JPH09273736A - Surface melting furnace - Google Patents
Surface melting furnaceInfo
- Publication number
- JPH09273736A JPH09273736A JP8495896A JP8495896A JPH09273736A JP H09273736 A JPH09273736 A JP H09273736A JP 8495896 A JP8495896 A JP 8495896A JP 8495896 A JP8495896 A JP 8495896A JP H09273736 A JPH09273736 A JP H09273736A
- Authority
- JP
- Japan
- Prior art keywords
- furnace
- melted
- melted material
- melting
- gate
- 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
Links
- 238000002844 melting Methods 0.000 title claims abstract description 71
- 230000008018 melting Effects 0.000 title claims abstract description 71
- 239000002893 slag Substances 0.000 claims abstract description 36
- 239000000463 material Substances 0.000 claims description 98
- 239000000155 melt Substances 0.000 claims description 3
- 239000000126 substance Substances 0.000 claims description 2
- 230000003028 elevating effect Effects 0.000 abstract 1
- 238000000034 method Methods 0.000 description 12
- 238000002485 combustion reaction Methods 0.000 description 8
- 238000002156 mixing Methods 0.000 description 8
- 239000000446 fuel Substances 0.000 description 7
- 238000010128 melt processing Methods 0.000 description 5
- 238000004056 waste incineration Methods 0.000 description 5
- 239000000428 dust Substances 0.000 description 4
- 239000007788 liquid Substances 0.000 description 4
- 238000010586 diagram Methods 0.000 description 3
- 238000007599 discharging Methods 0.000 description 3
- 239000010881 fly ash Substances 0.000 description 3
- 239000002828 fuel tank Substances 0.000 description 3
- 239000003350 kerosene Substances 0.000 description 3
- 238000010309 melting process Methods 0.000 description 3
- 239000010813 municipal solid waste Substances 0.000 description 3
- 239000003921 oil Substances 0.000 description 3
- 239000004576 sand Substances 0.000 description 3
- 238000001816 cooling Methods 0.000 description 2
- 239000000295 fuel oil Substances 0.000 description 2
- 239000012768 molten material Substances 0.000 description 2
- 230000000704 physical effect Effects 0.000 description 2
- 238000010248 power generation Methods 0.000 description 2
- 238000007789 sealing Methods 0.000 description 2
- 239000010802 sludge Substances 0.000 description 2
- 230000008023 solidification Effects 0.000 description 2
- 238000007711 solidification Methods 0.000 description 2
- 239000004071 soot Substances 0.000 description 2
- 239000002956 ash Substances 0.000 description 1
- 239000000919 ceramic Substances 0.000 description 1
- 239000000571 coke Substances 0.000 description 1
- 239000000567 combustion gas Substances 0.000 description 1
- 238000010828 elution Methods 0.000 description 1
- 238000001125 extrusion Methods 0.000 description 1
- 239000007789 gas Substances 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- 239000010763 heavy fuel oil Substances 0.000 description 1
- 229910001385 heavy metal Inorganic materials 0.000 description 1
- 239000002440 industrial waste Substances 0.000 description 1
- 229910052751 metal Inorganic materials 0.000 description 1
- 239000002184 metal Substances 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 230000002093 peripheral effect Effects 0.000 description 1
- 230000002265 prevention Effects 0.000 description 1
- 239000000779 smoke Substances 0.000 description 1
- 239000002918 waste heat Substances 0.000 description 1
- 239000002699 waste material Substances 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 1
Classifications
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
- Y02W30/00—Technologies for solid waste management
- Y02W30/50—Reuse, recycling or recovery technologies
- Y02W30/62—Plastics recycling; Rubber recycling
Landscapes
- Gasification And Melting Of Waste (AREA)
- Processing Of Solid Wastes (AREA)
- Processing And Handling Of Plastics And Other Materials For Molding In General (AREA)
- Vertical, Hearth, Or Arc Furnaces (AREA)
- Furnace Charging Or Discharging (AREA)
Abstract
Description
【0001】[0001]
【発明の属する技術分野】本発明は、都市ごみや産業廃
棄物の焼却により生成する燃焼残渣や飛灰、不燃性破砕
廃棄物等を溶融処理する溶融炉に関するものであり、被
溶融物の種類が変っても常に高能率で安定した溶融処理
を行なえるようにした表面溶融炉に関するものである。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a melting furnace for melting and processing combustion residues, fly ash, non-combustible crushed waste, etc. generated by incineration of municipal solid waste and industrial waste. The present invention relates to a surface melting furnace capable of performing stable melting processing with high efficiency even if the temperature changes.
【0002】[0002]
【従来の技術】近年、都市ごみ等の焼却炉から排出され
る焼却残渣や飛灰の減容化及び無害化を図るため、焼却
残渣等の溶融固化処理法が注目され、現実に実用に供さ
れている。焼却残渣等は溶融固化することにより、その
容積を1/2〜1/3に減らすことができると共に、重
金属等の有害物質の溶出防止や溶融スラグの再利用、最
終埋立処分場の延命等が可能になるからである。2. Description of the Related Art In recent years, in order to reduce the volume and harmlessness of incineration residues and fly ash discharged from incinerators such as municipal solid waste, attention has been paid to a method of melting and solidifying incineration residues and the like, which are actually put to practical use. Has been done. By melting and solidifying incineration residues, etc., the volume can be reduced to 1/2 to 1/3. At the same time, prevention of elution of harmful substances such as heavy metals, reuse of molten slag, and extension of the life of the final landfill disposal site, etc. Because it becomes possible.
