JPS621549Y2 - - Google Patents
Info
- Publication number
- JPS621549Y2 JPS621549Y2 JP1981111372U JP11137281U JPS621549Y2 JP S621549 Y2 JPS621549 Y2 JP S621549Y2 JP 1981111372 U JP1981111372 U JP 1981111372U JP 11137281 U JP11137281 U JP 11137281U JP S621549 Y2 JPS621549 Y2 JP S621549Y2
- Authority
- JP
- Japan
- Prior art keywords
- temperature
- combustion
- industrial waste
- exhaust gas
- nozzle
- 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
Links
- 238000002485 combustion reaction Methods 0.000 claims description 30
- 239000007789 gas Substances 0.000 claims description 22
- 238000002844 melting Methods 0.000 claims description 16
- 230000008018 melting Effects 0.000 claims description 16
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 13
- 239000002440 industrial waste Substances 0.000 claims description 12
- 230000001174 ascending effect Effects 0.000 claims description 11
- 239000000463 material Substances 0.000 claims description 7
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 claims description 5
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 claims description 5
- 239000003546 flue gas Substances 0.000 claims description 5
- 239000012768 molten material Substances 0.000 claims description 5
- 229910052760 oxygen Inorganic materials 0.000 claims description 5
- 239000001301 oxygen Substances 0.000 claims description 5
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims description 4
- 229910052799 carbon Inorganic materials 0.000 claims description 3
- 239000000428 dust Substances 0.000 description 6
- 239000000571 coke Substances 0.000 description 5
- 239000002893 slag Substances 0.000 description 4
- 239000010802 sludge Substances 0.000 description 4
- 238000001514 detection method Methods 0.000 description 3
- 239000010801 sewage sludge Substances 0.000 description 3
- 238000001816 cooling Methods 0.000 description 2
- 239000000498 cooling water Substances 0.000 description 2
- 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
- 239000003245 coal Substances 0.000 description 1
- 238000010276 construction Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 229910002804 graphite Inorganic materials 0.000 description 1
- 239000010439 graphite Substances 0.000 description 1
- 229910001385 heavy metal Inorganic materials 0.000 description 1
- 239000013462 industrial intermediate Substances 0.000 description 1
- 239000013067 intermediate product Substances 0.000 description 1
- 239000000843 powder Substances 0.000 description 1
- 239000000047 product Substances 0.000 description 1
- 230000000630 rising effect Effects 0.000 description 1
- 239000007921 spray Substances 0.000 description 1
- 239000008400 supply water Substances 0.000 description 1
- 239000002699 waste material Substances 0.000 description 1
Landscapes
- Air Supply (AREA)
Description
【考案の詳細な説明】
本考案は、下水汚泥などの各種の産業廃棄物や、
あるいはそれらを必要に応じて予め乾燥焼却や粉
砕処理した中間処理物を、埋立てに使用した時に
重金属が流出しないようにしたり、あるいは建設
骨材に利用できるようにする等のために焼却、溶
融する炉に関し、詳しくは、産業廃棄物あるいは
その中間処理物を炭素系可燃物質で形成した高温
炉床の上部において焼却溶融させ、その溶融物を
前記高温炉床の下部側から取出すべく構成すると
共に、前記高温炉床の上方に燃焼排ガス用上昇流
路を設けた産業廃棄物溶融炉に関する。[Detailed explanation of the invention] This invention is designed to treat various industrial wastes such as sewage sludge,
Alternatively, if necessary, the intermediately processed materials have been dried and incinerated or pulverized before being incinerated or melted in order to prevent heavy metals from flowing out when used in landfills, or to be used as construction aggregate. More specifically, the furnace is configured to incinerate and melt industrial waste or intermediately treated products thereof in the upper part of a high-temperature hearth made of carbon-based combustible material, and take out the molten material from the lower side of the high-temperature hearth. , relates to an industrial waste melting furnace having an ascending passage for flue gas above the high temperature hearth.
