JPS62158913A - Industrial waste material melting furnace - Google Patents

Industrial waste material melting furnace

Info

Publication number
JPS62158913A
JPS62158913A JP29950885A JP29950885A JPS62158913A JP S62158913 A JPS62158913 A JP S62158913A JP 29950885 A JP29950885 A JP 29950885A JP 29950885 A JP29950885 A JP 29950885A JP S62158913 A JPS62158913 A JP S62158913A
Authority
JP
Japan
Prior art keywords
level
control means
amount
industrial waste
hearth
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
Application number
JP29950885A
Other languages
Japanese (ja)
Other versions
JPH0515929B2 (en
Inventor
Takeshi Shimizu
武 清水
Akihiko Yokoyama
明彦 横山
Shogo Ogasawara
小笠原 昌吾
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.)
Osaka Gas Co Ltd
Original Assignee
Osaka Gas Co Ltd
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 Osaka Gas Co Ltd filed Critical Osaka Gas Co Ltd
Priority to JP29950885A priority Critical patent/JPS62158913A/en
Publication of JPS62158913A publication Critical patent/JPS62158913A/en
Publication of JPH0515929B2 publication Critical patent/JPH0515929B2/ja
Granted legal-status Critical Current

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  • Incineration Of Waste (AREA)
  • Gasification And Melting Of Waste (AREA)
  • Crucibles And Fluidized-Bed Furnaces (AREA)

Abstract

PURPOSE:To maintain a level of operation and improve an accuracy in an industrial waste material melting furnace of a hot temperature furnace floor type by a method wherein the furnace floor level is detected by a laser type level sensor, and an amount of gas containing oxygen and carbonic combustibles is controlled in response to a detected level. CONSTITUTION:A level of a hot temperature furnace floor A is detected by a laser type level sensor 26. The sensor 26 is provided with three sets of sensing portions 26a and 26b so as to detect a standard level SL, a high level HL and a low level LL and a discriminating portion 26c may discriminate a level of a furnace floor A. When a level shows the high level HL, a flow rate control means 25 is controlled through a control means 26 in such a way as an amount of gas containing oxygen for combustion is increased to more than that found in the case of the standard level SL. In turn, in the case of the low level LL, a feeding volume control means 22 is controlled through a control means 28 in such a way as an amount of feeding of carbonic combustibles is increased. With this arrangement, it is possible to improve an accuracy in maintaining of a furnace floor level.

Description

【発明の詳細な説明】 〔産業上の利用分野〕 本発明は、供給設備からの炭素系可燃物質に対する給気
装置からの燃焼用酸素含有ガスの吹込みによって、産業
廃棄物を熔融する高温炉床を形成するように構成した産
業廃棄物溶融炉に関する。
Detailed Description of the Invention [Field of Industrial Application] The present invention provides a high-temperature furnace for melting industrial waste by blowing oxygen-containing gas for combustion from an air supply device into carbon-based combustible materials from a supply facility. The present invention relates to an industrial waste melting furnace configured to form a bed.

〔従来の技術〕[Conventional technology]

従来、炭素系可燃物質を炉内に投入するに、はぼ一定量
づつをほぼ一定時間毎に投入し、目視で高温炉床の上面
レベルを確認し、その上面レベルを所定範囲に維持すべ
く、作業者の判断で投入量や投入間隔を酬節していた。
Conventionally, when introducing carbon-based combustible materials into a furnace, a fixed amount of carbon-based combustible material was introduced at approximately regular intervals, the upper surface level of the high-temperature hearth was visually checked, and the upper surface level was maintained within a predetermined range. However, the amount and interval of feeding was determined by the worker.

〔発明が解決しようとする問題点〕[Problem that the invention seeks to solve]

しかし、高温炉床の上面レベルを的確に維持することは
、実際上極めて困難又は不可能であり、下記(イ)ない
しくハ)項の問題を生じやず<、一層の改良の余地があ
った。
However, it is actually extremely difficult or impossible to accurately maintain the upper surface level of the high-temperature hearth, and there is still room for further improvement. Ta.