【0003】而して、前記焼却残渣等の溶融固化処理方
法には、アーク溶融炉やプラズマアーク炉、電気抵抗炉
等を使用し、電気エネルギーによって被溶融物を溶融固
化する方法と、表面溶融炉や旋回溶融炉、コークスベッ
ド炉等を使用し、燃料の燃焼エネルギーによって被溶融
物を溶融固化する方法とが多く利用されており、都市ご
み焼却設備に発電設備が併置されている場合には、前者
の電気エネルギーを用いる方法が、また発電設備が併置
されていない場合には、後者の燃焼エネルギーを用いる
方法が夫々多く採用されている。尚、後者の燃焼エネル
ギーを用いる溶融固化処理方法にあっては、従来から灯
油や重油等の液体燃料をエネルギー源とする溶融固化処
理設備が多く利用されている。As a method for melting and solidifying the incineration residue and the like, an arc melting furnace, a plasma arc furnace, an electric resistance furnace, etc. are used to melt and solidify a material to be melted by electric energy, and surface melting. A method of using a furnace, a swirling melting furnace, a coke bed furnace, etc. to melt and solidify the material to be melted by the combustion energy of the fuel is often used, and when the power generation equipment is installed in parallel with the municipal waste incineration equipment, The former method of using electric energy and the latter method of using combustion energy are often used when the power generation equipment is not collocated. Incidentally, in the latter method of melting and solidifying using combustion energy, a melting and solidifying processing facility using a liquid fuel such as kerosene or heavy oil as an energy source has been widely used.
【0004】図6及び図7は、従前のごみ焼却処理設備
に併置した液体燃料を用いる燃焼残渣等の溶融固化処理
設備の一例を示す説明図であり、図6及び図7に於い
て、1は炉本体、2は炉底、3は炉側壁、4は炉天井
壁、5はスラグタップ、6は被溶融物供給路、6aはホ
ッパ、7はプッシャ、8は灯油バーナ、9は高温煙道、
10は水封式スラグ排出用コンベア、11は空気予熱
器、12は燃料タンク、13は送油ポンプ、14は燃料
制御装置、15は空気圧縮機、16はエアータンク、1
7は押込送風機、18は空気供給ダクト、19は空気量
調整ダンパである(特開平5−104074等)。FIG. 6 and FIG. 7 are explanatory views showing an example of a melting and solidifying treatment equipment for a combustion residue etc. using a liquid fuel arranged in parallel with the conventional refuse incineration treatment equipment. In FIG. 6 and FIG. Is a furnace body, 2 is a furnace bottom, 3 is a furnace side wall, 4 is a furnace ceiling wall, 5 is a slag tap, 6 is a molten material supply path, 6a is a hopper, 7 is a pusher, 8 is kerosene burner, and 9 is high-temperature smoke. road,
10 is a water-sealed slag discharging conveyor, 11 is an air preheater, 12 is a fuel tank, 13 is an oil feed pump, 14 is a fuel control device, 15 is an air compressor, 16 is an air tank, 1
Reference numeral 7 is a forced air blower, 18 is an air supply duct, and 19 is an air amount adjusting damper (JP-A-5-104074, etc.).
【0005】前記表面溶融炉の要部である炉本体1は、
内方へ向って傾斜する炉底2と炉側壁3と炉天井壁4と
から構成されており、前記炉底2の中央にはスラグタッ
プ5が穿設されている。また、前記炉底2の側端部上方
には被溶融物供給路6が設けられており、該供給路6の
上方部がホッパ6aとなっている。更に、前記炉側壁3
には複数基のプッシャ7が、また炉天井壁4にはバーナ
8が夫々設けられている。The furnace body 1, which is the main part of the surface melting furnace, is
It is composed of a furnace bottom 2 which inclines inward, a furnace side wall 3 and a furnace ceiling wall 4, and a slag tap 5 is bored in the center of the furnace bottom 2. Further, a melted material supply passage 6 is provided above the side end portion of the furnace bottom 2, and an upper portion of the supply passage 6 serves as a hopper 6a. Further, the furnace side wall 3
A plurality of pushers 7 are provided in the furnace, and a burner 8 is provided in the furnace ceiling wall 4.
【0006】A重油や灯油等の液体燃料はローリー車等
で溶融固化処理設備まで搬入され、燃料タンク12に一
担貯留される。また、ごみ焼却残渣や飛灰は、ごみ焼却
設備からコンベアー(図示省略)等により溶融固化処理
設備へ搬入され、表面溶融炉Aのホッパ6a内へ貯留さ
れたあと、複数のプッシャ7により溶融炉本体1内へ順
次供給され、スラグタップ5を中心にして炉底2上に擂
鉢状の外表面を有する層状に積層されて行く。前記送油
ポンプ13により圧送された液体燃料は、空気圧縮機1
5からの高圧空気若しくはごみ焼却炉の廃熱ボイラから
の蒸気(図示省略)によって溶融バーナ8のノズル内で
微粒化され、溶融炉本体1内の被溶融物Bへ向けて噴射
される。そして、これに空気供給ダクト18を通して高
温の燃焼用空気が供給されることにより、前記微粒化さ
れた燃料油が燃焼される。尚、溶融バーナ8の作動等
は、全て燃焼制御装置14によってコントロールされて
いる。また、前記溶融バーナ8からの燃焼火炎によって
加熱溶融されたスラグは、スラグタップ5を通して水封
式のスラグ排出用コンベア10上へ排出され、冷却固化
されたあと外部へ排出されて行く。更に、溶融炉本体1
内の燃焼ガスは空気予熱器11で冷却されたあと、ガス
冷却設備(図示省略)を通して大気中へ排出されて行
く。Liquid fuel such as heavy fuel oil A or kerosene is carried to a melting and solidification treatment facility by a lorry vehicle or the like, and stored in a fuel tank 12 as a whole. Further, the refuse incineration residue and fly ash are carried into the melting and solidification treatment facility from the refuse incineration facility by a conveyor (not shown), etc., and are stored in the hopper 6a of the surface melting furnace A, and then the melting furnaces are pushed by the plurality of pushers 7. The slag taps 5 are centered on the slag tap 5 and are stacked on the furnace bottom 2 in layers having a mortar-shaped outer surface. The liquid fuel pumped by the oil pump 13 is used as the air compressor 1
High-pressure air from 5 or steam (not shown) from the waste heat boiler of the refuse incinerator is atomized in the nozzle of the melting burner 8 and injected toward the melted material B in the melting furnace body 1. Then, high-temperature combustion air is supplied to this through the air supply duct 18, whereby the atomized fuel oil is burned. The operation of the melting burner 8 and the like are all controlled by the combustion control device 14. The slag that is heated and melted by the combustion flame from the melting burner 8 is discharged through the slag tap 5 onto the water-sealing type slag discharging conveyor 10, cooled and solidified, and then discharged to the outside. Further, the melting furnace body 1
The combustion gas inside is cooled by the air preheater 11 and then discharged into the atmosphere through a gas cooling facility (not shown).