上記溶融炉において、燃焼排ガスの温度が産業
廃棄物あるいは中間処理物から離脱した燃焼灰分
や微粉等の飛散ダストにおける軟化溶融点以上に
なると、飛散ダストが上昇流路における炉壁に融
着する不都合をもたらすものとなり、燃焼排ガス
の温度を前記軟化溶融点内に維持させる必要があ
るが、燃焼排ガスの温度調節を高温炉床における
燃焼状態の調節で行なおうとすると、処理能率の
低下をきたすものとなる。 In the above-mentioned melting furnace, if the temperature of the combustion exhaust gas exceeds the softening melting point of the scattered dust such as combustion ash and fine powder released from industrial waste or intermediate processed materials, the scattered dust will fuse to the furnace wall in the upward flow path, which is a disadvantage. Therefore, it is necessary to maintain the temperature of the flue gas within the softening and melting point, but if the temperature of the flue gas is adjusted by adjusting the combustion state in a high-temperature hearth, the processing efficiency will decrease. becomes.
本考案は、上記実状に鑑みて為されたものであ
つて、燃焼排ガスを効果的に冷却し、処理能率の
向上を図る点にある。 The present invention has been developed in view of the above-mentioned circumstances, and its purpose is to effectively cool combustion exhaust gas and improve processing efficiency.
従つて本考案によれば、前記上昇流路内に水又
は水蒸気の供給口を、燃焼排ガス後燃焼用酸素含
有ガスを供給するための羽口よりも上方に配置し
てあると共に、前記供給口を通る管の先端に取付
けられたノズルの開度が該ノズルよりも上方の燃
焼排ガスの温度に基いて制御される構成であるこ
とを特徴とする産業廃棄物溶融炉が提供される。 Therefore, according to the present invention, the water or steam supply port is disposed in the upward passage above the tuyere for supplying the oxygen-containing gas for post-combustion of the combustion exhaust gas, and the supply port An industrial waste melting furnace is provided, characterized in that the opening degree of a nozzle attached to the tip of a pipe passing through the nozzle is controlled based on the temperature of the combustion exhaust gas above the nozzle.
以下、本考案の実施の態様を例示図に基いて詳
述する。 Hereinafter, embodiments of the present invention will be described in detail based on illustrative drawings.
産業廃棄物例えば下水汚泥を焼却溶融するため
の溶融炉を構成するに、第1図に示すように、炭
素系可燃物質例えばコークスによつて高温炉床1
を形成するための燃焼部2と、反射式などの溶融
物取出し炉体3を、前記燃焼部2の底部近くで連
通させて架台4に設け、かつ、前記燃焼部2の底
部分2aを開閉自在に構成してコークスの燃焼滓
を取り出せるようにすると共に、燃焼排ガス用上
昇流路5を、前記高温炉床1の上方に連設し、そ
して、前記高温炉床1を形成するためのコークス
供給用並びにその高温炉床1の上面への汚泥供給
用の兼用流下路6を、その端部供給口6aを高温
炉床1の上方近くに位置させる状態で、排ガス用
上昇流路5に下降傾斜させて接続し、もつて、汚
泥及びコークスの充填層Aを高温炉床1の上部に
形成させるようにし、そして、前記燃焼部2への
供給コークスに対する着火用の燃焼装置7と、排
ガス廃熱利用の熱交換器(図外)からの燃焼用酸
素含有ガスの供給用第1羽口8を、夫々燃焼部2
に設け、もつて、汚泥を高温炉床1の上部におい
て焼却、溶融させるようにするとともに、その溶
融物を高温炉床1の下部がわから炉体3に取出
し、炉体3に取り出した溶融物を第1及び第2出
滓口9,10から適宜回収させるようにし、そし
て、前記熱交換器からの燃焼排ガス後燃焼用酸素
含有ガスを上昇流路5内に供給するための第2羽
口11を、前記供給口6aよりも上方に設け、も
つて、前記高温炉床1からの燃焼排ガスを後燃焼
させるようにし、つまり、燃焼排ガスが充填層A
を通過する際に生成される臭気成分及び有害成分
の燃焼分解を行なわせるようにし、そして、ダス
ト除去用サイクロン12を、前記上昇流路5に排
気ダクト13を介して連通接続させ、且つ、前記
熱交換器に連通接続させる状態で設け、もつて、
排ガスをそれに含むダストを除去させたのち熱交
換器に供給するようにし、そして、前記上昇流路
5内に水を供給する口14を、前記第2羽口11
よりも上方に位置させる状態で設け、前記供給口
14を挿通させる状態で水噴出ノズル15を設
け、もつて、前記後燃焼後の燃焼排ガスを、その
温度が飛散ダストの軟化溶融点以下となるように
冷却させるようにしてある。 In constructing a melting furnace for incinerating and melting industrial waste, such as sewage sludge, as shown in FIG.
