JPH0480511A - Incinerator - Google Patents
IncineratorInfo
- Publication number
- JPH0480511A JPH0480511A JP19670290A JP19670290A JPH0480511A JP H0480511 A JPH0480511 A JP H0480511A JP 19670290 A JP19670290 A JP 19670290A JP 19670290 A JP19670290 A JP 19670290A JP H0480511 A JPH0480511 A JP H0480511A
- Authority
- JP
- Japan
- Prior art keywords
- incinerator
- layer
- central part
- ash
- combustion
- 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
- 239000002956 ash Substances 0.000 abstract description 15
- 238000002485 combustion reaction Methods 0.000 abstract description 12
- 238000000034 method Methods 0.000 abstract description 5
- 239000004576 sand Substances 0.000 abstract description 2
- 238000007599 discharging Methods 0.000 abstract 4
- 239000000126 substance Substances 0.000 abstract 4
- 235000002918 Fraxinus excelsior Nutrition 0.000 abstract 1
- 239000003245 coal Substances 0.000 abstract 1
- 239000011343 solid material Substances 0.000 abstract 1
- 239000000463 material Substances 0.000 description 6
- 238000003756 stirring Methods 0.000 description 5
- 239000000428 dust Substances 0.000 description 4
- 230000000694 effects Effects 0.000 description 4
- 239000002699 waste material Substances 0.000 description 3
- 239000002440 industrial waste Substances 0.000 description 2
- 239000010813 municipal solid waste Substances 0.000 description 2
- 239000010802 sludge Substances 0.000 description 2
- 239000007787 solid Substances 0.000 description 2
- 238000009423 ventilation Methods 0.000 description 2
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 description 1
- CDBYLPFSWZWCQE-UHFFFAOYSA-L Sodium Carbonate Chemical compound [Na+].[Na+].[O-]C([O-])=O CDBYLPFSWZWCQE-UHFFFAOYSA-L 0.000 description 1
- 239000003546 flue gas Substances 0.000 description 1
- 230000005484 gravity Effects 0.000 description 1
- 239000011148 porous material Substances 0.000 description 1
- 230000000630 rising effect Effects 0.000 description 1
- 239000000779 smoke Substances 0.000 description 1
- 238000005507 spraying Methods 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 1
- 230000002087 whitening effect Effects 0.000 description 1
Landscapes
- Gasification And Melting Of Waste (AREA)
Abstract
Description
【発明の詳細な説明】
[産業上の利用分野コ
本発明は、焼却炉、特に産業廃棄物、雑芥、汚泥、廃油
等の焼却炉に関するものである。DETAILED DESCRIPTION OF THE INVENTION [Field of Industrial Application] The present invention relates to an incinerator, particularly an incinerator for industrial waste, garbage, sludge, waste oil, etc.
[従来の技術]
一般に、産業廃棄物、雑芥、汚泥、廃油等の焼却炉では
、燃焼性を改良し、しかも灰塵等の固形分を含む排煙の
排出を極力抑えることが、肝要とされている。従来、燃
焼性を向上させるには、竪型炉であれ、横型炉であれ、
撹拌手段を設けるのが普通であった。[Prior Art] In general, in incinerators for industrial waste, garbage, sludge, waste oil, etc., it is important to improve the combustibility and to suppress the emission of flue gas containing solids such as ash as much as possible. ing. Traditionally, in order to improve combustibility, whether it is a vertical furnace or a horizontal furnace,
It was common to provide stirring means.