【0007】ところで、図6の如き従前の表面溶融炉に
於いては、溶融処理すべき特定の被溶融物Bの性状や処
理量に応じて炉底2と炉天井壁4の位置及び寸法関係を
決定すると云う方法で、炉本体1の設計が行なわれてい
る。即ち、図7に示す如く、処理対象である特定の被溶
融物Bが有する個有の安息角Cに合わせて、被溶融物B
の供給部の切り出し高さ寸法H1 や溶融バーナ8と被溶
融物の外表面B1 との間の高さ寸法H2 を決定し、これ
等両寸法H1 、H2を基にして、当該被溶融物Bの溶融
に最適な炉の形態や炉底2上に積層された被溶融物Bの
積層形態を選定するようにしている。By the way, in the conventional surface melting furnace as shown in FIG. 6, the position and the dimensional relationship between the furnace bottom 2 and the furnace ceiling wall 4 depend on the properties and the amount of the specific material B to be melted. The furnace main body 1 is designed by a method of determining. That is, as shown in FIG. 7, the melted material B is matched with the unique angle of repose C of the specific melted material B to be processed.
The cut-out height dimension H 1 of the supply part and the height dimension H 2 between the melting burner 8 and the outer surface B 1 of the material to be melted are determined, and based on these dimensions H 1 and H 2 , The optimum form of the furnace for melting the melted material B and the stacked form of the melted material B stacked on the furnace bottom 2 are selected.
【0008】換言すれば、従前のこの種表面溶融炉は、
何れも特定の被溶融物Bを最適条件下で溶融処理すると
云うことを第1目標として設計されており、その結果、
被溶融物Bの性状や物性がほぼ一定の場合には、極めて
高能率で安定した溶融処理を行なうことが可能となる。In other words, the conventional surface melting furnace of this kind is
All of them are designed with the first goal of performing a melting process on a specific material B to be melted under optimum conditions, and as a result,
When the properties and physical properties of the material to be melted B are substantially constant, it is possible to perform a stable melting process with extremely high efficiency.
【0009】ところが、実稼動の表面溶融炉に於いて
は、一般に異なる種類の被溶融物Bを受け入れ、これ等
を溶融処理しなければならない場合が通常であり、特定
種類の被溶融物Bのみを受け入れするような設備は殆ん
ど稀である。より具体的には、実稼動の表面溶融炉で
は、通常被溶融物Bとして都市ごみ焼却灰やばいじん、
破砕不燃物、汚泥等が搬入されて来る。そして、搬入さ
れた各種の被溶融物Bは、都市ごみ焼却残渣のみを単
独で溶融処理する方法、都市ごみ焼却残渣とばいじん
とを混合溶融処理する方法(例えば混合率70:3
0)、都市ごみ焼却残渣とばいじんと破砕不燃物とを
混合溶融処理する方法(例えば混合率50:30:2
0)、汚泥のみを単独で溶融処理する方法、多数の
各種被溶融物を混合溶融処理する方法、等の何れかを適
宜に組み合せることにより、順次溶融処理されて行く。However, in a practical surface melting furnace, it is usually the case that different types of melted materials B must be received and melted, and only specific types of melted materials B are to be processed. The equipment that accepts is almost rare. More specifically, in an actual surface melting furnace, the municipal solid waste incineration ash or dust, etc.
Crushed incombustibles, sludge, etc. are brought in. Then, for each of the various melted objects B that have been carried in, a method of melting only the municipal waste incineration residue alone, or a method of mixing and melting the municipal waste incineration residue and soot and dust (for example, a mixing ratio of 70: 3)
0), a method of mixing and melting municipal waste incineration residues, soot and dust, and crushed incombustibles (for example, mixing ratio 50: 30: 2)
0), a method in which only sludge alone is melt-processed, a method in which a large number of various objects to be melted are mixed and melt-processed, and the like are appropriately combined for successive melt-processing.
【0010】しかし、各種の異なる被溶融物Bを溶融処
理する場合には、各被溶融物Bの安息角C1 が夫々異な
るため(例えば、ばいじんの安息角C1 =15〜20
°、ごみ焼却残渣の安息角C1 =30〜50°、破砕不
燃物の安息角C1 =30〜60°)、夫々の被溶融物B
を単独で溶融処理する場合であっても、或いは混合して
溶融処理(混合率に応じて平均安息角C1 が変化する)
する場合であっても、被溶融物Bの現実の安息角C1 が
炉本体1の設計に採用した最適安息角Cから大きく外れ
ることになり、その結果、高能率で安定した溶融処理の
達成が難くなる。However, when various kinds of different melted materials B are melt-processed, the angle of repose C 1 of each melted material B is different (for example, the angle of repose C 1 of dust is 15 to 20).
Angle of repose of refuse incineration residue C 1 = 30 to 50 °, angle of repose of crushed incombustible material C 1 = 30 to 60 °), and respective melted materials B
Melt processing alone or by mixing and melting (average angle of repose C 1 changes depending on the mixing ratio)
Even if it does, the actual angle of repose C 1 of the melted material B deviates largely from the optimum angle of repose C used in the design of the furnace body 1, and as a result, a stable melting process with high efficiency is achieved. Becomes difficult.
【0011】また、仮りに搬入されてくる被溶融物Bが
同じごみ焼却炉からの焼却残渣であったとしても、被焼
却物であるごみの品質が変ることによって焼却残渣(被
溶融物B)の性状や物性も大きく変化する。そのため、
上述の場合と同様に、被溶融物Bの安息角C1 そのもの
が変ることになり、同じごみ焼却炉から排出されてきた
被溶融物Bであってもこれを常に最適条件下で溶融処理
することができなくなる。Even if the material B to be melted is an incineration residue from the same refuse incinerator, the incineration residue (material to be melted B) may change due to the quality change of the refuse to be incinerated. The properties and physical properties of will also change significantly. for that reason,
As in the case described above, the angle of repose C 1 of the melted material B itself changes, and even the melted material B discharged from the same refuse incinerator is always melted under optimum conditions. Can't do it.