A combustion section 2 for forming a combustion chamber 2 and a molten material take-out furnace body 3 such as a reflective type are installed on a frame 4 in communication with each other near the bottom of the combustion section 2, and the bottom section 2a of the combustion section 2 is opened and closed. The structure can be freely configured so that the combustion slag of coke can be taken out, and the ascending passage 5 for combustion exhaust gas is connected above the high-temperature hearth 1, and the coke slag for forming the high-temperature hearth 1 is provided. The dual-purpose flow path 6 for supplying sludge to the upper surface of the high-temperature hearth 1 is lowered into the exhaust gas ascending flow path 5 with its end supply port 6a located near the top of the high-temperature hearth 1. The sludge and coke packed bed A is formed in the upper part of the high-temperature hearth 1 by connecting the sludge and coke at an angle. The first tuyere 8 for supplying oxygen-containing gas for combustion from a heat exchanger (not shown) for heat utilization is connected to the combustion section 2, respectively.
The sludge is incinerated and melted in the upper part of the high-temperature hearth 1, and the molten material is taken out into the furnace body 3 through the lower part of the high-temperature hearth 1, and the molten material taken out into the furnace body 3 is a second tuyere for appropriately collecting the slag from the first and second slag outlets 9 and 10, and supplying the oxygen-containing gas for combustion after the combustion exhaust gas from the heat exchanger into the ascending passage 5; 11 is provided above the supply port 6a, so that the combustion exhaust gas from the high-temperature hearth 1 is post-combusted, that is, the combustion exhaust gas flows into the packed bed A.
The cyclone 12 for dust removal is connected to the ascending flow path 5 via the exhaust duct 13, and the Provided in a state where it is connected to the heat exchanger,
The exhaust gas is supplied to the heat exchanger after removing the dust contained therein, and the port 14 for supplying water into the ascending flow path 5 is connected to the second tuyere 11.
A water jet nozzle 15 is provided in such a manner that the water jet nozzle 15 is located above the water supply port 14, and the water jet nozzle 15 is provided in a state in which the supply port 14 is inserted, so that the temperature of the combustion exhaust gas after the post-combustion becomes equal to or lower than the softening melting point of the scattered dust. It is designed to cool down like this.
前記ノズル15を構成するに、第2図に示すよ
うに、炉壁に取付けられるケーシング16に、供
給用水案内管17、スプレーノズルチツプ18、
冷却用水案内管19、及び、冷却用水排出管20
を組付け、もつて、熱損を防止するようにしてあ
る。 As shown in FIG. 2, the nozzle 15 includes a casing 16 attached to the furnace wall, a supply water guide pipe 17, a spray nozzle tip 18,
Cooling water guide pipe 19 and cooling water discharge pipe 20
are assembled and attached to prevent heat loss.