(イ)高温炉床の上面レベルが高くなり過ぎると、燃焼
域の上方に大量の炭素系可燃物質が未燃状態で堆積する
ため、燃焼域からのCO□がCで還元されて、大量のC
Oが発生して高温炉床よりも上方で燃焼し、エネルギー
ロスが膨大になる。
(b) If the upper surface level of the high-temperature hearth becomes too high, a large amount of carbon-based combustible material will accumulate in an unburned state above the combustion zone, and CO□ from the combustion zone will be reduced with C, resulting in a large amount of C
O is generated and burns above the high-temperature hearth, resulting in enormous energy loss.

(2))高温炉床の上面レベルが低くなり過ぎると、燃
焼域の可燃物質が不足するため、高温炉床の温度低下で
処理能力が低下する。
(2)) If the upper surface level of the high-temperature hearth becomes too low, there will be a shortage of combustible material in the combustion zone, and the temperature of the high-temperature hearth will drop, resulting in a reduction in processing capacity.

(ハ)炉頂圧及び炉底圧の両方を所定通りに制御するこ
とが、高温炉床の厚さ変化で極めて困難又は不能になる
ため、産業廃棄物及び可燃物質が投入時に炉内ガスと共
に炉外に吹出されたり、溶融物排出路への高温ガス供給
不足のために溶融物の固化による詰りを生じたり、溶融
物排出路への高温ガス供給過剰番こよるエネルギーロス
が膨大になる。
(c) It is extremely difficult or impossible to control both the furnace top pressure and the furnace bottom pressure as specified due to changes in the thickness of the high-temperature hearth, so industrial waste and combustible materials are mixed with the gas in the furnace when being charged. The energy loss caused by blowing out of the furnace, clogging due to solidification of the molten material due to insufficient supply of high-temperature gas to the molten material discharge channel, and excessive supply of high-temperature gas to the molten material discharge channel is enormous.

本発明の目的は、高温炉床の上面レベルを精度良好にか
つ依頼性高く所定レベルに維持できるようにする点にあ
る。
An object of the present invention is to enable the upper surface level of a high-temperature hearth to be maintained at a predetermined level with good accuracy and reliability.

〔問題点を解決するための手段〕[Means for solving problems]

本発明の特徴構成は、産業廃棄物を溶融する高温炉床の
上面レベルが標準レベル、その標準レベルより上位の高
レベル、及び、前記標準レベルより下位の低レベルのい
ずれであるかを検出するレーザ式レベル検出器を設け、
そのレベル検出器からの情報に基づいて、前記高温炉床
の上面レベルが前記高レベルである時に前記標準レベル
である時よりも前記高温炉床への燃焼用酸素含有ガス吹
込量を増加するように、給気装置の流量制御手段を自動
操作する第1自動制御手段、並びに、前記高温炉床の上
面レベルが前記低レベルである時に前記標準レベルであ
る時よりも前記高温炉床への炭素系可燃物質投入量を増
加するように、供給設備の投入量調節手段を自動操作す
る第2自動制御手段を設けたことにあり、その作用効果
は次の通りである。
A characteristic configuration of the present invention is to detect whether the upper surface level of a high temperature hearth for melting industrial waste is a standard level, a high level above the standard level, or a low level below the standard level. Equipped with a laser level detector,
Based on the information from the level detector, the amount of oxygen-containing gas blown into the high temperature hearth is increased when the upper surface level of the high temperature hearth is at the high level than when it is at the standard level. a first automatic control means for automatically operating the flow rate control means of the air supply device; and a first automatic control means for automatically operating the flow rate control means of the air supply device; The second automatic control means is provided to automatically operate the input amount adjusting means of the supply equipment so as to increase the amount of combustible material input into the system, and its effects are as follows.

〔作 用〕[For production]

つまり、レベル検知器としてレーザ式のものを利用する
ことによって、自動検知が不可能と考えられていた高温
炉床の上面レベルを、精度良くかつ継続して自動的に確
認できるようになった。
In other words, by using a laser type level detector, it has become possible to automatically and continuously check the upper surface level of a high-temperature hearth, which was previously thought to be impossible to detect automatically.