【0012】具体的には、例えば、特定の被溶融物Bの
安息角(30°)を設計安息角Cとして設計した表面溶
融炉に於いて、安息角C1 が設計安息角C=30°よ
り小さな被溶融物Bを溶融処理する場合には、溶融が進
行して炉底の先端部よりスラグが流出し出すのに伴なっ
て、プッシャ7を作動せしめて被溶融物Bを炉本体1内
へ供給すると、供給された被溶融物Bの勢いで炉底2上
の被溶融物Bが下方へ向ってなだれ現象を起し、これに
よって未溶融の被溶融物Bが溶融した被溶融物と一緒に
スラダタップ5内へ流出すると云う事象が多発する。ま
た逆に、前記設計安息角C=30°よりも大きな安息
角C1 の被溶融物Bを溶融処理する場合には、溶融が進
行して炉底先端部よりスラグが流出し出すのに伴なっ
て、プッシャ7を作動せしめても、被溶融物Bの先端部
が必要な距離だけ前方へ移動せず、その結果溶融した被
溶融物Bが円滑にスラグタップ5内へ落ち込まないと云
う事象が発生し、被溶融物Bの処理量の低下を招くこと
になる。Specifically, for example, in a surface melting furnace in which the angle of repose (30 °) of a specific material B to be melted is designed as the angle of repose C, the angle of repose C 1 is the designed angle of repose C = 30 °. When the smaller melted material B is subjected to the melting treatment, the pusher 7 is operated to move the melted material B to the furnace body 1 as the melting progresses and the slag flows out from the tip of the furnace bottom. When it is supplied to the inside, the melted material B on the furnace bottom 2 causes an avalanche phenomenon by the momentum of the supplied melted material B, whereby the unmelted melted material B is melted The phenomenon that it flows out into the slada tap 5 occurs frequently with. On the contrary, when the melted material B having the angle of repose C 1 larger than the designed angle of repose C = 30 ° is melted, the melting progresses and the slag flows out from the tip of the furnace bottom. Then, even if the pusher 7 is operated, the tip of the melted material B does not move forward by a required distance, and as a result, the melted melted material B does not smoothly fall into the slag tap 5. Occurs, resulting in a decrease in the throughput of the melted material B.
【0013】[0013]
【発明が解決しようとする課題】本発明は従前のこの種
表面溶融炉に於ける上述の如き問題、即ち、溶融処理す
べき被溶融物Bの種類が変ってその安息角C1 が変化す
ると、被溶融物Bを最適条件下で溶融処理することがで
きずに、溶融スラグの品質が変化したり、或いは溶融処
理能力が低下する等の問題を解決せんとするものであ
り、一基の表面溶融処理炉でもって安息角C1 の異なる
多種類の被溶融物Bを常に高能率で安定して溶融処理で
きるようにした表面溶融炉を提供するものである。SUMMARY OF THE INVENTION The present invention has the above-mentioned problem in the conventional surface melting furnace of this kind, that is, when the type of the material B to be melted is changed and the repose angle C 1 thereof is changed. The problem is that the melted material B cannot be melt-processed under the optimum conditions and the quality of the molten slag is changed or the melt-processing capacity is reduced. It is intended to provide a surface melting furnace capable of constantly and stably melting various kinds of melted objects B having different angles of repose C 1 with a surface melting treatment furnace with high efficiency.
【0014】[0014]
【課題を解決するための手段】本件請求項1に記載の発
明は、内方へ向って傾斜した炉底2の中央部にスラグタ
ップ5を、また炉底2の外端部上方に被溶融物供給路6
を夫々具備すると共に、前記スラグタップ5を中心にし
て炉底2上に、被溶融物Bを擂鉢状の外表面を有する層
状に積層せしめる炉本体1と、前記炉本体1の側壁3に
設けられ、被溶融物供給路6から搬入された被溶融物B
を炉本体1内へ供給するプッシャ7と、炉本体1の天井
壁4に設けられ、前記積層せしめた被溶融物の表面B1
を加熱溶融するバーナ8と、炉本体1内へ被溶融物Bを
供給する供給部の近傍に上・下方向へ昇降自在に配設さ
れ、炉底2上へ供給した被溶融物Bの積層形態を変える
ゲート20とを備えたことを発明の基本構成とするもの
である。According to the invention described in claim 1, the slag tap 5 is provided at the center of the furnace bottom 2 which is inclined inward, and the slag tap 5 is melted above the outer end of the furnace bottom 2. Material supply path 6
And a furnace main body 1 for stacking the material B to be melted in a layer having a mortar-shaped outer surface on the furnace bottom 2 around the slag tap 5 and a side wall 3 of the furnace main body 1. To be melted B, which has been transported from the melted material supply path 6
And a pusher 7 for supplying the inside of the furnace main body 1 to the ceiling wall 4 of the furnace main body 1, and the surface B 1 of the stacked objects to be melted.
The burner 8 that heats and melts the melted material B and the supply unit that supplies the melted material B into the furnace body 1 are arranged so as to be movable up and down, and the melted material B that is supplied onto the furnace bottom 2 is stacked. The provision of the gate 20 for changing the form is the basic configuration of the invention.
【0015】また、本件請求項2に記載の発明は、傾斜
炉底2の一端にスラグタップ5を、また炉底2の他端上
方に被溶融物供給路6を夫々具備すると共に、前記炉底
2上に被溶融物Bを傾斜状の外表面を有する層状に積層
せしめる炉本体1と、前記炉本体1の側壁3に設けら
れ、被溶融物供給路6から搬入された被溶融物Bを炉本
体1内へ供給するプッシャ7と、炉本体1の天井壁4に
設けられ、前記積層せしめた被溶融物の表面B1 を加熱
溶融するバーナ8と、炉本体1内へ被溶融物Bを供給す
る供給部の近傍に上・下方向へ昇降自在に配設され、炉
底2上へ供給した被溶融物Bの積層形態を変えるゲート
20とを備えたことを発明の基本構成とするものであ
る。The invention according to claim 2 further comprises a slag tap 5 at one end of the inclined furnace bottom 2 and a melted material supply passage 6 above the other end of the furnace bottom 2, and the furnace A furnace body 1 for stacking the melted material B on the bottom 2 in a layer having an inclined outer surface, and a melted material B which is provided on the side wall 3 of the furnace body 1 and is carried in from a melted material supply path 6 And a burner 8 provided on the ceiling wall 4 of the furnace body 1 for heating and melting the surface B 1 of the stacked objects to be melted, and a material to be melted into the furnace body 1. A basic configuration of the invention is provided with a gate 20 which is arranged in the vicinity of a supply unit for supplying B so as to be able to move up and down, and which changes the stacking form of the melted material B supplied onto the furnace bottom 2. To do.
