JPH0515929B2 - - Google Patents
Info
- Publication number
- JPH0515929B2 JPH0515929B2 JP29950885A JP29950885A JPH0515929B2 JP H0515929 B2 JPH0515929 B2 JP H0515929B2 JP 29950885 A JP29950885 A JP 29950885A JP 29950885 A JP29950885 A JP 29950885A JP H0515929 B2 JPH0515929 B2 JP H0515929B2
- Authority
- JP
- Japan
- Prior art keywords
- level
- hearth
- temperature hearth
- amount
- temperature
- 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.)
- Expired - Lifetime
Links
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims description 22
- 229910052799 carbon Inorganic materials 0.000 claims description 22
- 239000000463 material Substances 0.000 claims description 21
- 239000002440 industrial waste Substances 0.000 claims description 16
- 238000002485 combustion reaction Methods 0.000 claims description 12
- 239000007789 gas Substances 0.000 claims description 11
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 claims description 8
- 229910052760 oxygen Inorganic materials 0.000 claims description 8
- 239000001301 oxygen Substances 0.000 claims description 8
- 230000008018 melting Effects 0.000 claims description 6
- 238000002844 melting Methods 0.000 claims description 6
- 238000007664 blowing Methods 0.000 claims description 5
- 230000001174 ascending effect Effects 0.000 description 3
- 230000000694 effects Effects 0.000 description 3
- 239000012768 molten material Substances 0.000 description 3
- 239000000155 melt Substances 0.000 description 2
- 238000000034 method Methods 0.000 description 2
- 239000002699 waste material Substances 0.000 description 2
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 description 1
- RHZUVFJBSILHOK-UHFFFAOYSA-N anthracen-1-ylmethanolate Chemical compound C1=CC=C2C=C3C(C[O-])=CC=CC3=CC2=C1 RHZUVFJBSILHOK-UHFFFAOYSA-N 0.000 description 1
- 239000003830 anthracite Substances 0.000 description 1
- 239000003054 catalyst Substances 0.000 description 1
- 239000000571 coke Substances 0.000 description 1
- 230000007423 decrease Effects 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 239000003546 flue gas Substances 0.000 description 1
- 239000013067 intermediate product Substances 0.000 description 1
- 238000011084 recovery Methods 0.000 description 1
- 239000010801 sewage sludge Substances 0.000 description 1
- 239000000779 smoke Substances 0.000 description 1
- 238000007711 solidification Methods 0.000 description 1
- 230000008023 solidification Effects 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 238000004056 waste incineration Methods 0.000 description 1
Landscapes
- Incineration Of Waste (AREA)
- Gasification And Melting Of Waste (AREA)
- Crucibles And Fluidized-Bed Furnaces (AREA)
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
によつて、産業廃棄物を溶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] [Industrial Application Field] The present invention melts 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 high temperature hearth.
従来、炭素系可燃物質を炉内に投入するに、ほ
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
や投入間隔を調節していた。
Conventionally, when introducing carbon-based combustible materials into a furnace, a constant amount of carbon-based combustible material was introduced at approximately constant intervals, the upper surface level of the high-temperature hearth was visually confirmed, and the upper surface level was maintained within a predetermined range. The amount and interval of feeding was adjusted by the operator's judgment.
しかし、高温炉床の上面レベルを的確に維持す
ることは、実際上際めて困難又は不可能であり、
下記(イ)ないし(ハ)項の問題を生じやすく、一層の改
良の余地があつた。
However, it is actually extremely difficult or impossible to accurately maintain the upper surface level of the high-temperature hearth.
The following problems (a) to (c) were likely to occur, and there was room for further improvement.
(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CO2がCで還
元されて、大量のCO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 level of the high temperature hearth becomes too high,
Because a large amount of carbon-based combustible material is deposited in an unburned state above the combustion zone, CO 2 from the combustion zone is reduced with C, producing a large amount of CO, which burns above the high-temperature hearth. Energy loss will be enormous.
(ロ) 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。(b) If the top level of the high temperature hearth becomes too low,
Due to the lack of combustible material in the combustion zone, the temperature of the high-temperature hearth decreases, reducing 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によるエネルギーロス
が膨大になる。(c) Because it is extremely difficult or impossible to control both the furnace top pressure and furnace bottom pressure as specified due to changes in the thickness of the high-temperature hearth, industrial waste and combustible materials may be mixed with the gas in the furnace when being charged. being blown out of the furnace,
Insufficient supply of high-temperature gas to the molten material discharge channel causes clogging due to solidification of the molten material, and excessive supply of high-temperature gas to the molten material discharge channel causes enormous energy loss.
