JPS63315819A - Waste melting furnace - Google Patents

Waste melting furnace

Info

Publication number
JPS63315819A
JPS63315819A JP14952687A JP14952687A JPS63315819A JP S63315819 A JPS63315819 A JP S63315819A JP 14952687 A JP14952687 A JP 14952687A JP 14952687 A JP14952687 A JP 14952687A JP S63315819 A JPS63315819 A JP S63315819A
Authority
JP
Japan
Prior art keywords
take
melted
melting furnace
disposed
substance
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Pending
Application number
JP14952687A
Other languages
Japanese (ja)
Inventor
Kotaro Taniguchi
谷口 興太郎
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.)
Kubota Corp
Original Assignee
Kubota Corp
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 Kubota Corp filed Critical Kubota Corp
Priority to JP14952687A priority Critical patent/JPS63315819A/en
Publication of JPS63315819A publication Critical patent/JPS63315819A/en
Pending legal-status Critical Current

Links

Landscapes

  • Gasification And Melting Of Waste (AREA)

Abstract

PURPOSE:To smoothly take out a substance to be melted and disposed of without mounting a heating device for an exclusive use to a take-out part, by a method wherein a take-out part is disposed in the vicinity of the storage level of a substance to be melted and disposed of so that the substance to be melted and disposed of can be taken out through overflow, and a smoke passage is connected to the take-out part. CONSTITUTION:A take-out part 11 to take out a substance to be melted and disposed of through natural flow down from a secondary melting furnace is located in a secondary melting furnace 6, mounted to a plasma torch 5 and at a position in the vicinity of the storage level of the substance to be melted and disposed of so that the substance to be melted and disposed of can be taken out through overflow. A smoke passage 7 through which high temperature exhaust gas through a passage 4 is exhausted is connected to a take-out part 11. A rotary cooler 12 to continuously receive the overflowing dropping substance to be melted and disposed of, cool cooling air from the outside for cooling, and exhaust the cooling air to the outside of a system when its temperature is reduced to, for example, 900 deg.C, is situated below the take-out part 11, and slug discharged from the rotary cooler 12 is discharged in a crystallized and gradually cooled state.

Description

【発明の詳細な説明】 〔産業上の利用分野〕 本発明は、被処理物を充填状態で自重下降させる環状供
給路に、その全周にわたって溶融室を連通接続するとと
もに、前記溶融室の底部中央に溶融処理物を高温排ガス
と共に排出する通路を設け、前記排出通路からの溶融処
理物を受止めて貯留する二次溶融炉を設け、前記二次溶
融炉に、そこからの溶融処理物を自然流下により取出す
取出部を設けると共に、前記排出通路からの高温排ガス
を排出する煙道を接続してある廃棄物溶融炉に関する。
Detailed Description of the Invention [Industrial Field of Application] The present invention provides a method for connecting a melting chamber over its entire circumference to an annular supply channel through which the processed material is lowered under its own weight in a filled state, A passage for discharging the melted material together with high-temperature exhaust gas is provided in the center, a secondary melting furnace is provided for receiving and storing the melted material from the discharge passage, and the melted material from there is provided in the secondary melting furnace. The present invention relates to a waste melting furnace which is provided with a take-out portion for taking out the waste by gravity flow and is connected to a flue for discharging high-temperature exhaust gas from the discharge passage.

〔従来の技術〕[Conventional technology]

従来の上記廃棄物溶融炉では、取出部を二次溶融炉の底
部に配置し、煙道を溶融処理物の貯留レベルよりも高い
位置に接続してあった(例えば特開昭58−49824
号公報)。
In the conventional waste melting furnace mentioned above, the take-out part was arranged at the bottom of the secondary melting furnace, and the flue was connected to a position higher than the storage level of the melted material (for example, Japanese Patent Application Laid-Open No. 58-49824
Publication No.).

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

しかし、取出部から溶融処理物をスムーズに取出すには
、取出部に専用の加熱装置を設けて、溶融処理物の流動
状態を維持しなければ、自然放熱によって流動性を失っ
てしまう欠点があった。
However, in order to smoothly take out the molten material from the take-out section, a special heating device must be installed in the take-out section to maintain the fluidity of the molten material, otherwise it will lose its fluidity due to natural heat radiation. Ta.