【0016】[0016]
【発明の実施の態様】以下、図面に基づいて本発明の実
施の態様を説明する。図1は本発明に係る表面溶融炉の
要部を示す縦断面図であり、図2はゲート20の配設状
態を示す斜面図である。尚、図1及び図2に於いて、前
記図6及び図7と同一の部位・部材には、これと同じ参
照番号を使用するものとする。図1及び図2に於いて、
2は炉底、3は炉側壁、4は炉天井壁、5はスラグタッ
プ、6は被溶融物供給路、7はプッシャ、8はバーナ、
20はゲート、21はゲート昇降装置、22はサンドシ
ールである。BEST MODE FOR CARRYING OUT THE INVENTION Embodiments of the present invention will be described below with reference to the drawings. FIG. 1 is a vertical cross-sectional view showing a main part of a surface melting furnace according to the present invention, and FIG. 2 is a perspective view showing a disposition state of a gate 20. 1 and 2, the same parts and members as those in FIGS. 6 and 7 are designated by the same reference numerals. In FIGS. 1 and 2,
2 is a furnace bottom, 3 is a furnace side wall, 4 is a furnace ceiling wall, 5 is a slag tap, 6 is a molten material supply path, 7 is a pusher, 8 is a burner,
20 is a gate, 21 is a gate lifting device, and 22 is a sand seal.
【0017】前記ゲート20は、図1に示す如く、ホッ
パ6a内の被溶融物Bが被溶融物供給路6を通して炉本
体1内へ入り、炉底2上へその安息角C1 を以ってなだ
れ込む供給部の上方に上・下方向へ昇降自在に設けられ
ており、油圧シリンダ等の昇降装置21により遠隔自動
制御装置(図示省略)からの制御信号により昇降駆動さ
れる構成となっている。In the gate 20, as shown in FIG. 1, the material B to be melted in the hopper 6a enters the furnace main body 1 through the material supply path 6 to be melted, and has a repose angle C 1 on the furnace bottom 2. It is provided so as to be able to ascend / descend in the upward / downward direction above the supply section that is being drooled, and is configured to be lifted / lowered by a lifting / lowering device 21 such as a hydraulic cylinder according to a control signal from a remote automatic control device (not shown). .
【0018】具体的には、前記ゲート20は図2に示す
如く、炉天井壁4を挿通せしめて被溶融物供給路6の外
壁面に沿って垂直に昇降自在に配設されている。また、
ゲート20は、これを最低部まで下降せしめた場合には
炉本体1内からの輻射熱を受けて高温となるため、水
(又は空気)による強制冷却構造となっている。尚、本
実施態様では、ゲート20を水冷(又は空冷)方式のゲ
ートとしているが、耐熱セラミック製のゲート20とし
てもよいことは勿論である。更に、本実施態様では、ゲ
ート20のスライド部分の気密性をサンドシールにより
確保する構成としているが、その他のシール構造を用い
てもよいことは勿論である。More specifically, as shown in FIG. 2, the gate 20 is vertically movable along the outer wall surface of the melted material supply path 6 with the furnace ceiling wall 4 inserted therethrough. Also,
The gate 20 has a forced cooling structure with water (or air) because when it is lowered to the lowest part, it becomes high temperature by receiving radiant heat from the inside of the furnace body 1. In this embodiment, the gate 20 is a water-cooled (or air-cooled) gate, but it goes without saying that the gate 20 may be a heat-resistant ceramic gate 20. Furthermore, in this embodiment, the airtightness of the sliding portion of the gate 20 is ensured by the sand seal, but it goes without saying that other sealing structures may be used.
【0019】次に、本発明の作動について説明する。先
ず、被溶融物Bの安息角C1 が炉本体1の設計安息角C
にほぼ近い場合には、図3に示す如くゲート20は最上
方位置まで引き上げられる。また、逆に、被溶融物Bの
安息角C1 が炉本体1の設計安息角Cよりも大幅に小さ
い場合には、図4に示す如く、ゲート20は最下方位置
まで下降される。更に、被溶融物Bの安息角C1 が炉本
体1の設計安息角Cよりも若干小さい場合には、図5に
示す如くゲート20の下降量は適宜に調整され、炉底上
に積層せしめた被溶融物Bの先端がほぼ炉底2の先端上
へ来るように調整する。尚、前記図3及び図4は、内方
へ向って傾斜した炉底2の中央部にスラグタップ5を設
けた形態の表面溶融炉の場合を示し、また図5は傾斜状
の炉底の一端にスラグタップ5を設けた形態の表面溶融
炉の場合を示すものである。Next, the operation of the present invention will be described. First, the angle of repose C 1 of the melted material B is the designed angle of repose C of the furnace body 1.
When it is almost close to the gate, the gate 20 is pulled up to the uppermost position as shown in FIG. On the contrary, when the angle of repose C 1 of the melted material B is significantly smaller than the designed angle of repose C of the furnace body 1, the gate 20 is lowered to the lowest position as shown in FIG. Further, when the angle of repose C 1 of the melted material B is slightly smaller than the designed angle of repose C of the furnace body 1, the descending amount of the gate 20 is appropriately adjusted as shown in FIG. It is adjusted so that the tip of the melted material B is almost on the tip of the furnace bottom 2. 3 and 4 show the case of the surface melting furnace in which the slag tap 5 is provided in the center of the furnace bottom 2 which is inclined inward, and FIG. It shows a case of a surface melting furnace in which a slag tap 5 is provided at one end.
