JPS61195208A - Incinerator - Google Patents

Incinerator

Info

Publication number
JPS61195208A
JPS61195208A JP60034497A JP3449785A JPS61195208A JP S61195208 A JPS61195208 A JP S61195208A JP 60034497 A JP60034497 A JP 60034497A JP 3449785 A JP3449785 A JP 3449785A JP S61195208 A JPS61195208 A JP S61195208A
Authority
JP
Japan
Prior art keywords
incinerator
exhaust gas
gas cooling
incineration
hollow shield
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
JP60034497A
Other languages
Japanese (ja)
Other versions
JPH0160729B2 (en
Inventor
Tsutomu Higo
勉 肥後
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.)
Ebara Corp
Original Assignee
Ebara 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 Ebara Corp filed Critical Ebara Corp
Priority to JP60034497A priority Critical patent/JPS61195208A/en
Publication of JPS61195208A publication Critical patent/JPS61195208A/en
Publication of JPH0160729B2 publication Critical patent/JPH0160729B2/ja
Granted legal-status Critical Current

Links

Abstract

PURPOSE:To prevent transmitting heat of an incinerator inside in the form of radiation to a cooling part for incinerated exhaust gas by installing a hollow shield between an incinerator and the cooling part for exhaust gas installed at the upper part of the incinerator. CONSTITUTION:A cooling part 2 for incinerated exhaust gas is installed at the upper part of an incinerator 1 as one body with the incinerator and a hollow shield of which outside surface is covered with fire-resistant material is installed in a exhaust gas path between the incinerator 1 and the cooling part 2 for incinerated exhaust gas. By this structure, it is not necessary to over cool the inside of the incinerator 1 beyond necessity and also it is possible to use a simple incinerator composed of the incinerator 1 and exhaust gas cooling part 2 as one body for any waste to be incinerated.

Description

【発明の詳細な説明】 〔産業上の利用分野〕 本発明は、焼却排ガス冷却部を焼却炉と一体に備えた焼
却装置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 that includes an incineration exhaust gas cooling section and an incinerator integrally.

〔従来の技術〕[Conventional technology]

従来、廃熱ボイラ、空気冷却器および水噴霧ガス冷却室
などの焼却炉から排出する排ガスを冷却する焼却排ガス
冷却部を備えた焼却炉において、上記の焼却排ガス冷却
部は焼却炉から独立した機器として焼却炉から離して設
置され、耐火物を内その具体的構造は、例えば第7図な
いし第9図に示すようなものである。
Conventionally, in an incinerator equipped with an incineration exhaust gas cooling section that cools the exhaust gas discharged from the incinerator, such as a waste heat boiler, an air cooler, and a water spray gas cooling room, the above incineration exhaust gas cooling section is a device independent from the incinerator. The concrete structure of the refractory is as shown in FIGS. 7 to 9, for example.

第7図に示すものでは、焼却炉20、ガス冷却室22、
空気予熱器23、電気集塵器24、誘引送風機25およ
び煙突26が順次にダクトによって連結され”ζいる。
In the one shown in FIG. 7, an incinerator 20, a gas cooling chamber 22,
An air preheater 23, an electric precipitator 24, an induced blower 25, and a chimney 26 are sequentially connected by a duct.

そして、焼却炉20には、焼却物、助燃物および燃焼用
空気が供給され、不燃物が排出される。ガス冷却室22
においては、燃焼排ガス中に噴射水加圧ポンプ27を通
った冷却水が噴射され、ガスを冷却する。空気予熱器2
3は押込送風機28から送られた燃焼用空気を予熱して
焼却炉20に送り、その一方排ガスを冷却する。ガス冷
却室22および電気集塵器24からは燃焼排ガス中から
分離された灰が除去される。
The incinerator 20 is supplied with incineration materials, auxiliary combustion materials, and combustion air, and incombustible materials are discharged. Gas cooling chamber 22
In the combustion exhaust gas, cooling water that has passed through the injection water pressure pump 27 is injected into the combustion exhaust gas to cool the gas. Air preheater 2
3 preheats the combustion air sent from the forced air blower 28 and sends it to the incinerator 20, while cooling the exhaust gas. Ash separated from the combustion exhaust gas is removed from the gas cooling chamber 22 and the electrostatic precipitator 24.