しかしながら、高温の炉内に攪拌手段を設けるのは、撹
拌機の寿命が短く、取り替えに費用、労力を要するばか
りでなく、撹拌により未燃焼の灰塵が舞い上がり、煙突
から排出される欠点があった。撹拌手段に代わるものと
して、例えば傾斜回転式焼却炉といったものも知られて
いる(特開昭49−421 Ei8号公報)。しかし、
この傾斜回転式焼却炉は、攪拌手段に代えて被焼却物を
転勤させるものではあるが、いわゆる横型のロータリー
キルンの一種で、不完全燃焼灰塵の排出抑止能はない。However, installing a stirring means in a high-temperature furnace not only has a short lifespan of the stirrer, requiring cost and labor to replace it, but also has the drawback that unburned ash dust is thrown up by the stirring and discharged from the chimney. . As an alternative to the stirring means, for example, a tilting rotary incinerator is known (Japanese Patent Application Laid-Open No. 49-421 Ei8). but,
Although this tilting rotary incinerator transfers the material to be incinerated in place of a stirring means, it is a type of so-called horizontal rotary kiln and does not have the ability to suppress the emission of incompletely burned ash.
このため、煙突との間に二次燃焼室を設けたり、散水手
段等を要し、装置の大型化は避けられなかった。For this reason, it was necessary to provide a secondary combustion chamber between the chimney and the chimney, and to provide water spraying means, making it inevitable to increase the size of the device.
一方、燃焼性をあげるたぬ、二次、三次燃焼室を設けた
り、自然給気あるいは強制送風することもよく知られて
いる。たとえば、空気の給気方式として、煙道を二重管
にして多数の給気孔から排煙に加熱外気を供給し、自己
燃焼させることも知られている(特開昭54−4424
0号公報)。On the other hand, it is also well known to provide secondary or tertiary combustion chambers, or to use natural air supply or forced ventilation, in order to improve combustibility. For example, it is known that as an air supply method, the flue is made into a double pipe, and heated outside air is supplied to the exhaust smoke through a large number of air supply holes to cause self-combustion (Japanese Patent Laid-Open No. 54-4424
Publication No. 0).
らしかし、との給気方式では二次燃焼効果はあっても、
煙道の一端が焼却炉の側壁に開口しているたき込む方式
も知られているが(特開昭56−94113号)、被焼
却物に対し垂直方向に旋回しているため、これも灰塵が
かえって舞い上がることは避けられない。いずれにしろ
、従来の給気方式は、燃焼効果のみに留意して、灰塵抑
止には逆効果になっているのが実状であった。したがっ
て炉と煙突の間になんらかの灰塵除去手段を、要し、炉
上部に煙突を直接とりつける簡便な焼却炉の設計は困難
であった。However, although there is a secondary combustion effect with the air supply method,
There is also a known method in which one end of the flue opens into the side wall of the incinerator (Japanese Unexamined Patent Publication No. 56-94113), but since the flue rotates perpendicularly to the material to be incinerated, this method also generates ash dust. It is inevitable that things will rise again. In any case, the conventional air supply system focuses only on the combustion effect, and the reality is that it has the opposite effect on suppressing ash dust. Therefore, some kind of ash removal means is required between the furnace and the chimney, and it has been difficult to design a simple incinerator in which the chimney is directly attached to the upper part of the furnace.
[発明が解決しようとする課題]
本発明は、前記のごとき問題点を解消した燃焼効率がよ
く、未燃焼固形物の随伴排出のおそれのない簡便な構造
の傾斜回転竪型焼却炉を提供することを目的としている
。[Problems to be Solved by the Invention] The present invention provides a tilting rotary vertical incinerator that eliminates the above-mentioned problems, has good combustion efficiency, and has a simple structure without the risk of accompanying discharge of unburned solids. The purpose is to
[課題を解決するための手段]
前記目的を達成した本発明に係わる焼却炉の実第1図に
おいて、耐火性の竪型椀状炉体1は、垂直軸に対し約1
0度傾斜して基台10に回転自在に支承されている。1
1はその可変減速駆動装置である。本発明では、この炉
体1の略中央に灰排出口4を突設して開口し、排出管1
2に連設しである。排出管の出口には開閉手段13を設
け、必要時に待機中の移動車14に排出し得るようにし
である。17は炉体1の排気化水套である。[Means for Solving the Problems] In Fig. 1 of the incinerator according to the present invention which achieves the above object, the refractory vertical bowl-shaped furnace body 1 has an angle of about 1 with respect to the vertical axis.
