JPS59158909A - Melting furnace for industrial waste - Google Patents
Melting furnace for industrial wasteInfo
- Publication number
- JPS59158909A JPS59158909A JP58032514A JP3251483A JPS59158909A JP S59158909 A JPS59158909 A JP S59158909A JP 58032514 A JP58032514 A JP 58032514A JP 3251483 A JP3251483 A JP 3251483A JP S59158909 A JPS59158909 A JP S59158909A
- Authority
- JP
- Japan
- Prior art keywords
- furnace
- section
- jacket boiler
- temperature
- industrial waste
- 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.)
- Granted
Links
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
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E50/00—Technologies for the production of fuel of non-fossil origin
- Y02E50/30—Fuel from waste, e.g. synthetic alcohol or diesel
-
- 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
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P40/00—Technologies relating to the processing of minerals
- Y02P40/10—Production of cement, e.g. improving or optimising the production methods; Cement grinding
- Y02P40/121—Energy efficiency measures, e.g. improving or optimising the production methods
Landscapes
- Gasification And Melting Of Waste (AREA)
- Processing Of Solid Wastes (AREA)
- Vertical, Hearth, Or Arc Furnaces (AREA)
Abstract
Description
【発明の詳細な説明】
本発明は、産業廃棄物あるいはその中間処理物?、炭素
系可燃物質で形成した高温炉床で溶融させるように構成
すると共に、前記高温炉床から溶融物を取出すように構
成し、@記高温炉床の上方に燃焼排ガス用上昇流路を設
は次産業廃棄物溶融炉に関する。[Detailed Description of the Invention] Is the present invention applicable to industrial waste or intermediate treatment thereof? , is configured to melt in a high-temperature hearth made of carbon-based combustible material, is configured to take out the molten material from the high-temperature hearth, and has an ascending passage for combustion exhaust gas above the high-temperature hearth. relates to secondary industrial waste melting furnaces.
上記産業廃棄物溶融炉は、炉周壁のうち高温炉床の上部
に相当する部分が極めて高温になるために、従来、第3
図に示すように、炉周壁の一部全水冷ジャケット田)に
して、炉(1)の熱洛損に対する保it図っていた。
しかし、その水冷ジャケラ)I311の技術意図は、単
に炉周壁の異常昇温を防止する点に留まってぃ几ために
、ポンプ<P) VCよって大量の水?水冷ジャケット
L”1lVC循環供給すると共に、冷却器、32で水冷
ジャケット賄)からの温水と冷却し、しかも、その温水
の温度が後利用するには低い几めに冷却器′34からT
hk放出しており、その結果、炉(1)の全入熱のJチ
ないし10チもの熱が無軟になり、省エネルギー而で改
善の余地があっ之。In the above-mentioned industrial waste melting furnace, the part of the furnace peripheral wall corresponding to the upper part of the high-temperature hearth becomes extremely high temperature.
As shown in the figure, a part of the furnace peripheral wall was completely water-cooled to protect the furnace (1) from heat damage.
However, the technical intention of the water-cooled jacket I311 is not simply to prevent abnormal temperature rises on the peripheral wall of the reactor, but in order to do so, the pump <P) VC generates a large amount of water. In addition to circulating the water cooling jacket L''11VC, it is cooled with hot water from the water cooling jacket 32, and the temperature of the hot water is too low for later use.
As a result, the total heat input to the furnace (1) becomes as low as J to 10, and there is room for improvement in terms of energy conservation.
また、従来、高温炉床(、U7j・ら上昇する1000
°C以上の燃焼排ガス金、冷却後の燃焼排ガスや水等の
冷却媒?ノズル(絽から上昇流路(81に供給すること
によって、NOx発生やクリンカー発生を抑制できる1
00℃ないしり0θ℃程度に冷却していたが、例えば排
ガス量が溶融処理で発生するガス量のへダ倍ないしん2
倍にもなり、排ガス熱損失が増すと共に、排ガス処理設
備が大型化し、かつ、その設備の運転経費が高くなり、
全体として、省エネルギー面、イニシャルコスト面及ヒ
ランニングコスト向のいずれにおいても改善の余地があ
った。In addition, conventionally, high-temperature hearth (1000
Combustion exhaust gas gold above °C, cooling medium such as combustion exhaust gas or water after cooling? NOx generation and clinker generation can be suppressed by supplying the rising flow path (81) from the nozzle (1).