【0020】ホッパ6aから被溶融物供給路6を通して
供給された被溶融物Bは、プッシャ7によって炉本体1
内へ順次押し出されてくる。この時、被溶融物Bの炉内
への供給部の上方にはゲート20が配設されているた
め、当該ゲート20によって、炉底2上へ繰り出されて
炉底2上に擂鉢状の外表面を有する層状に積層される被
溶融物Bの積層形態が変えられることになる。即ち、ゲ
ート20の昇降量を調整することにより、炉底2上に積
層された被溶融物Bの先端が、丁度炉底2の先端部即ち
スラグタップ5の上端外周縁の近傍に位置するように調
整される。これにより、炉底2上の被溶融物Bは、その
外表面から順次溶融されてスラグタップ5内へ円滑に流
下し、プッシャ7が作動されても、その押し出し時の衝
撃等によって炉底2上の被溶融物Bが下方へなだれ落ち
ることも皆無となる。The material to be melted B supplied from the hopper 6a through the material to be melted supply path 6 is pushed by the pusher 7 into the furnace body 1
It is pushed out in order. At this time, since the gate 20 is disposed above the supply part of the material B to be melted into the furnace, the gate 20 feeds the material to the furnace bottom 2 and the mortar-shaped outer surface on the furnace bottom 2. The layered form of the melted material B to be layered having the surface can be changed. That is, by adjusting the amount of elevation of the gate 20, the tip of the melted material B laminated on the furnace bottom 2 is located just near the tip of the furnace bottom 2, that is, the outer peripheral edge of the upper end of the slag tap 5. Adjusted to. As a result, the material B to be melted on the furnace bottom 2 is sequentially melted from the outer surface thereof and smoothly flows down into the slag tap 5, and even if the pusher 7 is operated, it is impacted at the time of extrusion and the like. The upper melted material B is never avalanche downward.
【0021】本発明に係る表面溶融炉に於いては、被溶
融物Bの安息角に合わせてゲート20の昇降動操作を行
ない、炉底2上の被溶融物Bの先端部の位置をスラグタ
ップ5の近傍へ位置せしめることにより、下記の如き被
溶融物の溶融処理操作を高能率で且つ安定して行なうこ
とができる。 内方へ向って傾斜する炉底2の中央部にスラグタッ
プ5を有する構成の表面溶融炉にあっては、両側の炉底
2上で任意の安息角C1 を有する被溶融物Bを、同時に
溶融処理すること。 左右の炉底2上で夫々異なる安息角C1 を有する被
溶融物Bを同時に溶融処理すること。 左右の炉底2上で、二種以上の被溶融物Bの混合体
を一定の混合率の下又は混合率を可変とした状態下で、
同時に溶融処理すること。In the surface melting furnace according to the present invention, the gate 20 is moved up and down according to the angle of repose of the material to be melted B, and the position of the tip of the material to be melted B on the furnace bottom 2 is slagged. By locating it near the tap 5, the following melting processing operation of the material to be melted can be performed with high efficiency and stability. In the surface melting furnace having the slag tap 5 in the central portion of the furnace bottom 2 inclined inward, in the furnace bottoms 2 on both sides, the melted material B having an arbitrary angle of repose C 1 is Melt processing at the same time. Simultaneous melting processing of the melted objects B having different angles of repose C 1 on the left and right furnace bottoms 2, respectively. On the left and right furnace bottoms 2, a mixture of two or more kinds of melted materials B is mixed under a constant mixing ratio or a variable mixing ratio,
Melt processing at the same time.
【0022】また、溶融炉に於ける溶融処理量を減ずる
場合(低負荷運転状態の場合)には、ゲート20を下降
せしめて炉底2上の被溶融物Bの溶融面を短かくし、こ
れによって低負荷運転状態に対応する。Further, in the case of reducing the melting treatment amount in the melting furnace (in the case of low load operation state), the gate 20 is lowered to shorten the melting surface of the material B to be melted on the furnace bottom 2, It corresponds to the low load operation state.
【0023】更に、溶融炉の始動時或はオーバーホール
後の始動時に、被溶融物Bを炉内へ投入して炉底上に被
溶融物Bの溶融傾斜面を形成させる際に、ゲート20を
最低部まで下降させておけば、被溶融物Bを炉内へ投入
した時にこれが炉底2上ではね返ったり、或いは転んだ
りして、未溶融のまヽスラグタップ5から炉外へ出てし
まうことも防ぐことができる。即ち、被溶融物Bをうま
く炉内へ供給して、溶融できる状態に炉底2上へ堆積さ
せることができ、これによって被溶融物Bによる炉のシ
ールも円滑且つ確実に行うことができる。Further, at the time of starting the melting furnace or after starting the overhaul, when the melted material B is charged into the furnace and the melting slope of the melted material B is formed on the bottom of the furnace, the gate 20 is set. If it is lowered to the lowest part, when the material B to be melted is thrown into the furnace, it will bounce or fall on the bottom 2 of the furnace, and it will come out of the furnace from the unmelted slag tap 5. Can also be prevented. That is, the material to be melted B can be well fed into the furnace and deposited on the furnace bottom 2 in a meltable state, whereby the furnace can be smoothly and reliably sealed with the material to be melted B.
【0024】なお本発明の実施態様に於いては、第1図
乃至第4図に示すような炉底の中央部にスラグタップ5
を有し、これの中心線に対して左右対称に被溶融物Bの
ホッパ6a、炉底2、プッシャ7、ゲート20、バーナ
8を配置した構成の表面溶融炉について説明をしたが、
第5図に示すように、炉底の一端にスラグタップ5を有
し、その片側のみに被溶融物Bの供給用ホッパ6a、炉
底2、プッシャ7、ゲート20、バーナ8を配置した構
成の表面溶融炉についても、本発明が適用できることは
勿論である。In the embodiment of the present invention, the slag tap 5 is provided at the center of the furnace bottom as shown in FIGS. 1 to 4.
The surface melting furnace having the configuration in which the hopper 6a for the material B to be melted, the furnace bottom 2, the pusher 7, the gate 20, and the burner 8 are arranged symmetrically with respect to the center line thereof has been described.
As shown in FIG. 5, the slag tap 5 is provided at one end of the furnace bottom, and the hopper 6a for supplying the melted material B, the furnace bottom 2, the pusher 7, the gate 20, and the burner 8 are arranged only on one side thereof. Needless to say, the present invention can be applied to the surface melting furnace.