It is rotatably supported on the base 10 with an inclination of 0 degrees. 1
1 is its variable speed reduction drive device. In the present invention, an ash discharge port 4 is opened and protrudes from approximately the center of the furnace body 1, and a discharge pipe 1
It is connected to 2. An opening/closing means 13 is provided at the outlet of the discharge pipe so that the discharge can be discharged to a waiting moving vehicle 14 when necessary. Reference numeral 17 denotes an exhaust canopy for the furnace body 1.
方、蓋2は、炉体1の上を覆うように、枠15に固定さ
れている。蓋2の略中央には、煙突3の煙道下端が直接
開口している。本発明では、煙突3の煙道下部から蓋2
の上面に亘って外套5を設けて、給気路6を形成しであ
る。給気路6は一方で強制送風機7に連接されており、
他方は蓋2に開設された給気口8と小気孔9にそれぞれ
連通している。6Aは自然通気孔である。本発明の給気
白変開設されている。小気孔9は炉心近傍に寄せ集めら
れた火焔とともに、灰塵が舞い上がるのを抑また、蓋2
の外縁には、排気止め板16を設けである。18はバー
ナー 19は温度計であり、20は被焼却物投入ホッパ
ーである。On the other hand, the lid 2 is fixed to the frame 15 so as to cover the top of the furnace body 1. The lower end of the flue of the chimney 3 directly opens approximately at the center of the lid 2. In the present invention, from the lower part of the flue of the chimney 3 to the lid 2.
A mantle 5 is provided over the upper surface of the air supply passage 6 to form an air supply passage 6. The air supply path 6 is connected to a forced air blower 7 on the one hand;
The other side communicates with an air supply port 8 and a small air hole 9 provided in the lid 2, respectively. 6A is a natural ventilation hole. The present invention has been established for air supply whitening. The small pores 9 suppress the flames gathered near the core and ash dust from flying up, and the lid 2
An exhaust stop plate 16 is provided on the outer edge of the exhaust valve. 18 is a burner, 19 is a thermometer, and 20 is a hopper for charging materials to be incinerated.
[作用コ
前記のごとく構成された本発明の廃棄物等の焼却炉では
、先ず炉体1を竪型傾斜回転炉にすることによって、回
転にもとづく平行方向の遠心力と傾斜にもとづく移動で
、撹拌機を設けなくても被焼却物は転動し、たえず新鮮
な燃焼層が上面に露出して、良好な燃焼がえられる。の
みならず、被焼却物の比重差により、外周部に比較的重
い被焼却物で焔となる層、中間部に戻火となる層、中心
部に灰の層、炉底部に流動砂層が形成され、順次移行す
る。本発明ではこの炉床1真の中心近傍に灰排出口を突
設開口しであるので、軽い灰は自然に中央に集まり、こ
の排出口4から排出される。[Function] In the waste incinerator of the present invention constructed as described above, first, the furnace body 1 is made into a vertical tilted rotary furnace. Even without a stirrer, the material to be incinerated is rolled, and a fresh combustion layer is constantly exposed on the top surface, resulting in good combustion. In addition, due to the difference in specific gravity of the materials to be incinerated, a layer of relatively heavy materials to be incinerated that becomes flames is formed at the outer periphery, a layer that causes return fire in the middle, a layer of ash in the center, and a layer of fluidized sand at the bottom of the furnace. and will be migrated sequentially. In the present invention, since the ash discharge port is provided in the vicinity of the true center of the hearth 1, light ash naturally gathers in the center and is discharged from the discharge port 4.