本発明の目的は、取出部に専用の加熱装置を設けなくて
も、溶融処理物をスムーズに取出せるようにする点にあ
る。
An object of the present invention is to make it possible to smoothly take out the melted product without providing a dedicated heating device in the take-out section.

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

本発明の廃棄物溶融炉の特徴構成は、取出部をオーバー
フローによって溶融処理物を取出すように溶融処理物の
貯留レベル近くに配置し、煙道を前記取出部に接続して
あることにあり、その作用効果は次の通りである。
The characteristic configuration of the waste melting furnace of the present invention is that the take-out part is disposed near the storage level of the melted product so as to take out the melted product by overflow, and the flue is connected to the take-out part, Its effects are as follows.

〔作 用〕[For production]

つまり、二次溶融炉からの高温排ガスは、取出部を通っ
て煙道に流れながら、取出部からオーバーフローによっ
て取出される溶融処理物に熱エネルギーを与え、溶融処
理物の流動性を維持する。
In other words, the high-temperature exhaust gas from the secondary melting furnace flows into the flue through the take-out part and gives thermal energy to the melted material taken out by overflow from the take-out part, thereby maintaining the fluidity of the melted material.

〔発明の効果〕〔Effect of the invention〕

従って、取出し部に専用の加熱装置を設けなくとも、溶
融処理物をその流動性を維持した状態でスムーズに取出
すことができ、簡単な構造によって廃棄物の溶融処理に
おけるイニシャルコスト及びランニングコストを下げる
ことができるに至った。
Therefore, it is possible to smoothly take out the melted material while maintaining its fluidity without installing a dedicated heating device in the take-out section, and the simple structure reduces the initial cost and running cost of waste melting processing. I was able to do this.

〔実施例〕〔Example〕

次に、本発明の実施例を、図面に基づいて説明する。 Next, embodiments of the present invention will be described based on the drawings.

第1図に示すように、供給貯留部(1)から供給される
被処理物を、炉外周壁(2)の上側部分(2a)に対す
る下側部分(2b)の駆動回転により全周にわたって分
散させ、被処理物を充填状態で自重下降させる環状供給
路(R)を構成し、前記環状供給路(R)に、その全周
にわたって溶融室(3)を連通接続するとともに、前記
溶融室(3)の底部中央に溶融処理物を高温排ガスと共
に排出する通路(4)を設け、通路(4)からの溶融処
理物を受止めて貯留すると共に、溶融処理物中に含まれ
る未溶融物を滞留させて完全に溶融させるために、プラ
ズマトーチ(5)を付設した二次溶融炉(6)を設け、
二次溶融炉(6)に、そこからの溶融処理物を自然流下
により取出す取出部(11)を、オーバーフローによっ
て溶融処理物を取出すように溶融処理物の貯留レベル近
くに配置し、前記通路(4)からの高温排ガスを排出す
る煙道(7)を、取出部(11)に接続し、煙道(7)
には、その下流側にボイラー等の廃熱回収装置(8)を
設けて、下水汚泥、し原汚泥、都市ゴミ残渣、並びに、
プラスチックゴミ等の夫々の単独物又は混合物を溶融処
理する廃棄物溶融炉を構成してある。
As shown in Fig. 1, the workpiece supplied from the supply reservoir (1) is distributed over the entire circumference by driving rotation of the lower part (2b) relative to the upper part (2a) of the outer peripheral wall (2) of the furnace. The melting chamber (3) is connected to the annular supply path (R) over its entire circumference, and the melting chamber (3) is connected to the annular supply path (R) over its entire circumference. 3) is provided with a passageway (4) in the center of the bottom for discharging the melted material together with the high-temperature exhaust gas, which receives and stores the melted material from the passageway (4) and removes unmelted materials contained in the melted material. A secondary melting furnace (6) equipped with a plasma torch (5) is provided to retain and completely melt the melt.
In the secondary melting furnace (6), a take-out part (11) for taking out the melted product from there by gravity flow is arranged near the storage level of the melted product so as to take out the melted product by overflow, and the passage ( Connect the flue (7) for discharging high-temperature exhaust gas from 4) to the extraction part (11), and
A waste heat recovery device (8) such as a boiler is installed downstream of the sewage sludge, raw sludge, municipal waste residue, and
A waste melting furnace is configured to melt plastic waste and other individual objects or mixtures thereof.