【0025】[0025]
【発明の効果】本願発明では、炉本体1内へ被溶融物B
を供給する供給部の上方にゲート20を昇降動自在に配
置し、当該ゲート20の昇降位置調整を行なうことによ
り、炉本体1内へ繰り出して炉底2上へ層状に積層せし
めた被溶融物Bの先端が、丁度炉底2のスラグタップ5
側の先端部近傍に位置するようにその積層形態を変える
構成としている。その結果、溶融処理すべき被溶融物B
の種類が変ってその安息角が変動をしても、従前の表面
溶融炉の場合のように、プッシャ7の作動時に未溶融の
被溶融物Bがなだれ状にスラグタップ内へ落下したり、
或いはプッシャ7の作動時に被溶融物Bが円滑且つ十分
に前方へ移動しないと云うようなトラブルの発生を完全
に防止することができる。また、ゲート20の昇降量を
調整することにより、表面溶融炉の低負荷運転にも簡単
に対応することができると共に、被溶融物Bの初期充填
も極めて円滑且つ迅速に行なうことができる。本発明は
上述の通り、一基の表面溶融炉でもって異なる種類の被
溶融物を常に高能率で、しかも安定して溶融処理するこ
とができると共に、高品質で且つ品質の揃った水砕スラ
グが得られると云う優れた実用的効用を奏するものであ
る。According to the present invention, the material B to be melted is placed in the furnace body 1.
The gate 20 is arranged above and below the supply unit for supplying the molten metal, and by adjusting the vertical position of the gate 20, the melted material is fed into the furnace main body 1 and laminated in layers on the furnace bottom 2. The tip of B is just the slag tap 5 on the bottom 2
The laminated form is changed so as to be located near the tip end on the side. As a result, the melted material B to be melt-processed
Even if the type of change occurs and the angle of repose changes, as in the case of the conventional surface melting furnace, the unmelted melted material B drops into the slag tap in an avalanche state when the pusher 7 operates,
Alternatively, it is possible to completely prevent the occurrence of a trouble that the melted material B does not move smoothly and sufficiently when the pusher 7 is operated. Further, by adjusting the amount of raising and lowering of the gate 20, it is possible to easily cope with the low load operation of the surface melting furnace, and the initial filling of the melted material B can be performed extremely smoothly and quickly. INDUSTRIAL APPLICABILITY As described above, the present invention can always and efficiently melt different types of objects to be melted with a single surface melting furnace, and can also provide high quality and uniform quality granulated slag. It has an excellent practical utility that is obtained.
【図面の簡単な説明】[Brief description of drawings]
【図1】本発明の第1実施態様に係る表面溶融炉の要部
を示す縦断面図である。FIG. 1 is a vertical cross-sectional view showing a main part of a surface melting furnace according to a first embodiment of the present invention.
【図2】ゲートの取付状況の概要を示す斜面図である。FIG. 2 is a perspective view showing an outline of a mounting state of a gate.
【図3】安息角の大きな被溶融物に対応するため、ゲー
トを引上げた場合の被溶融物の積層状態を示す説明図で
ある。FIG. 3 is an explanatory view showing a laminated state of the melted object when the gate is pulled up in order to cope with the melted object having a large repose angle.
【図4】安息角の小さな被溶融物に対応するため、ゲー
トを下降せしめた場合の被溶融物の積層状態を示す説明
図である。FIG. 4 is an explanatory diagram showing a stacked state of the melted object when the gate is lowered in order to cope with the melted object having a small repose angle.
【図5】本発明の第2実施態様に係る表面溶融炉のゲー
トの作動状況を示す説明図である。FIG. 5 is an explanatory diagram showing an operating state of a gate of the surface melting furnace according to the second embodiment of the present invention.
【図6】従前の表面溶融炉の一例を示す説明図である。FIG. 6 is an explanatory diagram showing an example of a conventional surface melting furnace.
【図7】従前の表面溶融炉の炉本体の一部を示す縦断面
図である。FIG. 7 is a vertical sectional view showing a part of a furnace body of a conventional surface melting furnace.
A:表面溶融炉、B:被溶融物、B1 :層状の被溶融物
の表面、C:設計安息角、C1 :被溶融物の安息角、H
1 :切り出し部の高さ、H2 :バーナと溶融面間の高
さ、1:炉本体、2:炉底、3:炉側壁、4:炉天井
壁、5:スラグタップ、6:被溶融物供給路、6a:ホ
ッパ、7:プッシャ、8:バーナ、9:高温煙道、1
0:水封式スラグ排出用コンベア、11:空気予熱器、
12:燃料タンク、13:送油ポンプ、14:燃料制御
装置、15:空気圧縮機、16:エアータンク、17:
押込送風機、18:空気供給ダクト、19:空気量調整
タンバ、20:ゲート、21:ゲート昇降装置、22:
サンドシール。A: surface melting furnace, B: melted material, B 1 : surface of layered melted material, C: design repose angle, C 1 : repose angle of melted material, H
1 : height of cutout part, H 2 : height between burner and melting surface, 1: furnace body, 2: furnace bottom, 3: furnace side wall, 4: furnace ceiling wall, 5: slag tap, 6: melted Material supply path, 6a: hopper, 7: pusher, 8: burner, 9: high temperature flue, 1
0: Water-sealed slag discharging conveyor, 11: Air preheater,
12: Fuel tank, 13: Oil pump, 14: Fuel control device, 15: Air compressor, 16: Air tank, 17:
Push blower, 18: Air supply duct, 19: Air amount adjusting tamper, 20: Gate, 21: Gate lifting device, 22:
Sand seal.