また、蓋2の給気口8から炉体1の回転方向に孟イ丁
卑旋回状に給気することにより、転勤により生じった焔
が舞い上がるのを、炉心に向けた小気孔9からの空気が
抑え込む。In addition, by supplying air from the air supply port 8 of the lid 2 in a spiral manner in the rotational direction of the reactor body 1, flames generated by transfer can be prevented from rising from the small air holes 9 toward the reactor core. The air is oppressive.
[発明の効果コ
以上要するに本発明の焼却炉によれば、以下の実用上の
利点が得られる。[Effects of the Invention] In summary, the incinerator of the present invention provides the following practical advantages.
■0、撹拌機のごとき複雑な手段なしに、良好な燃焼が
得られる。■0.Good combustion can be obtained without complicated means such as a stirrer.
■、灰分が自然に分離されて炉床から排出されて、煙突
に逃げるおそれがない。■ Ash is naturally separated and discharged from the hearth, and there is no risk of it escaping into the chimney.
■、上記の結果、煙突を直結でき、焼却炉全体の構造も
簡単となる。(2) As a result of the above, the chimney can be directly connected, and the overall structure of the incinerator becomes simple.
第1図は、本発明の焼却炉の一例を示す断面図である。 FIG. 1 is a sectional view showing an example of the incinerator of the present invention.
Claims (3)
口(4)を備え、かつ全体が傾斜して回転自在に設けら
れた椀状竪型炉体(1)。(1) A bowl-shaped vertical furnace body (1) that is provided with an ash discharge port (4) projecting from the center of the hearth (1), and that is tilted as a whole and is rotatable.
たる外套(5)により形成された給気路(6)を介して
、送風機(7)に連接され、炉体(1)の回転方向に対
し平行旋回状に開口された給気口(8)と、略炉心に向
けて開穿された多数の小気孔(9)とを備えた炉の蓋(
2)。(2) is connected to the blower (7) through the air supply path (6) formed by the mantle (5) extending from at least the lower part of the flue to the upper surface of the chimney (3), and is connected to the furnace body (1). A reactor lid (8) equipped with an air supply port (8) opened in a spiral shape parallel to the rotation direction and a large number of small air holes (9) opened approximately toward the reactor core.
2).
、請求項(2)記載の固定上蓋(2)を付設してなる焼
却炉。(3) An incinerator comprising a vertical tilting rotary furnace body (1) according to claim (1) and a fixed upper lid (2) according to claim (2).
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP2196702A JPH0743107B2 (en) | 1990-07-24 | 1990-07-24 | Incinerator |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP2196702A JPH0743107B2 (en) | 1990-07-24 | 1990-07-24 | Incinerator |
Publications (2)
Publication Number | Publication Date |
---|---|
JPH0480511A true JPH0480511A (en) | 1992-03-13 |
JPH0743107B2 JPH0743107B2 (en) | 1995-05-15 |
Family
ID=16362168
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP2196702A Expired - Fee Related JPH0743107B2 (en) | 1990-07-24 | 1990-07-24 | Incinerator |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH0743107B2 (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO1998033014A1 (en) * | 1997-01-23 | 1998-07-30 | Oil-Recycle Co., Ltd. | Incinerator |
Citations (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS4963777U (en) * | 1972-08-29 | 1974-06-04 | ||
JPS4977465A (en) * | 1972-11-30 | 1974-07-25 | ||
JPS56158731U (en) * | 1980-04-22 | 1981-11-26 |
-
1990
- 1990-07-24 JP JP2196702A patent/JPH0743107B2/en not_active Expired - Fee Related
Patent Citations (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS4963777U (en) * | 1972-08-29 | 1974-06-04 | ||
JPS4977465A (en) * | 1972-11-30 | 1974-07-25 | ||
JPS56158731U (en) * | 1980-04-22 | 1981-11-26 |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO1998033014A1 (en) * | 1997-01-23 | 1998-07-30 | Oil-Recycle Co., Ltd. | Incinerator |
Also Published As
Publication number | Publication date |
---|---|
JPH0743107B2 (en) | 1995-05-15 |
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