It was cooled to about 00℃ or 0θ℃, but for example, the amount of exhaust gas was about 2 times the amount of gas generated in the melting process.
This increases the heat loss of the exhaust gas, increases the size of the exhaust gas treatment equipment, and increases the operating cost of the equipment.
Overall, there was room for improvement in terms of energy saving, initial cost, and running cost.
本発明の目的は、上記実情に鑑みて、極めて合理的な改
造により、炉の保護及び燃焼排ガスの温度低下を図りな
がら、熱損失全大巾に減少できるように、かつ、設備経
費及び運転経費?効果的に低減できるようにする点にあ
る。In view of the above-mentioned circumstances, the purpose of the present invention is to protect the furnace and lower the temperature of the combustion exhaust gas, while reducing the total heat loss through extremely rational modification, as well as equipment costs and operating costs. ? The point is to make it possible to reduce it effectively.
本発明VCよる産業廃棄物溶融炉の特徴h’を成は、少
くとも産業廃棄物あるいはその中聞処理物?溶融すべく
炭素系可燃物質で形成した高温炉床の上部に相当する部
分、並びに、高温炉床上方の燃焼排ガス用上昇流路の下
部に相当する部分において、炉周壁がジャケットボイラ
ー胴から成ることにあり、その作用効果は次の通りであ
る。Characteristic h' of the industrial waste melting furnace according to the VC of the present invention consists of at least industrial waste or its intermediate processed material? In the part corresponding to the upper part of the high-temperature hearth made of carbon-based combustible material to be melted, and in the part corresponding to the lower part of the ascending passage for flue gas above the high-temperature hearth, the furnace peripheral wall consists of a jacket boiler shell. Its functions and effects are as follows.
つまり、炉壁溶損を防止する几めの構成としてジャケッ
トボイラー胴?採用すると共に、高温炉床上部に相当す
る部分のみならず、上昇流路下部に相当する部分にジャ
ケットボイラー胴全配置することによって、従来無駄に
なってぃ炉壁からの大量の放熱全十分にかつ利用価値の
高いスチームとして回収利用できるようになっ建。 し
かも、高温炉床からの燃焼排ガスをジャケットボイラー
胴の作用でNOx@生ヲ十分ニ抑制できる温+yあるい
けそれに近い温度VCまで冷却することができ、排ガス
冷却のための冷排ガスや水の供給を無くすあるいは大T
’lJ Vc少くすることがoT能となり、その結果、
排ガス量が大中に減少して、排ガスによる熱損失?顕著
に減少できると共VC排ガス処3!J!設備?十分に小
型化でき、かつ、運転経費?大巾VC低減したものにで
きた。In other words, is the jacket boiler body used as a careful structure to prevent furnace wall meltdown? In addition, by arranging the entire jacket boiler body not only in the area corresponding to the upper part of the high-temperature hearth but also in the area corresponding to the lower part of the ascending passage, a large amount of heat dissipated from the furnace wall, which was previously wasted, can be completely dissipated. Moreover, it can now be collected and used as steam with high utility value. In addition, the combustion exhaust gas from the high-temperature hearth can be cooled down to a temperature VC that is at or near the temperature VC that can sufficiently suppress NOx by the action of the jacket boiler body, and the supply of cold exhaust gas and water for cooling the exhaust gas. Eliminate or large T
'lJ Vc decrease becomes oT ability, and as a result,
Is the amount of exhaust gas significantly reduced and heat loss due to exhaust gas? VC exhaust gas treatment can be significantly reduced! J! Facility? Can it be sufficiently miniaturized and have low operating costs? It was made with a large VC reduction.
その上、ジャケットボイラー胴により得られたスチーム
によって、産業廃棄物の予備乾燥や燃焼用空気の予熱等
が可能であり、金体とし王省エネルギー面で極めて優れ
、かつ、イニシャルコスト及びランニングコストの而で
も優れ、σらtl−1、耐久性及び環境衛生にも優りた
、極めて優秀な産業廃棄物溶融炉を屍供できるようにな
った。Furthermore, the steam obtained from the jacketed boiler body can be used to pre-dry industrial waste and pre-heat combustion air.The metal body is extremely energy efficient and saves initial and running costs. However, it has become possible to provide corpses with an extremely excellent industrial waste melting furnace that has excellent σ, tl-1, durability, and environmental hygiene.
次に、$1図及び第2図に、j:り実施例金示す。Next, FIG. 1 and FIG. 2 show an example of J.