前記プラズマトーチ(5)は、放電させるための受電設
備(10)と、エアー、窒素、アルゴンガス、水性ガス
等の内の一種のプロセスガスを加熱対象に高圧で噴出さ
せるプロセスガス供給装置(9)を備え、プロセスガス
を放電エネルギーによって高温のプラズマにして吹出す
ように形成してあり、前記溶融室(3)では1350℃
〜1450℃に加熱された処理物が、二次溶融炉(6)
内の貯留室(6A)では、1500℃〜1600℃にプ
ラズマで加熱され未溶融物でも完全に溶融される。尚、
プロセスガスとしては、処理物中に有機分の多い場合は
エアーを使い、無機質の多い場合は窒素ガスを使う。
The plasma torch (5) includes a power receiving equipment (10) for discharging, and a process gas supply device (9) for ejecting a type of process gas such as air, nitrogen, argon gas, water gas, etc. to a heating target at high pressure. ), the process gas is turned into high-temperature plasma by discharge energy, and is blown out.
The processed material heated to ~1450°C is transferred to the secondary melting furnace (6)
The storage chamber (6A) inside is heated by plasma to 1500°C to 1600°C, and even unmelted materials are completely melted. still,
As the process gas, air is used if the processed material contains a large amount of organic matter, and nitrogen gas is used if the material contains a large amount of inorganic material.

前記取出部(11)の下方には、オーバーフローして落
下した溶融処理物を連続的に受止めて、外部からの冷却
空気を供給によって2〜bの冷却速度で冷やし、900
℃になったところで系外に排出されるロータリークーラ
ー(12)を設けてあり、このロータリークーラー(1
2)から排出されるスラグは、結晶徐冷化されて出て来
る。
The lower part of the take-out part (11) continuously receives the melted material that has overflowed and fallen, and cools it at a cooling rate of 2 to 900 m by supplying cooling air from the outside.
A rotary cooler (12) is provided, which is discharged from the system when the temperature reaches ℃.
The slag discharged from 2) is slowly cooled into crystals.

尚、ロータリークーラー(12)から排ガスは、排ガス
ダクト(13)を介して煙道に排出される。
Note that the exhaust gas from the rotary cooler (12) is discharged into the flue via the exhaust gas duct (13).

前記煙道(7)には、取出部(11)からの高温排ガス
を、溶融処理物と共に下方に向けて並流した後、上方の
二次燃焼室(14)にニーターンさせるニーターン経路
(U)を形成してあり、二次燃焼室(14)では、外部
からのエアーの供給によって、排ガス中の未燃焼ガスを
完全燃焼させるように構成してある。
The flue (7) has a knee-turn path (U) in which the high-temperature exhaust gas from the take-out part (11) flows downward together with the molten material and then knee-turns into the upper secondary combustion chamber (14). The secondary combustion chamber (14) is configured to completely burn unburned gas in the exhaust gas by supplying air from the outside.

図中(15)は、水冷ジャケットで取出部(11)の耐
火度を維持してある。
In the figure (15), the fire resistance of the extraction part (11) is maintained by a water cooling jacket.

〔別実施例〕[Another example]

前記プラズマトーチ(5)は、1本以外に複数本でも良
く、燃焼式の加熱バーナであっても良い。
The plasma torch (5) may be one or more, and may be a combustion type heating burner.

前記煙道(7)には、第2図に示すように、排ガス中か
ら回収された低沸点重金属を含有する・ダストに対する
低温溶融装置(16)を、二次燃焼室(14)の出口の
下流側に配設して、排ガスの熱エネルギーを利用してダ
ストを溶融するように構成しても良く、図中(17)は
ダスト供給装置で、(18)は、スラグ搬出装置である
As shown in Figure 2, the flue (7) is equipped with a low-temperature melting device (16) for dust containing low-boiling heavy metals recovered from the exhaust gas at the outlet of the secondary combustion chamber (14). It may be arranged on the downstream side to melt the dust using the thermal energy of the exhaust gas. In the figure, (17) is a dust supply device, and (18) is a slag transport device.