本発明の目的は、高温炉床の上面レベルを精度
良好にかる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 maintain the upper surface level of a high-temperature hearth at a predetermined level with good accuracy and reliability.
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. a laser level detector is provided, and based on information from the level detector, when the upper surface level of the hot hearth is at the high level, more combustion oxygen is supplied to the hot hearth 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 so as to increase the amount of gas blown into the air supply device; The second automatic control means is provided for automatically operating the input amount adjusting means of the supply equipment so as to increase the amount of carbon-based combustible material input into the high-temperature hearth, and its effects are as follows. be.
つまり、レベル検知器としてレーザ式のものを
利用することによつて、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つた。
In other words, by using a laser-type level detector, it is now possible to automatically and accurately check the top surface level of a high-temperature hearth, which was previously thought to be impossible. Ta.
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. than,
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.
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つて、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
物質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、溶融物の詰りやエネルギーロスを
効果的に防止できる。
As a result, it becomes possible to maintain the upper surface level of the high-temperature hearth 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 charge industrial waste and carbon-based combustible materials without blowing, and it is possible to control the furnace top pressure and furnace bottom pressure easily and effectively. By optimizing the amount of high-temperature gas supplied, clogging of the melt and energy loss can be effectively prevented.
要するに、運転経費、省エネルギー、炉性能の
全てにおいて一段と優れた産業廃棄物溶融炉を提
供できるようになつた。 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.
次に、第1図及び第2図により実施例を示す。 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ツパー2を、二重ダン
パー3を介して連通させて、ホツパー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
るように構成してある。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を炉下部に付設してある。 A hopper 2 for charging industrial waste and carbon-based combustible materials is placed between the upper and lower sides of the vertical furnace 1 and communicated via a double damper 3. It is configured to form a floor A. A nozzle 5 for supplying combustion air from the blower 4 to the high-temperature hearth A is attached to the lower part of the furnace with its outlet located below the top surface of the high-temperature hearth A and near the bottom of the furnace, and also for ignition. A 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口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11に
より接続してある。 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 with a tuyere 9 that supplies air from the blower 4 for after-combustion, and the ascending passage 8 is used for collecting exhaust gas. A cyclone 10 is connected by a duct 11.
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 molten waste discharge passage 12 is connected to the bottom of the furnace,
A lid body 13 configured to allow recovery of industrial waste melted in the high-temperature hearth A and opening the bottom of the hearth.
is provided.
前記投入用ホツパー2に対して、貯留用ホツパ
ー14からの炭素系可燃物質をゲート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
ツパー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ユー式等のコンベヤ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18を、上記ダンパー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、もつて、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てあ
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
給量に見合つて調節する投入量調節手段22を付
設してある。 A conveyor 15 such as a belt type conveyor 15 that continuously conveys and supplies the carbon-based combustible material from the storage hopper 14 to the input hopper 2 at a thickness set by level adjustment of the gate 14a, and a storage hopper A conveyor 17 such as a screw type that continuously supplies a fixed amount of industrial waste such as mud from the damper 16 is provided, and a drive device 18 such as a hydraulic type that opens and closes the double damper 3 is provided. A program operating means 19 is provided that automatically operates the input operation of opening and closing the lower damper 3b after closing it at set time intervals, and thereby generates a standard amount of carbon-based combustible materials and industrial waste at set time intervals. It is configured to automatically feed into the furnace 1 one by one. The conveyor 17 is provided with an input amount setting means 20 for artificially changing and setting the feed amount of industrial waste, and the conveyor 15 is provided with an input amount setting means 20 for artificially setting the feed rate of the carbon-based combustible material by a setting device 21. An input amount adjusting means 22 is provided to adjust the amount of input according to the amount of supply.
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つて開度調節する
流量制御手段25を付設してある。 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.
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(SLH)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
(LL)のいずれであるかを、受光部26bからの
情報によつて判定する手段26cを、レベル検出
器26に備えさせてある。 A laser level detector 26 that detects the level of the upper surface of the high-temperature hearth A based on whether the laser beam from the light projecting part 26a reaches the light receiving part 26b is arranged in three stages, with the light projecting part 26a and the light receiving part 26a arranged in upper and lower stages. Furnace 1
attached to the high temperature hearth A, the upper surface level of the high temperature hearth A is the upper (SLH) and lower (SLL) of the standard level (SL), the high level (HL) above the standard level (SL), and
The level detector 26 is provided with means 26c for determining which of the low levels (LL) below the standard level (SL) is, based on information from the light receiving section 26b.