竪型炉il+の上下中間位置に、産業Fs桑物及び炭素
系可燃物質?投入するホッパー(2)金、二重ダン、(
−1:112 介して連通すせて、ホッパー(21から
の炭素系可燃物質により炉底部に高温炉床(8)を形成
すると共に、高温炉原人)の上部に産業廃棄物の充填層
(B)?形成するように構成しである。Is there industrial Fs mulberry material and carbon-based combustible materials in the upper and lower intermediate positions of the vertical furnace IL+? Hopper to feed (2) gold, double dan, (
-1:112 through which a high-temperature hearth (8) is formed at the bottom of the furnace by the carbon-based combustible material from the hopper (21), and a packed bed of industrial waste ( B)? It is configured to form.
ブロアー(4)からの燃焼用突気?高温炉床A)に供給
するノズル(ffil ’ji’ 、その出口が高温炉
床置の上面よりも下方に(q置する状態でF illに
II設L、また、点火用バーナ(7)全戸(1)のF都
に付設しである。Combustion blast from blower (4)? The nozzle (ffil 'ji') that supplies the high-temperature hearth A) is installed in the Fill with its outlet placed below the top surface of the high-temperature hearth (Q), and the ignition burner (7) is installed in all units. It is attached to F city in (1).
炉(1)の上sを燃焼排ガス用上昇流路(8)とし、ソ
ノ上!#−流1i+81の下部に、プロワ−(4)から
の空気?後燃焼用として供給する羽口[91i接続し、
上昇流路(81に排塵回収用サイクロン(1CA”rダ
クト(lりにより接続しである。The upper part of the furnace (1) is used as the ascending passage (8) for combustion exhaust gas, and the upper part of the furnace (1) is used as the ascending flow path (8) for combustion exhaust gas. Is there air from the blower (4) at the bottom of #-Flow 1i+81? Tuyeres supplied for after-combustion [91i connected,
The ascending flow path (81) is connected to a cyclone (1CA"r duct) for collecting waste dust.
炉底部に溶融物排出路0匂?接続して、高温炉床置で溶
融し几産業廃棄物?回収できるように構成すると共に、
炉底部?開閉する蓋Q萄を設けて、炭素系可燃物質の残
滓を取出せるように構成しである。No odor in the melt discharge path at the bottom of the furnace? Connect and melt industrial waste in a high temperature hearth? In addition to configuring it so that it can be collected,
Hearth bottom? A lid Q that can be opened and closed is provided so that the residue of carbon-based combustible substances can be taken out.
tPU+に対するホッパー(2)貫通位置よりも上方か
ら下端部において、炉周壁をジャケットボイラーハ1(
6)で形成し、ホッパー(2)、ノズル(6)、点火用
バーナ(7)、羽口(9)形成筒、溶融物排出路(12
)形成筒等紮、ジャケットボイラー胴(6)の外側金属
壁(6a)及び内側金属壁(6b)に対して貫通止着し
である。 そり、て、ジャケットボイラー胴(6)の下
端側に給水管04)?、かつ、上端側にスチーム回収管
u5)及び安余弁06)全夫々接続して、炉ill内か
らの熱にエリジャケットボイラー胴(6)で発生し之ス
チーム金、スチーム回収管(+5)7)・ら産業廃棄物
予備乾燥装置(図外)に乾燥熱源として供給すべく構成
すると共に、上昇流路(81のガス温度?、NOxやタ
リン力−の発生全抑制すべく、望ましくは200℃ない
しりoo′C程度に、ジャケットボイラー胴(6)によ
り冷却すべく構成しである。From above to the lower end of the hopper (2) penetration position relative to tPU+, cover the furnace peripheral wall with the jacket boiler 1 (
6), a hopper (2), a nozzle (6), an ignition burner (7), a tuyere (9) forming cylinder, a melt discharge passage (12
) Forming a cylinder, etc., the outer metal wall (6a) and the inner metal wall (6b) of the jacket boiler body (6) are penetrated and fixed. Warp, water supply pipe 04) on the lower end side of the jacket boiler body (6)? , and the steam recovery pipe (U5) and the safety valve (06) are all connected to the upper end side, so that the steam generated in the Eli jacket boiler body (6) is absorbed by the heat from inside the furnace, and the steam recovery pipe (+5) is connected to the upper end side. 7) It is configured to supply the industrial waste pre-drying equipment (not shown) as a drying heat source, and the rising flow path (81 gas temperature?, desirably 200 mm) in order to completely suppress the generation of NOx and talin It is configured to be cooled by a jacket boiler shell (6) to about 0.degree.
