶融させたり、また気体を加熱する内燃式熱媒体燃焼炉。  An internal combustion type that burns a mixed gas of fuel gas and air in a furnace, places a heat medium that does not flow in the combustion atmosphere, heats it at a high temperature, heats and melts the powder with that heat medium, and heats the gas Heat medium combustion furnace. 前記内燃式熱媒体燃焼炉の熱媒体は、金属系やセラミック系の素材で構成される。The heat medium of the internal combustion heat medium combustion furnace is made of a metal or ceramic material. 前記内燃式熱媒体燃焼炉は、ロッド式振動ミルと連結され、ロッド式振動ミルはレベルセンサ−を搭載したバッファ−タンクと連結され、さらに可変回転数制御できるモ−タ−で回転するスクリュ−フィ−ダ−で連結されている。  The internal combustion heat medium combustion furnace is connected to a rod-type vibration mill, which is connected to a buffer tank equipped with a level sensor, and is further rotated by a motor capable of controlling the variable rotational speed. They are connected by a feeder. 前記内燃式熱媒体燃焼炉は、被加熱体から発生する可燃性ガスによる異常燃焼を検知し燃焼制御により安定した燃焼を行う。  The internal combustion heat medium combustion furnace detects abnormal combustion caused by a combustible gas generated from an object to be heated and performs stable combustion by combustion control.
JP2006031626A 2006-01-13 2006-01-13 Scattering asbestos melting treatment device Pending JP2007225125A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP2006031626A JP2007225125A (en) 2006-01-13 2006-01-13 Scattering asbestos melting treatment device

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP2006031626A JP2007225125A (en) 2006-01-13 2006-01-13 Scattering asbestos melting treatment device

Publications (1)

Publication Number Publication Date
JP2007225125A true JP2007225125A (en) 2007-09-06

Family

ID=38547105

Family Applications (1)

Application Number Title Priority Date Filing Date
JP2006031626A Pending JP2007225125A (en) 2006-01-13 2006-01-13 Scattering asbestos melting treatment device

Country Status (1)

Country Link
JP (1) JP2007225125A (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2012096155A (en) * 2010-11-01 2012-05-24 Chutoku Kenki Kk Asbestos-containing suspended matter burning/melting treatment device and method of burning/melting treatment for asbestos-containing suspended matter
CN105299663A (en) * 2015-12-04 2016-02-03 深圳智慧能源技术有限公司 Pressure control fixed value adjusting system based on torch running working condition
WO2017092028A1 (en) * 2015-12-04 2017-06-08 深圳智慧能源技术有限公司 Pressure control fixed value adjusting system based on torch operating condition

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2012096155A (en) * 2010-11-01 2012-05-24 Chutoku Kenki Kk Asbestos-containing suspended matter burning/melting treatment device and method of burning/melting treatment for asbestos-containing suspended matter
CN105299663A (en) * 2015-12-04 2016-02-03 深圳智慧能源技术有限公司 Pressure control fixed value adjusting system based on torch running working condition
WO2017092028A1 (en) * 2015-12-04 2017-06-08 深圳智慧能源技术有限公司 Pressure control fixed value adjusting system based on torch operating condition

Similar Documents

Publication Publication Date Title
JPH01270990A (en) Continuous fluocculationof heavy metal contained in ash of incinerator
CN111112299B (en) Melting furnace for melting garbage fly ash
JP2007301425A (en) Apparatus for melting asbestos-containing waste
JP2007225125A (en) Scattering asbestos melting treatment device
WO2002014743A1 (en) Method for incineration disposal of waste
JP2001227714A (en) Method for incinerating disposal of waste
RU2258179C2 (en) Method of action onto properties of residues of incineration from incinerator plant
JP2007064498A (en) Combustion melting furnace
JPH1177017A (en) Prevention of moisture absorption of fused or burnt fly ash
JPH1073233A (en) Molten slug water-cooling device for combustion melting furnace
JP4157187B2 (en) Method for preventing moisture absorption from molten or burned fly ash
WO2001083126A1 (en) Fly ash treating method and device
JP2006297331A (en) Production method and apparatus of granulation particle
KR20050083488A (en) Brown gas ash melting furnace
JP2799550B2 (en) Melting furnace
JP2680714B2 (en) Ash treatment method for coal-fired boiler
JP3927917B2 (en) Waste treatment system
KR200351156Y1 (en) Brown gas ash melting furnace
JP3869043B2 (en) Exhaust gas treatment equipment in waste treatment equipment
JP2566260B2 (en) Sludge melting incinerator
JP2001304524A (en) Waste heat recovery apparatus in melting furnace
JP2007307548A (en) Method and equipment for melting asbestos waste
JP2002228124A (en) Melting furnace
JPH09250727A (en) Waste disposing device
WO2002103240A1 (en) Melting device and waste treatment system