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(LL)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 determination means 26c, when the upper surface level of the high temperature hearth A is at the high level (HL), the high temperature hearth A is higher than when it is at the standard level (SL).
so that the amount of air blown into the furnace is increased by the set amount, and the upper surface level of high temperature hearth A is at the standard level
Flow rate control means so that the amount of air blown into the high temperature hearth A is reduced by a set amount when the temperature is at the lower level (SLL) and the lower level (LL) than when it is at the upper level (SLH) of the standard level (SL). The first to give correction instructions to 25
Automatic control means 27 are provided. Also, based on the information from the determination means 26c, when the upper surface level of the high-temperature hearth A is at the low level (LL), the carbon-based combustible material is injected into the high-temperature hearth A more than when it is at the standard level (SL). A second automatic control means 28 is provided for instructing the input amount adjusting means 22 to correct the amount so as to increase the amount by a set amount.
要するに、高温炉床Aの上面レベルが高レベル
(HL)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(SL)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てある。 In short, if the top surface level of high temperature hearth A reaches a high level (HL), the consumption of carbon-based combustible materials is accelerated by increasing the amount of air blowing, and the top surface level of high temperature hearth A is quickly corrected to the standard level (SL). However, 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 materials is suppressed by reducing the amount of air blown, and the upper surface level of the high-temperature hearth A becomes lower than the standard level (SL). In addition, if the upper surface level of high-temperature hearth A becomes a low level (LL), an increase in the amount of carbon-based combustible material input will quickly return the upper surface level of high-temperature hearth A to the standard level (SL). It is configured.
ホツパー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、無煙炭等の煉炭、黒煙電極屑等である。
The industrial waste inputted from the hopper 2 is, for example, various industrial wastes such as sewage sludge, tire scraps, municipal waste incineration ash, waste catalysts, etc., or their intermediate products, and the carbon-based combustible substances are, for example, coke. , briquettes such as anthracite, black smoke electrode scraps, 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, and in short, the structure may be such that oxygen-containing gas for combustion is blown into the high-temperature hearth A using appropriate air supply devices 4 and 5. Bye.
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 structure for supplying carbon-based combustible materials to the high-temperature hearth A can be changed as appropriate, and they can be connected to the supply equipment 14,
Collectively referred to as 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
上下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 projecting section 26a and the light receiving section 26b can be provided in two or more upper and lower stages.
In short, it is sufficient if there is a function to detect whether the upper surface level of the high temperature hearth A is a standard level (SL), a high level (HL), or a low level (LL).
供給設備14,5,2,3の投入量調節手段2
2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。 Input amount adjustment means 2 for supply equipment 14, 5, 2, 3
2 can be changed to a method in which the conveyor 15 is operated intermittently to change the supply time per time, a time interval between opening operations of the damper 3 is changed, or any other suitable method.
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 rate control means, 26...Level detector, 27...First automatic control means, 28...Second automatic control means, A
...High-temperature hearth.
Claims (1)
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つて、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
物溶融炉であつて、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。1. A high-temperature hearth A for melting industrial waste is formed 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. In the industrial waste melting furnace configured as follows, the upper surface level of the high-temperature hearth A is a standard level (SL), a high level (HL) higher than the standard level (SL), and the standard level (SL). ) is provided, and based on information from the level detector 26, the upper surface level of the high temperature hearth A is set to the high level. The flow rate control means 25 of the air supply devices 4 and 5 is configured to increase the amount of combustion oxygen-containing gas blown into the high temperature hearth A when the temperature is at the standard level (SL) than when the temperature is at the standard level (SL). a first automatic control means 27 for automatic operation, and a carbon system to the high temperature hearth A when the upper surface level of the high temperature hearth A is at the low level (LL) than when it is at the standard level (SL); The industrial waste melting furnace is provided with a second automatic control means 28 for automatically operating the input amount adjusting means 22 of the supply equipment 14, 15, 2, and 3 so as to increase the amount of combustible material input.
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 JPS62158913A (en) | 1987-07-14 |
| JPH0515929B2 true 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) |
Families Citing this family (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH064187Y2 (en) * | 1988-02-05 | 1994-02-02 | 大阪瓦斯株式会社 | Waste melting furnace |
| 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 |
| JP2004205188A (en) * | 2002-11-07 | 2004-07-22 | Tokyo Elex Kk | Waste treatment method and treatment equipment |
-
1985
- 1985-12-28 JP JP29950885A patent/JPS62158913A/en active Granted
Also Published As
| Publication number | Publication date |
|---|---|
| JPS62158913A (en) | 1987-07-14 |
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| Date | Code | Title | Description |
|---|---|---|---|
| EXPY | Cancellation because of completion of term |