又、1600℃で溶融したスラグの利用方法によっては
、空冷ロータリークーラー(12)以外の水冷式のフラ
イドコンベア等でも可能となり、この時のスラグは、一
般に水滓スラグと呼ばれている。
Furthermore, depending on how the slag melted at 1600° C. can be used, it may be possible to use a water-cooled fried conveyor other than the air-cooled rotary cooler (12), and the slag at this time is generally called slag slag.

尚、特許請求の範囲の項に図面との対照を便利にする為
に符号を記すが、該記入により本発明は添付図面の構造
に限定されるものではない。
Incidentally, although reference numerals are written in the claims section for convenient comparison with the drawings, the present invention is not limited to the structure shown in the accompanying drawings.

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

図面は本発明に係る廃棄物溶融炉の実施例を示し、第1
図は全体の断面図、第2図は要部の別実施例を示す断面
図である。 (3)・・・・・・溶融室、(4)・・・・・・通路、
(6)・・・・・・二次溶融炉、(7)・・・・・・煙
道、(11)・・・・・・取出部、(R)・・・・・・
環状供給路。
The drawings show an embodiment of the waste melting furnace according to the present invention.
The figure is a sectional view of the whole, and FIG. 2 is a sectional view showing another embodiment of the main part. (3)... Melting chamber, (4)... Passage,
(6)... Secondary melting furnace, (7)... Flue, (11)... Taking out part, (R)...
Circular supply channel.

Claims (1)

【特許請求の範囲】[Claims] 被処理物を充填状態で自重下降させる環状供給路(R)
に、その全周にわたって溶融室(3)を連通接続すると
ともに、前記溶融室(3)の底部中央に溶融処理物を高
温排ガスと共に排出する通路(4)を設け、前記排出通
路(4)からの溶融処理物を受止めて貯留する二次溶融
炉(6)を設け、前記二次溶融炉(6)に、そこからの
溶融処理物を自然流下により取出す取出部(11)を設
けると共に、前記排出通路(4)からの高温排ガスを排
出する煙道(7)を接続してある廃棄物溶融炉であって
、前記取出部(11)をオーバーフローによって溶融処
理物を取出すように溶融処理物の貯留レベル近くに配置
し、前記煙道(7)を前記取出部(11)に接続してあ
る廃棄物溶融炉。
Annular supply path (R) that lowers the processed material under its own weight in a filled state
A melting chamber (3) is connected to the melting chamber (3) over its entire circumference, and a passage (4) is provided at the center of the bottom of the melting chamber (3) for discharging the melted material together with high-temperature exhaust gas, and from the discharge passage (4) A secondary melting furnace (6) is provided for receiving and storing the melted material, and the secondary melting furnace (6) is provided with a take-out part (11) for taking out the melted material from there by gravity, A waste melting furnace is connected to a flue (7) for discharging high-temperature exhaust gas from the discharge passageway (4), and the waste melting furnace is configured to take out the melted product by overflowing the take-out section (11). a waste melting furnace located close to the storage level of the waste melting furnace, said flue (7) being connected to said removal point (11).
JP14952687A 1987-06-15 1987-06-15 Waste melting furnace Pending JPS63315819A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP14952687A JPS63315819A (en) 1987-06-15 1987-06-15 Waste melting furnace

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP14952687A JPS63315819A (en) 1987-06-15 1987-06-15 Waste melting furnace

Publications (1)

Publication Number Publication Date
JPS63315819A true JPS63315819A (en) 1988-12-23

Family

ID=15477062

Family Applications (1)

Application Number Title Priority Date Filing Date
JP14952687A Pending JPS63315819A (en) 1987-06-15 1987-06-15 Waste melting furnace

Country Status (1)

Country Link
JP (1) JPS63315819A (en)

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH038739A (en) * 1989-05-18 1991-01-16 Tetronics Res & Dev Co Ltd Treatment of liquid material
JPH0355411A (en) * 1989-07-25 1991-03-11 Ebara Infilco Co Ltd Melting disposing device for incinerated ash
WO1994020791A1 (en) * 1993-03-08 1994-09-15 Kabushiki Kaisha Kobe Seiko Sho Plasma fusion furnace and method of its operation
US5771818A (en) * 1996-05-20 1998-06-30 Prometron Technics Co., Ltd. Cooling system for waste disposal device
US20130309153A1 (en) * 2012-05-17 2013-11-21 Strategic Environmental & Energy Resources, Inc. Waste disposal

Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5063774A (en) * 1973-10-09 1975-05-30
JPS52155880A (en) * 1976-06-21 1977-12-24 Kubota Ltd Incinerator of melting type
JPS55140025A (en) * 1979-04-17 1980-11-01 Hitachi Plant Eng & Constr Co Ltd Fusing furnace of waste material
JPS5916199A (en) * 1982-07-16 1984-01-27 Nec Corp Storage device

Patent Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5063774A (en) * 1973-10-09 1975-05-30
JPS52155880A (en) * 1976-06-21 1977-12-24 Kubota Ltd Incinerator of melting type
JPS55140025A (en) * 1979-04-17 1980-11-01 Hitachi Plant Eng & Constr Co Ltd Fusing furnace of waste material
JPS5916199A (en) * 1982-07-16 1984-01-27 Nec Corp Storage device

Cited By (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH038739A (en) * 1989-05-18 1991-01-16 Tetronics Res & Dev Co Ltd Treatment of liquid material
JPH0355411A (en) * 1989-07-25 1991-03-11 Ebara Infilco Co Ltd Melting disposing device for incinerated ash
WO1994020791A1 (en) * 1993-03-08 1994-09-15 Kabushiki Kaisha Kobe Seiko Sho Plasma fusion furnace and method of its operation
US5771818A (en) * 1996-05-20 1998-06-30 Prometron Technics Co., Ltd. Cooling system for waste disposal device
US20130309153A1 (en) * 2012-05-17 2013-11-21 Strategic Environmental & Energy Resources, Inc. Waste disposal
US8870735B2 (en) * 2012-05-17 2014-10-28 Strategic Environmental & Energy Resources, Inc. Waste disposal
US9393519B2 (en) 2012-05-17 2016-07-19 Strategic Environmental & Energy Resources, Inc. Waste disposal
WO2014134408A1 (en) * 2013-03-01 2014-09-04 Strategic Environmental & Energy Resources, Inc. Waste disposal
GB2523062A (en) * 2013-03-01 2015-08-12 Strategic Environmental & Energy Resources Inc Waste disposal

Similar Documents

Publication Publication Date Title
KR100439547B1 (en) Melting/retaining furnace for aluminum ingot
CA1242585A (en) Ablating liquefaction employing plasma
JPS63315819A (en) Waste melting furnace
JP4685671B2 (en) Waste melting processing equipment
JP3580768B2 (en) Furnace wall structure of electric melting furnace and furnace wall cooling method
WO2007058567A1 (en) Radiative waste reprocessing method and device
JPS63315820A (en) Municipal refuse disposing system
JP3742472B2 (en) Method for preventing clinker formation in combustion furnace of product gas from waste melting furnace
JPH0346723B2 (en)
JP3576468B2 (en) Electric ash melting furnace and method for removing solids from electric ash melting furnace
CN217516034U (en) Spiral discharging device for arsenic trioxide purification system
JPH04293740A (en) Method for operating aluminum melting furnace
JPH11333411A (en) Electric melting furnace for ash treatment and method for operating the same
JPH01159312A (en) Method and apparatus for heating vacuum degassing vessel
JP2002098321A (en) Dust discharging device for secondary combustion chamber
JP2578821Y2 (en) Flash smelting furnace
JPS6349128B2 (en)
JP2001242290A (en) Device and method for incineration melting disposal of radioactive waste
JPH0480513A (en) Method and apparatus for actuation of fluidized bed type incinerator
JPH1151362A (en) Dust removing-melting apparatus for gas containing dust
JPS61235493A (en) Slag discharging apparatus for gasifying oven
JPS62258920A (en) Fluidized bed type incinerator
SU594200A1 (en) Slag subliming arrangement
JPS6033419A (en) Disposal device for incineration slag
CN113154400A (en) Dangerous waste ash melting and vitrifying device and high-temperature melting system comprising same