───────────────────────────────────────────────────── フロントページの続き (51)Int.Cl.6 識別記号 庁内整理番号 FI 技術表示箇所 F27B 3/18 B09B 3/00 ZAB F27D 3/14 303K // B29K 105:26 ─────────────────────────────────────────────────── ─── Continuation of the front page (51) Int.Cl. 6 Identification code Office reference number FI Technical display area F27B 3/18 B09B 3/00 ZAB F27D 3/14 303K // B29K 105: 26
Claims (2)
部にスラグタップ(5)を、また炉底(2)の外端部上
方に被溶融物供給路(6)を夫々具備すると共に、前記
スラグタップ(5)を中心にして炉底(2)上に被溶融
物(B)を擂鉢状の外表面を有する層状に積層せしめる
炉本体(1)と,前記炉本体(1)の側壁(3)に設け
られ、被溶融物供給路(6)から搬入された被溶融物
(B)を炉本体(1)内へ供給するプッシャ(7)と、
炉本体(1)の天井壁(4)に設けられ、前記積層せし
めた被溶融物の表面(B1 )を加熱溶融するバーナ
(8)と,炉本体(1)内へ被溶融物(B)を供給する
供給部の近傍に上・下方向へ昇降自在に配設され、被溶
融物(B)の安息角(C1 )に応じて炉底(2)上へ供
給した被溶融物(B)の積層形態を変えるゲート(2
0)とを備えたことを特徴とする表面溶融炉。1. A slag tap (5) is provided in the center of a furnace bottom (2) inclined inward, and a melted material supply path (6) is provided above the outer end of the furnace bottom (2). And a furnace body (1) for stacking the melted material (B) on the furnace bottom (2) around the slag tap (5) in a layered form having a mortar-shaped outer surface, and the furnace body (1) A pusher (7) that is provided on the side wall (3) of 1) and that supplies the melted material (B) carried in from the melted material supply path (6) into the furnace body (1);
A burner (8) which is provided on the ceiling wall (4) of the furnace body (1) and heats and melts the surface (B 1 ) of the laminated melted objects, and the melted material (B) into the furnace body (1). ) Is provided so as to be able to move up and down in the vicinity of a supply unit that supplies the melted material () to be supplied onto the furnace bottom (2) according to the angle of repose (C 1 ) of the melted material (B) ( Gate (2) that changes the stacking form of B)
0) and a surface melting furnace.
(5)を、また炉底(2)の他端上方に被溶融物供給路
(6)を夫々具備すると共に、前記炉底(2)上に被溶
融物(B)を傾斜状の外表面を有する層状に積層せしめ
る炉本体(1)と,前記炉本体(1)の側壁(3)に設
けられ、被溶融物供給路(6)から搬入された被溶融物
(B)を炉本体(1)内へ供給するプッシャ(7)と、
炉本体(1)の天井壁(4)に設けられ、前記積層せし
めた被溶融物の表面(B1 )を加熱溶融するバーナ
(8)と,炉本体(1)内へ被溶融物(B)を供給する
供給部の近傍に上・下方向へ昇降自在に配設され、被溶
融物(B)の安息角(C1 )に応じて炉底(2)上へ供
給した被溶融物(B)の積層形態を変えるゲート(2
0)とを備えたことを特徴とする表面溶融炉。2. A slag tap (5) is provided at one end of the inclined furnace bottom (2), and a melted material supply path (6) is provided above the other end of the furnace bottom (2). 2) A furnace main body (1) on which a material to be melted (B) is laminated in a layer having an inclined outer surface, and a side wall (3) of the furnace body (1), which is provided with a material to be melted supply path ( A pusher (7) for supplying the melted substance (B) carried in from 6) into the furnace body (1);
A burner (8) which is provided on the ceiling wall (4) of the furnace body (1) and heats and melts the surface (B 1 ) of the laminated melted objects, and the melted material (B) into the furnace body (1). ) Is provided so as to be able to move up and down in the vicinity of a supply unit that supplies the melted material () to be supplied onto the furnace bottom (2) according to the angle of repose (C 1 ) of the melted material (B) ( Gate (2) that changes the stacking form of B)
0) and a surface melting furnace.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP8495896A JPH09273736A (en) | 1996-04-08 | 1996-04-08 | Surface melting furnace |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP8495896A JPH09273736A (en) | 1996-04-08 | 1996-04-08 | Surface melting furnace |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| JPH09273736A true JPH09273736A (en) | 1997-10-21 |
Family
ID=13845147
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP8495896A Pending JPH09273736A (en) | 1996-04-08 | 1996-04-08 | Surface melting furnace |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH09273736A (en) |
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO1999050600A1 (en) * | 1998-03-27 | 1999-10-07 | Mitsubishi Heavy Industries, Ltd. | Ash melting furnace and ash melting method thereof |
| WO2011013726A1 (en) * | 2009-07-30 | 2011-02-03 | スチールプランテック株式会社 | Arc melting equipment and molten metal manufacturing method using arc melting equipment |
| JP2012037157A (en) * | 2010-08-09 | 2012-02-23 | Jp Steel Plantech Co | Arc melting equipment and method for manufacturing molten metal by using the arc melting equipment |
| JP2013190141A (en) * | 2012-03-13 | 2013-09-26 | Chisaki:Kk | Raw material heating device |
| JP2020051690A (en) * | 2018-09-27 | 2020-04-02 | 株式会社デンソー | Melt holding furnace |
-
1996
- 1996-04-08 JP JP8495896A patent/JPH09273736A/en active Pending
Cited By (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO1999050600A1 (en) * | 1998-03-27 | 1999-10-07 | Mitsubishi Heavy Industries, Ltd. | Ash melting furnace and ash melting method thereof |
| CN100356105C (en) * | 1998-03-27 | 2007-12-19 | 三菱重工业株式会社 | Ash melting furnace and method |
| WO2011013726A1 (en) * | 2009-07-30 | 2011-02-03 | スチールプランテック株式会社 | Arc melting equipment and molten metal manufacturing method using arc melting equipment |
| JP2011033217A (en) * | 2009-07-30 | 2011-02-17 | Jp Steel Plantech Co | Arc melting equipment and method of manufacturing molten metal by using the same |
| JP2012037157A (en) * | 2010-08-09 | 2012-02-23 | Jp Steel Plantech Co | Arc melting equipment and method for manufacturing molten metal by using the arc melting equipment |
| JP2013190141A (en) * | 2012-03-13 | 2013-09-26 | Chisaki:Kk | Raw material heating device |
| JP2020051690A (en) * | 2018-09-27 | 2020-04-02 | 株式会社デンソー | Melt holding furnace |
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