そして、高温炉床の上面レベルが高レベルになると、燃
焼用酸素含有ガスの吹込量を増大させて、炭素系可燃物
質の消費量を増大させ、例えば単に炭素系可燃物質の投
入量を減少するよりも、高温炉床の上面レベルを迅速に
標準レベルに戻すことができる。
When the upper surface level of the high-temperature hearth reaches a high level, the amount of oxygen-containing gas blown for combustion is increased to increase the consumption of carbon-based combustible materials, and for example, the amount of input of carbon-based combustible materials is simply reduced. The upper surface level of the high-temperature hearth can be quickly returned to the standard level.

また、高温炉床の上面レベルが低レベルになると、炭素
系可燃物質の投入量を増大させて、例えば単に炭素可燃
物質の消費を減少するよりも、高温炉床の上面レベルを
迅速に標準レベルに戻すことができ、かつ、高温炉床の
温度低下を抑制できる。
Also, when the top level of the hot hearth falls to a low level, increasing the input of carbon-based combustibles will quickly bring the top level of the hot hearth to normal levels, for example, rather than simply reducing the consumption of carbon-based combustibles. temperature of the high-temperature hearth can be suppressed.

〔発明の効果〕〔Effect of the invention〕

その結果、高温炉床の上面レベル維持を精度良好にかつ
信頼性高く行えるようになって、COの大量発生による
エネルギーロス、及び、高温炉床の温度低下による処理
能力低下を効果的に防止できると共に、炉頂圧及び炉底
圧の良好な制御を確実に行え、ひいては、産業廃棄物及
び炭素系可燃物資の投入を吹出しの無い状態で容易かつ
良好に行え、かつ、溶融物排出路への高温ガス供給量の
適正化により、溶融物の詰りゃエネルギーロスを効果的
に防止できる。
As a result, the upper surface level of the high-temperature hearth can be maintained with high accuracy and reliability, effectively preventing energy loss due to large amounts of CO generation and reduction in processing capacity due to a drop in the temperature of the high-temperature hearth. At the same time, it is possible to reliably control the furnace top pressure and the furnace bottom pressure, and in turn, it is possible to easily and effectively input industrial waste and carbon-based combustible materials without blowing, and it is possible to easily and efficiently input industrial waste and carbon-based combustible materials into the molten material discharge path. By optimizing the amount of high-temperature gas supplied, energy loss due to clogging of melt can be effectively prevented.

要するに、運転経費、省エネルギー、炉外能の全てにお
いて一段と優れた産業廃棄物溶融炉を提供できるように
なった。
In short, it has become possible to provide an industrial waste melting furnace that is even better in terms of operating costs, energy savings, and furnace performance.

〔実施例〕 次に、第1図及び第2図により実施例を示す。〔Example〕 Next, an example will be shown with reference to FIGS. 1 and 2.

竪型炉(1)の上下中間位置に、産業廃棄物及び炭素系
可燃物質を投入するホッパー(2)を、二重ダンパー(
3)を介して連通させて、ホッパー(2)からの炭素系
可燃物質により炉下部に高温炉床(A)を形成するよう
に構成しである。ブロアー(4)からの燃焼用空気を高
温炉床(A)に供給するノズル(5)を、その出口が高
温炉床(A)の上面よりも下方で炉内底面近くに位置す
る状態で炉下部に付設し、また、点火用バーナ(7)を
炉下部に付設しである。
A hopper (2) for charging industrial waste and carbon-based combustible materials is placed between the top and bottom of the vertical furnace (1) with a double damper (
3) to form a high-temperature hearth (A) in the lower part of the furnace with the carbon-based combustible material from the hopper (2). The nozzle (5) that supplies combustion air from the blower (4) to the high-temperature hearth (A) is placed in the furnace with its outlet located below the top surface of the high-temperature hearth (A) and near the bottom of the furnace. An ignition burner (7) is attached to the lower part of the furnace.