又、第1図に示すように、前記ノズル15への
水供給量を変更調節する流量制御弁21を設け、
前記上昇流路5における燃焼排ガスの温度を検出
する装置22を設け、さらに、温度検出装置22
からの情報に基づいて前記制御弁21を自動操作
する制御機構23を設け、もつて、飛散ダストを
炉壁に融着させないように、温度検出装置22に
よる排ガス検出値を設定範囲内に維持させるよう
にしてある。 Further, as shown in FIG. 1, a flow control valve 21 is provided to change and adjust the amount of water supplied to the nozzle 15,
A device 22 for detecting the temperature of the combustion exhaust gas in the ascending flow path 5 is provided, further comprising a temperature detection device 22.
A control mechanism 23 is provided that automatically operates the control valve 21 based on information from the temperature detector 22, and maintains the exhaust gas detection value by the temperature detection device 22 within a set range so as not to fuse the scattered dust to the furnace wall. It's like this.
尚、上記の溶融炉は、下水汚泥の外に、例えば
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を処理対象にで
きる。 In addition to sewage sludge, the above-mentioned melting furnace can treat various industrial wastes such as tire scraps, city garbage incineration ash, and waste catalysts, or intermediate products thereof.
又、本案を実施するに、水の代わりに水蒸気を
用いる場合、第3図に示すように、炉壁内面に沿
つて水蒸気を流動させるべく、口14を傾斜状に
形成するとよい。 Further, when carrying out the present invention and using steam instead of water, the opening 14 may be formed in an inclined shape to allow the steam to flow along the inner surface of the furnace wall, as shown in FIG.
又、本案を実施するに、水又は水蒸気の供給量
を手動で調節させる形態で実施してもよい。 Furthermore, the present invention may be implemented in a manner in which the amount of water or steam supplied is manually adjusted.
又、本案は、燃焼排ガス後燃焼用酸素含有ガス
を供給するための羽口11を備えていない構成の
溶融炉にも適用できるものである。 Further, the present invention can also be applied to a melting furnace having a configuration that does not include the tuyere 11 for supplying oxygen-containing gas for combustion after combustion exhaust gas.
また、利用する溶融炉の具体的構成は、各種変
形可能である。第4図は、その一例を示し、高温
炉床2部分に対する側壁を、2重管構造に形成し
て水冷ジヤケツト24を構成したものである。 Furthermore, the specific configuration of the melting furnace used can be modified in various ways. FIG. 4 shows an example of this, in which the side wall for the two portions of the high-temperature hearth is formed into a double pipe structure to constitute a water-cooled jacket 24.
また、高温炉床2を形成する炭素系可燃物質と
しては、主としてコークスを用いるとよいが、無
煙炭等の練炭、黒鉛電極屑等の各種のものを利用
してもよい。 Further, as the carbon-based combustible material forming the high-temperature hearth 2, it is preferable to mainly use coke, but various materials such as briquettes such as anthracite coal, graphite electrode scraps, etc. may also be used.
以上要するに本考案は、冒記産業廃棄物溶融炉
において、前記上昇流路5内に水又は水蒸気を供
給する口14を設けてあることを特徴とする。 In summary, the present invention is characterized in that the above-mentioned industrial waste melting furnace is provided with an opening 14 for supplying water or steam into the upward passage 5.
すなわち、上昇流路5内に水又は水蒸気を供給
することによつて、燃焼排ガスを効果的に冷却で
きるようにしてあるから、高温炉床1における燃
焼状態を調節する冒記手段の不都合を回避し、処
理能率の向上を図れるものである。 That is, by supplying water or steam into the ascending passage 5, the combustion exhaust gas can be effectively cooled, thereby avoiding the disadvantages of the above-mentioned means for adjusting the combustion state in the high-temperature hearth 1. However, it is possible to improve processing efficiency.
さらに詳述すると、本案と同様の目的に達する
別手段として、上昇流路5内に冷却用空気を供給
することによつて、燃焼排ガスを冷却する手段が
考えられるが、この場合、本案手段に較べて充分
な冷却作用を発揮させ難いものであり、高温炉床
1における燃焼状態を調節する手段を併用しなけ
ればならない等の不利があるが、本案によればこ
のような不利なく所望の目的に達し得るものであ
る。 To explain in more detail, another means to achieve the same purpose as the present invention is to cool the combustion exhaust gas by supplying cooling air into the ascending passage 5, but in this case, the present means is In comparison, it is difficult to exert a sufficient cooling effect, and there are disadvantages such as the need to use means for adjusting the combustion state in the high-temperature hearth 1. However, according to the present invention, the desired purpose can be achieved without such disadvantages. can be reached.