ジャケットボイラー胴(6)の上部に、内部水位を検出
するセンブーQ7j’に設け、そのセンサーHの検出水
位に基いて給水管O葡のパルプ(1樽ヲ自動開閉操作す
る制御器α9)?設けて、検出水位が設定下限(L+)
に達するとパルプ(+8)’e開き、かつ、検出水位が
設定上限(Lりに達するとパルプ(国を閉じて、水位?
自動的に設定範囲に維持するように構成しである。A sensor Q7j' is installed at the top of the jacket boiler body (6) to detect the internal water level, and a controller α9 automatically opens and closes the water supply pipe O grape pulp (1 barrel) based on the water level detected by the sensor H. The detection water level is set at the lower limit (L+).
When it reaches the upper limit (L), the pulp (+8)'e opens, and when the detected water level reaches the set upper limit (L), the pulp (close the country, water level?
It is configured to automatically maintain within a set range.
ジャケットボイラー胴(6)の上部のうち水位変動範囲
に相当する部分?、耐火物金主桐とする炉周壁上部(ホ
)に対して環状の隙間(21)がある状態で外側に配置
し、隙間(21)の上部をシール材L22+で密閉し、
ブロワ−(4)からの空気金、給気管(社))、隙間力
)及び羽【コ(24)を経て上昇流路(8)に送るよう
に構成し、もって、ジャケットボイラー胴(6)の上端
側部分の熱溶損全防+hするように、ヵ・つ、羽口伐滲
からの空気で排ガス?冷却できるようにしである。The part of the upper part of the jacket boiler body (6) that corresponds to the water level fluctuation range? , disposed outside with an annular gap (21) to the upper part (e) of the furnace peripheral wall made of refractory metal main paulownia, and sealing the upper part of the gap (21) with sealing material L22+,
The air from the blower (4) is configured to be sent to the ascending passage (8) via the air supply pipe, gap force) and vane (24), and thereby the jacket boiler body (6). In order to completely prevent thermal erosion of the upper end of the tuyere, do you use exhaust gas from the air from the tuyere cutting? This allows for cooling.
グクト(11)の入口側に、排ガス温度音検出するセン
サー(社)に設け、冷却し几排ガスを羽目(26)から
上昇流路(8)に供給する排ガス還元用流路しηを設け
、そのセンサー(2(へ)の検出温度を設定範囲内に維
持するように排ガス還元量調節用パルプ(ハ)?自動操
作する制御器cl!9) k設け、排ガスの温度管理全
確実に行えるように構成しである3、ジャケットボイラ
ー胴(s+ k 、ホッパー(21の出口に相当する位
置付近から下方において、内径(D+及び壁間距離(l
t)のいずれもが上方程大になるように形成して、シャ
グツトボイラー胴(6)の高温炉床穴に相当する都がが
冷却され過ぎないように、かつ、高温炉床(A)上部へ
の燃焼用空気供給が均等に行われるように、さらに、炉
tll内の排ガス上昇線速かダスト飛散を少くするよう
に小さくなるように構成しである。 また、ジャケット
ボイラー胴(6)の上部?、下部に比して十分大きい壁
間距離Cl2) Kなるように形成して、排ガス冷却全
安定して行えるように構成しである。 そして、第2図
に示すように、内壁(6b)のうち高温炉床穴に接触す
る部分において、多数の凹部(2))を形成し、凹部鈍
に溜る灰分の断熱作用で高温炉床(Nからの放et−少
くして、溶融及び溶融物流化?円滑に行えるように構成
しである。On the inlet side of the exhaust gas (11), a sensor (company) for detecting exhaust gas temperature sound is provided, and an exhaust gas return flow path η is provided to supply cooled exhaust gas from the slat (26) to the ascending flow path (8). A pulp (c)?controller cl!9 for controlling the amount of exhaust gas reduction is installed to maintain the temperature detected by the sensor (2) within the set range, so that the temperature of the exhaust gas can be completely controlled. 3, jacketed boiler body (s + k), hopper (21
t) are formed so that they become larger upwardly so that the hole corresponding to the high temperature hearth hole of the shaft boiler body (6) is not cooled too much, and the high temperature hearth (A) It is configured so that the combustion air is evenly supplied to the upper part, and the linear velocity of the exhaust gas in the furnace tll is made small so as to reduce dust scattering. Also, the upper part of the jacket boiler body (6)? , the distance between the walls Cl2) K is sufficiently larger than that of the lower part, so that the exhaust gas can be cooled completely stably. As shown in FIG. 2, a large number of recesses (2) are formed in the portion of the inner wall (6b) that contacts the high-temperature hearth hole, and the high-temperature hearth ( The structure is designed to reduce the amount of nitrogen released and facilitate melting and melt flow.