炉(1)の上部を燃焼排ガス用上昇流路(8)とし、そ
の上昇流路(8)の下部に、ブロアー(4)からの空気
を後燃焼用として供給する羽目(9)を接続し、上昇流
路(8)に排塵回収用サイクロン(10)をダクト(1
1)により接続しである。
The upper part of the furnace (1) is an ascending passage (8) for flue gas, and the lower part of the ascending passage (8) is connected to a cuff (9) for supplying air from the blower (4) for after-combustion. , a duct (1
1).

炉底部に溶融廃棄物の排出路(12)を接続して、高温
炉床(A)で溶融した産業廃棄物を回収できるように構
成すると共に、炉底部を開放する蓋体(13)を設けて
ある。
A discharge path (12) for molten waste is connected to the bottom of the furnace so that industrial waste melted in the high-temperature hearth (A) can be recovered, and a lid (13) is provided to open the bottom of the furnace. There is.

前記投入用ホッパー(2)に対して、貯留用ホッパー(
14)からの炭素系可燃物質をゲー) (14a)のレ
ベル調整で設定される厚さで連続搬送して供給するベル
ト式等のコンベヤ(15)、並びに、貯留用ホッパー(
16)からの泥状等の産業廃棄物を連続的に定量供給す
るスクリュ一式等のコンベヤ(17)を設け、また、二
重ダンパー(3)を開閉する流体圧式等の駆動装置(1
8)を、上部ダンパー(3a)を開いて閉じた後下部ダ
ンパー(3b)を開いて閉じる投入動作が設定時間毎に
繰り返し行われるように自動操作するプログラム操作手
段(19)を設け、もって、炭素系可燃物質及び産業廃
棄物を設定時間毎に標準量づつ炉(1)内に自動供給す
るように構成しである。そして、コンベヤ(17)に、
産業廃棄物の送り量を人為的に変更設定する投入量設定
手段(20)を付設し、また、コンベヤ(15)に、炭
素系可燃物質の送り速度を設定器(21)により人為設
定される供給量に見合って調節する投入量調節手段(2
2)を付設しである。
In contrast to the input hopper (2), the storage hopper (
A conveyor (15) such as a belt type conveyor (15) that continuously conveys and supplies the carbon-based combustible material from (14) to a thickness set by the level adjustment in (14a), and a storage hopper (
A conveyor (17) such as a set of screws is installed to continuously supply a fixed amount of industrial waste such as mud from
8) is provided with a program operating means (19) that automatically operates the closing operation of opening and closing the upper damper (3a) and then opening and closing the lower damper (3b) at set time intervals. It is configured to automatically supply standard amounts of carbon-based combustible materials and industrial waste into the furnace (1) at set times. Then, on the conveyor (17),
Input amount setting means (20) for artificially changing and setting the feed amount of industrial waste is attached, and the feed rate of carbon-based combustible material is artificially set on the conveyor (15) by a setting device (21). Input amount adjustment means (2) that adjusts according to the supply amount
2) is attached.

前記ブロアー(4)からノズル(5)への燃焼用空気供
給量を調節するダンパー(23)に、設定器(24)に
より人為設定される吹込量に見合って開度調節する流量
制御手段(25)を付設しである。
The damper (23) that adjusts the amount of combustion air supplied from the blower (4) to the nozzle (5) is provided with a flow rate control means (25) that adjusts the opening according to the amount of blowing that is manually set by the setting device (24). ) is attached.

投光部(26a)からのレーザが受光部(26b)に到
達したか否かで高温炉床(A)の上面レベルを検出する
レーザ式レベル検出器(26)を、投光部(26a)及
び受光部(26a)を上下3段に配置した状態で炉(1
)に付設し、高温炉床(A)の上面レベルが標準レベル
(SL)の上部(S L I+ )と下部(SLL)、
その標準レベル(SL)より上位の高レベル(HL)、
及び、その標準レベル(SL)より下位の低レベル(L
L)のいずれであるかを、受光部(26b)からの情報
によって判定する手段(26c)を、レベル検出器(2
6)に備えさせである。
The light projecting part (26a) is equipped with a laser level detector (26) that detects the upper surface level of the high temperature hearth (A) depending on whether the laser from the light projecting part (26a) reaches the light receiving part (26b). The furnace (1
), the upper surface level of the high-temperature hearth (A) is the standard level (SL), the upper (SL I+) and the lower (SLL),
a high level (HL) higher than the standard level (SL);
and the low level (L) below the standard level (SL).
The means (26c) for determining whether the
6) Prepare for this.