図面は本考案に係る産業廃棄物溶融炉の実施の
態様を例示し、第1図は概略断面図、第2図はノ
ズルの縦断側面図、第3図は別の実施例の縦断側
面図、第4図は別構成の溶融炉の概略断面図であ
る。
1……高温炉床、5……上昇流路、11……羽
口、14……水又は水蒸気の供給口、15……ノ
ズル。
The drawings illustrate embodiments of the industrial waste melting furnace according to the present invention, in which FIG. 1 is a schematic sectional view, FIG. 2 is a longitudinal sectional side view of a nozzle, and FIG. 3 is a longitudinal sectional side view of another embodiment. FIG. 4 is a schematic sectional view of a melting furnace having a different configuration. DESCRIPTION OF SYMBOLS 1... High-temperature hearth, 5... Rising channel, 11... Tuyere, 14... Water or steam supply port, 15... Nozzle.
Claims (1)
燃物質で形成した高温炉床1の上部において焼却
溶融させ、その溶融物を前記高温炉床1の下部側
から取出すべく構成すると共に、前記高温炉床1
の上方に燃焼排ガス用上昇流路5を設けた産業廃
棄物溶融炉であつて、前記上昇流路5内に水又は
水蒸気の供給口14を、燃焼排ガス後燃焼用酸素
含有ガスを供給するための羽口11よりも上方に
配置してあると共に、前記供給口14を通る管の
先端に取付けられたノズル15の開度が該ノズル
よりも上方の燃焼排ガスの温度に基いて制御され
る構成であることを特徴とする産業廃棄物溶融
炉。 Industrial waste or its intermediate processed material is incinerated and melted in the upper part of a high-temperature hearth 1 made of carbon-based combustible material, and the molten material is taken out from the lower side of the high-temperature hearth 1, and the high-temperature hearth 1
This is an industrial waste melting furnace provided with an ascending passage 5 for flue gas in the upper part, and a water or steam supply port 14 is provided in the ascending passage 5 for supplying oxygen-containing gas for combustion after the flue gas. A configuration in which the opening degree of a nozzle 15, which is disposed above the tuyere 11 and attached to the tip of the pipe passing through the supply port 14, is controlled based on the temperature of the combustion exhaust gas above the nozzle. An industrial waste melting furnace characterized by:
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP11137281U JPS5821729U (en) | 1981-07-27 | 1981-07-27 | industrial waste melting furnace |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP11137281U JPS5821729U (en) | 1981-07-27 | 1981-07-27 | industrial waste melting furnace |
Publications (2)
Publication Number | Publication Date |
---|---|
JPS5821729U JPS5821729U (en) | 1983-02-10 |
JPS621549Y2 true JPS621549Y2 (en) | 1987-01-14 |
Family
ID=29905713
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP11137281U Granted JPS5821729U (en) | 1981-07-27 | 1981-07-27 | industrial waste melting furnace |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS5821729U (en) |
Families Citing this family (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP3905635B2 (en) * | 1998-04-24 | 2007-04-18 | 三菱重工業株式会社 | Ash melting furnace |
AU2003264364A1 (en) * | 2002-09-04 | 2004-03-29 | Sumitomo Metal Industries, Ltd. | Method and apparatus for treating waste |
Family Cites Families (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS577938Y2 (en) * | 1977-02-08 | 1982-02-16 |
-
1981
- 1981-07-27 JP JP11137281U patent/JPS5821729U/en active Granted
Also Published As
Publication number | Publication date |
---|---|
JPS5821729U (en) | 1983-02-10 |
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