ホッパ=(2)から投入さn、る産業Db秦物は、例え
ば下水汚泥、タイヤ屑、都市ゴミ焼却灰、廃触媒など各
種の産業廃棄物あるいけその中間処理物であり、ま之、
炭素系可燃物質は、例えば、コークス、無煙炭等の練炭
、黒鉛電極屑等である。The industrial Db material inputted from hopper (2) is, for example, various industrial wastes such as sewage sludge, tire scraps, municipal garbage incineration ash, and waste catalysts, as well as intermediately processed products.
Examples of the carbon-based combustible material include coke, briquettes such as anthracite, graphite electrode scraps, and the like.
次に、別の実施例を示す。Next, another example will be shown.
ジャケットボイラー胴(6)の設置範囲は、少くとも両
温炉床(Alの上部及び上昇流路(8)の下部に相当す
る範囲であればよく、高温炉床(Alや排ガスの温度等
の状況に応じて適宜決められるものである。The installation range of the jacket boiler body (6) should be at least the range corresponding to both hot hearths (the upper part of Al and the lower part of the ascending passage (8)), and the range corresponding to the high temperature hearth (the temperature of Al and exhaust gas, etc.). It can be determined as appropriate depending on the situation.
ジャケットボイラー11目+e+で得らiるスチーム全
いかに利用するかは、状況に応じて適当に変更できる。How to utilize all the steam obtained from the 11th jacket boiler +e+ can be changed as appropriate depending on the situation.
ジャケットボイラー胴(6)とは別にその上方に位置さ
せて気水用1[けて、ジャケットボイラー胴(6)内を
水で17tしてもよい。A steam/water tank may be placed above the jacket boiler body (6) separately from the jacket boiler body (6), and 17 tons of water may be filled inside the jacket boiler body (6).
第1図及び第2図は本発明の実施例?示し、第1図は炉
の全体概略縦断面図、第2図は都が拡大断面図である。
第8図は従来例紮示す炉の全体概略縦断面図である。
(6)・・・・・・ジャケットボイラー胴、(8)・・
・・・・燃焼排ガス用上昇流路、(A)・・・・・・高
温炉床。
第1図
48−
第3図Are Figures 1 and 2 examples of the present invention? 1 is a schematic vertical sectional view of the entire furnace, and FIG. 2 is an enlarged sectional view. FIG. 8 is an overall schematic vertical sectional view of a conventional furnace. (6)...Jacket boiler body, (8)...
. . . Rising channel for combustion exhaust gas, (A) . . . High-temperature hearth. Figure 1 48- Figure 3
Claims (1)
で形成し危高温炉床囚で溶融させるように構成すると共
に、前記高温炉床置から溶融物を取出す工う[8i成し
、前記高温炉床置の上方に燃焼排ガス用上昇流路(8)
を設けた産業廃棄物溶融炉であって、炉8壁のうち少く
ともnII記高温炉床國の上部及びWJ記上昇流路(8
)の下部に相当する部分がジャケットボイラー胴(6)
から成る産業廃棄物溶融炉。Industrial waste or its intermediate treatment? , is made of carbon-based combustible material and is configured to be melted in a dangerously high temperature hearth, and has a structure for taking out the molten material from the high temperature hearth. Rising channel (8)
An industrial waste melting furnace equipped with
) is the jacket boiler body (6)
Industrial waste melting furnace consisting of.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP58032514A JPS59158909A (en) | 1983-02-28 | 1983-02-28 | Melting furnace for industrial waste |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP58032514A JPS59158909A (en) | 1983-02-28 | 1983-02-28 | Melting furnace for industrial waste |
Publications (2)
Publication Number | Publication Date |
---|---|
JPS59158909A true JPS59158909A (en) | 1984-09-08 |
JPH0212323B2 JPH0212323B2 (en) | 1990-03-20 |
Family
ID=12361079
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP58032514A Granted JPS59158909A (en) | 1983-02-28 | 1983-02-28 | Melting furnace for industrial waste |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS59158909A (en) |
Cited By (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS63156913A (en) * | 1986-12-19 | 1988-06-30 | Sanki Eng Co Ltd | Horizontal type sludge diffusing and charging device for use in fluidized bed sludge incinerator |
JPH01123026U (en) * | 1988-02-08 | 1989-08-22 | ||