判定用手段(26c)からの情報に基づいて、高温炉床
(A)の上面レベルが高レベル(HL)である時に標準
レベル(SL)である時よりも高温炉床(A)への空気
吹込量を設定量だけ増大するように、かつ、高温炉床(
A)の上面レベルが標準レベル(SL)の下部(SLL
)及び低レベル(+、L)である時に標準レベル(SL
)の上部(SLH)である時よりも高温炉床(A)への
空気吹込量を設定量だけ減少するように、流量制御手段
(25)に修正指示する第1自動制御手段(27)を設
けてある。また、判定用手段(26c)からの情報に基
づいて、高温炉床(A)の上面レベルが低レベル(LL
)である時に標準レベル(SL)である時よりも高温炉
床(A)への炭素系可燃物質投入量を設定量だけ増加す
るように、投入量調節手段(22)に修正指示する第2
自動制御手段(28)を設けてある。
Based on the information from the determining means (26c), when the upper surface level of the hot hearth (A) is at the high level (HL), the air to the hot hearth (A) is lower than when it is at the standard level (SL). In order to increase the blowing amount by the set amount, and
A) The top surface level is the lower part (SLL) of the standard level (SL).
) and low level (+, L), the standard level (SL
), the first automatic control means (27) instructs the flow rate control means (25) to correct the amount of air blown into the high-temperature hearth (A) by a predetermined amount than when it is at the upper part (SLH) of the high temperature hearth (A). It is provided. Also, based on the information from the determination means (26c), the upper surface level of the high temperature hearth (A) is at a low level (LL
) to increase the amount of carbon-based combustible material introduced into the high-temperature hearth (A) by a set amount than when the standard level (SL) is reached.
Automatic control means (28) are provided.

要するに、高温炉床(A)の上面レベルが高レベル(H
L)になれば、空気吹込量増大で炭素系可燃物質の消費
を速めて高温炉床(A)の上面レベルを標準レベル(S
L)に迅速に修正し、また、高温炉床(A)の上面レベ
ルが標準レベル(SL)の下部(SLL)になれば、空
気吹込量減少で炭素系可燃物質の消費を抑制して、高温
炉床(A)の上面レベルの低下を抑え、さらに、高温炉
床(A)の上面レベルが低レベル(LL)になれば、炭
素系可燃物質投入量増大が高温炉床(A)の上面レベル
を標準レベル(SL)で迅速に戻すように構成しである
In short, the upper surface level of the high temperature hearth (A) is at the high level (H
L), the consumption of carbon-based combustible materials is accelerated by increasing the amount of air blowing, and the upper surface level of the high-temperature hearth (A) is brought to the standard level (S).
L), and if the upper surface level of the high-temperature hearth (A) reaches the lower level (SLL) of the standard level (SL), the consumption of carbon-based combustible substances is suppressed by reducing the amount of air blown, If the upper surface level of the high-temperature hearth (A) is suppressed and the upper surface level of the high-temperature hearth (A) becomes a low level (LL), the increase in the amount of carbon-based combustible material input will be reduced to the high-temperature hearth (A). It is configured to quickly return the top surface level to the standard level (SL).

〔別実施例〕[Another example]

ホッパー(2)から投入される産業廃棄物は、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
産業廃棄物あるいはその中間処理物であり、また、炭素
系可燃物質は、例えば、コークス、無煙炭等の燻炭、黒
鉛電極屑等である。
The industrial waste inputted from the hopper (2) is, for example, various kinds of industrial waste such as sewage sludge, tire scraps, municipal waste incineration ash, waste catalyst, etc., or its intermediate treatment products, and carbon-based combustible substances are, for example, , coke, smoky coal such as anthracite, graphite electrode scrap, etc.

ノズル(5)から高温炉床(A)に酸素富化空気や酸素
等を供給してもよく、要するに、適当な給気装置(4)
 、 (5)で燃焼用酸素含有ガスを高温炉床(A)に
吹込むように構成してあればよい。
Oxygen-enriched air, oxygen, etc. may be supplied from the nozzle (5) to the high-temperature hearth (A), in short, a suitable air supply device (4)
, (5) may be configured so that the oxygen-containing gas for combustion is blown into the high temperature hearth (A).

炭素系可燃物質を高温炉床(A)に供給する具体的構成
は適当に変更でき、それらを供給設備(14) 、 (
15) 、 (2) 、 (3)と総称する。
The specific configuration for supplying carbon-based combustible materials to the high-temperature hearth (A) can be changed as appropriate, and they can be connected to supply equipment (14), (
15), (2), and (3).

レーザ式レベル検出器(26)の具体構成も適当に選定
でき、例えば投光部(26a)と受光部(26b)を」
−下2段又は4段以上に設ける等が可能であり、要する
に、高温炉床(A)の上面レベルが標準レベル(SL)
、高レベル(HL)、低レベル(LL)のいずれである
かを検出する機能があればよい。
The specific configuration of the laser level detector (26) can also be selected appropriately, for example, the light emitting part (26a) and the light receiving part (26b).
- It is possible to install the lower two or four or more stages, and in short, the upper surface level of the high-temperature hearth (A) is at the standard level (SL).
, high level (HL), or low level (LL).

供給設備(14) 、 (15) 、 (2) 、 (
3)の投入量調節手段(22)は、コンベヤ(15)を
間歇動作させて1回当たりの供給時間を変更するもの、
ダンパー(3)の開き操作の時間的間隔を変更するもの
、その他適当なものに変更できる。
Supply equipment (14), (15), (2), (
The input amount adjusting means (22) of 3) operates the conveyor (15) intermittently to change the supply time per time;
It can be changed to one that changes the time interval between opening operations of the damper (3), or any other suitable one.

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

第1図及び第2図は本発明の実施例を示し、第1図は全
体縦断面図、第2図は制御構成の概念図である。 (4) 、 (5)・・・・・・給気装置、(14) 
、 (15) 、 (2) 、 (3)・・・・・・供
給設備、(22)・・・・・・投入量調節手段、(25
)・・・・・・流量制御手段、(26)・・・・・・レ
ベル検出器、(27)・・・・・・第1自動制御手段、
(28)・・・・・・第2自動制御手段、(A)・・・
・・・高温炉床。
1 and 2 show an embodiment of the present invention, with FIG. 1 being an overall vertical sectional view and FIG. 2 being a conceptual diagram of a control configuration. (4), (5)... Air supply device, (14)
, (15), (2), (3)... Supply equipment, (22)... Input amount adjustment means, (25
)...Flow control means, (26)...Level detector, (27)...First automatic control means,
(28)...Second automatic control means, (A)...
...High temperature hearth.

Claims (1)