JPH0882408A (en) * | 1994-09-12 | 1996-03-26 | Kitashiba Denki Kk | Waste melting method and waste melting equipment |
JPH10148320A (en) * | 1996-11-19 | 1998-06-02 | Shin Meiwa Ind Co Ltd | Melting-furnace device for incineration ash |
JP2007057113A (en) * | 2005-08-22 | 2007-03-08 | Plantec Inc | Vertical refuse incinerator provided with water tube wall |
JP2019019346A (en) * | 2017-07-12 | 2019-02-07 | Dowaエコシステム株式会社 | Recovery method of noble metal from incineration ash |
Citations (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS5226787U (en) * | 1975-08-16 | 1977-02-24 | ||
JPS52142871A (en) * | 1976-04-22 | 1977-11-29 | Zink Co John | Incinerator for granular waste |
JPS5813916A (en) * | 1981-07-20 | 1983-01-26 | Osaka Gas Co Ltd | Melting method for waste |
-
1983
- 1983-02-28 JP JP58032514A patent/JPS59158909A/en active Granted
Patent Citations (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS5226787U (en) * | 1975-08-16 | 1977-02-24 | ||
JPS52142871A (en) * | 1976-04-22 | 1977-11-29 | Zink Co John | Incinerator for granular waste |
JPS5813916A (en) * | 1981-07-20 | 1983-01-26 | Osaka Gas Co Ltd | Melting method for waste |
Cited By (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS63156913A (en) * | 1986-12-19 | 1988-06-30 | Sanki Eng Co Ltd | Horizontal type sludge diffusing and charging device for use in fluidized bed sludge incinerator |
JPH01123026U (en) * | 1988-02-08 | 1989-08-22 | ||
JPH0882408A (en) * | 1994-09-12 | 1996-03-26 | Kitashiba Denki Kk | Waste melting method and waste melting equipment |
JPH10148320A (en) * | 1996-11-19 | 1998-06-02 | Shin Meiwa Ind Co Ltd | Melting-furnace device for incineration ash |
JP2007057113A (en) * | 2005-08-22 | 2007-03-08 | Plantec Inc | Vertical refuse incinerator provided with water tube wall |
JP2019019346A (en) * | 2017-07-12 | 2019-02-07 | Dowaエコシステム株式会社 | Recovery method of noble metal from incineration ash |
Also Published As
Publication number | Publication date |
---|---|
JPH0212323B2 (en) | 1990-03-20 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
US4346661A (en) | Furnace for treating industrial wastes | |
EP0884545B1 (en) | Electric ARC melting furnace | |
US3556025A (en) | Incinerator for refuse | |
CN2910956Y (en) | Coiled-pipe air-seal type active chimney of evaporated cooling flue of steelmaking converter | |
JPS59158909A (en) | Melting furnace for industrial waste | |
CN207407351U (en) | The intermittent vibrating, deslagging device of waste incinerator | |
US3985518A (en) | Oxygen refuse converter | |
EP0846919B1 (en) | Burning/melting method of waste melting furnace | |
JPS59150005A (en) | Reactor iron making equipment | |
JPS621549Y2 (en) | ||
JP3734177B2 (en) | Waste melting method | |
EP0385098B1 (en) | Tubular rotary furnace with combustion air blown-in radially through the lining | |
JPS5822818A (en) | Structure of side wall and back surface of incinerator | |
CN210321165U (en) | Casting furnace | |
US2771285A (en) | Regenerator | |
JP3438573B2 (en) | Gasification and melting furnace for waste and gasification and melting method | |
JP3542831B2 (en) | Waste melting furnace | |
JPS6240607B2 (en) | ||
JPH109554A (en) | Control method of upper stage tuyere air blowing quantity for waste melting furnace | |
JPH109530A (en) | Sub raw material charging method of waste melting furnace | |
JPS6344660Y2 (en) | ||
CA1148411A (en) | Furnace for treating industrial wastes | |
JPH02293513A (en) | Method for controlling molten slag in circling type melting furnace | |
JP3851031B2 (en) | Melting furnace | |
JP3146164B2 (en) | Multi-chamber slag generator |