【特許請求の範囲】[Claims] 供給設備(14)、(15)、(2)、(3)からの炭
素系可燃物質に対する給気装置(4)、(5)からの燃
焼用酸素含有ガスの吹込みによって、産業廃棄物を溶融
する高温炉床(A)を形成するように構成した産業廃棄
物溶融炉であって、前記高温炉床(A)の上面レベルが
標準レベル(SL)、その標準レベル(SL)より上位
の高レベル(HL)、及び、前記標準レベル(SL)よ
り下位の低レベル(LL)のいずれであるかを検出する
レーザ式レベル検出器(26)を設け、そのレベル検出
器(26)からの情報に基づいて、前記高温炉床(A)
の上面レベルが前記高レベル(HL)である時に前記標
準レベル(SL)である時よりも前記高温炉床(A)へ
の燃焼用酸素含有ガス吹込量を増加するように、前記給
気装置(4)、(5)の流量制御手段(25)を自動操
作する第1自動制御手段(27)、並びに、前記高温炉
床(A)の上面レベルが前記低レベル(LL)である時
に前記標準レベル(SL)である時よりも前記高温炉床
(A)への炭素系可燃物質投入量を増加するように、前
記供給設備(14)、(15)、(2)、(3)の投入
量調節手段(22)を自動操作する第2自動制御手段(
28)を設けてある産業廃棄物溶融炉。
Industrial waste is removed by blowing oxygen-containing gas for combustion from the air supply devices (4) and (5) into the carbon-based combustible materials from the supply facilities (14), (15), (2), and (3). An industrial waste melting furnace configured to form a melting high-temperature hearth (A), wherein the upper surface level of the high-temperature hearth (A) is at a standard level (SL), which is higher than the standard level (SL). A laser level detector (26) is provided to detect whether the level is a high level (HL) or a low level (LL) lower than the standard level (SL). Based on the information, said hot hearth (A)
The air supply device is configured to increase the amount of combustion oxygen-containing gas blown into the high temperature hearth (A) when the upper surface level is at the high level (HL) than when it is at the standard level (SL). (4), a first automatic control means (27) that automatically operates the flow rate control means (25) of (5), and a first automatic control means (27) that automatically operates the flow rate control means (25) of The supply equipment (14), (15), (2), (3) is configured to increase the amount of carbon-based combustible material input into the high temperature hearth (A) compared to the standard level (SL). a second automatic control means (22) that automatically operates the input amount adjustment means (22);
28) Industrial waste melting furnace.
JP29950885A 1985-12-28 1985-12-28 Industrial waste material melting furnace Granted JPS62158913A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP29950885A JPS62158913A (en) 1985-12-28 1985-12-28 Industrial waste material melting furnace

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP29950885A JPS62158913A (en) 1985-12-28 1985-12-28 Industrial waste material melting furnace

Publications (2)

Publication Number Publication Date
JPS62158913A true JPS62158913A (en) 1987-07-14
JPH0515929B2 JPH0515929B2 (en) 1993-03-03

Family

ID=17873488

Family Applications (1)

Application Number Title Priority Date Filing Date
JP29950885A Granted JPS62158913A (en) 1985-12-28 1985-12-28 Industrial waste material melting furnace

Country Status (1)

Country Link
JP (1) JPS62158913A (en)

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH01123025U (en) * 1988-02-05 1989-08-22
JPH01267911A (en) * 1988-04-19 1989-10-25 Hitachi Cable Ltd Tape-foam oxide based superconductive wire rod and superconductive coil
WO2004042279A1 (en) * 2002-11-07 2004-05-21 Tokyo Elex Co., Ltd. Waste treatment method and treatment facility
JP4504533B2 (en) * 2000-08-15 2010-07-14 メタウォーター株式会社 Sintering method of granular aggregate

Cited By (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH01123025U (en) * 1988-02-05 1989-08-22
JPH01267911A (en) * 1988-04-19 1989-10-25 Hitachi Cable Ltd Tape-foam oxide based superconductive wire rod and superconductive coil
JP4504533B2 (en) * 2000-08-15 2010-07-14 メタウォーター株式会社 Sintering method of granular aggregate
WO2004042279A1 (en) * 2002-11-07 2004-05-21 Tokyo Elex Co., Ltd. Waste treatment method and treatment facility
JP2004205188A (en) * 2002-11-07 2004-07-22 Tokyo Elex Kk Waste treatment method and its device
EP1469253A1 (en) * 2002-11-07 2004-10-20 Tokyo Elex Co., Ltd. Waste treatment method and treatment facility
EP1469253A4 (en) * 2002-11-07 2007-01-03 Tokyo Elex Co Ltd Waste treatment method and treatment facility
US7392753B2 (en) 2002-11-07 2008-07-01 Tokyo Elex Co., Ltd. Process and apparatus for disposal of wastes

Also Published As

Publication number Publication date
JPH0515929B2 (en) 1993-03-03

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