つぎに、第8図に示すものでは、焼却炉20゜廃熱ボイ
ラ29、電気集塵器24、誘引送風機25および煙突2
6が順次にダクトによって連結されている。そして、焼
却炉20には、焼却物、助燃物および押込送風機28か
ら蒸気式空気予熱不燃物が排出される。廃熱ボイラ29
には缶水が供給され、蒸気を発生する。廃熱ボイラ29
および電気集塵器24からは、排ガス中の灰が除去され
る。
Next, in the one shown in FIG.
6 are sequentially connected by ducts. The incinerator 20 is then discharged with incinerated materials, auxiliary combustion materials, and non-combustible materials preheated by steam air from the forced air blower 28 . Waste heat boiler 29
canned water is supplied to generate steam. Waste heat boiler 29
Ash in the exhaust gas is removed from the electrostatic precipitator 24.

さらに、第9図に示すものでは、焼却炉2o、空気予熱
器23、白煙対策用熱交換器31、サイクロン32、誘
引送風機25、スクラバ33、および煙突26が順次に
ダクトによって連結されている。そして、焼却炉20に
は、焼却物、助燃物および押込送風機28から空気予熱
器23を通して燃焼用空気が供給され、不燃物が排出さ
れる。
Furthermore, in the one shown in FIG. 9, an incinerator 2o, an air preheater 23, a white smoke countermeasure heat exchanger 31, a cyclone 32, an induced fan 25, a scrubber 33, and a chimney 26 are sequentially connected by a duct. . Then, combustion air is supplied to the incinerator 20 through the air preheater 23 from the incineration materials, auxiliary combustion materials, and a forced air blower 28, and noncombustible materials are discharged.

白煙対策用ファン34は、白煙対策用空気を白煙対策用
熱交換器31において予熱した後、スクラバ33と煙突
26の間においてダクトに供給する。
The white smoke countermeasure fan 34 preheats the white smoke countermeasure air in the white smoke countermeasure heat exchanger 31 and then supplies it to the duct between the scrubber 33 and the chimney 26 .

空気予熱器23およびサイクロン32において分離され
た灰は、除去される。スクラバ33には、洗煙水が噴射
される。
The ash separated in the air preheater 23 and cyclone 32 is removed. Smoke washing water is injected into the scrubber 33.

上記のように、廃熱ボイラ29、空気予熱器23および
水噴霧ガス冷却室22などの、焼却炉2゜から排出する
排ガスを冷却する焼却排ガス冷却部はいずれも焼却炉2
0とは別に設置されていたので、膨大な設置面積が必要
となり、その上、焼却炉20、接続ダクト、焼却排ガス
冷却部22に対する支持架構、点検用歩廊等を設置しな
ければならず、また、接続ダクト、焼却炉出口、焼却排
ガス冷却部入口等の煙道における排ガス流の乱れに伴う
圧力損失や、ダストの堆積、付着などが避けられない等
の問題があった。
As mentioned above, the incineration exhaust gas cooling units such as the waste heat boiler 29, the air preheater 23, and the water spray gas cooling chamber 22 that cool the exhaust gas discharged from the incinerator 2° are all connected to the incinerator 2.
Since it was installed separately from the incinerator 20, a huge installation area was required, and in addition, it was necessary to install the incinerator 20, the connecting duct, a support frame for the incineration exhaust gas cooling section 22, a walkway for inspection, etc. There have been problems such as pressure loss due to turbulence in the flow of exhaust gas in the flue such as the connecting duct, the incinerator outlet, and the inlet of the incineration exhaust gas cooling section, and the unavoidable accumulation and adhesion of dust.

そこで、最近では、第10図に示すように、排ガス冷却
部21を焼却炉20の上に載置し、焼却炉20のフリー
ボード部の天井がそのまま焼却排ガス冷却部21人口と
なるように一体化した焼却装置が実用化されつつある。
Therefore, recently, as shown in FIG. 10, the exhaust gas cooling unit 21 is placed on top of the incinerator 20, and the ceiling of the freeboard part of the incinerator 20 is integrated with the incineration exhaust gas cooling unit 21. Advanced incinerators are being put into practical use.

これにより、設備の設置面積は焼却排ガス冷却部の分が
全く不要となり、接続ダクトが無くなり、支持架構は焼
却炉の分だけで済み、点検歩廊は焼却炉や冷却部ケーシ
ングから張り出したものだけで間に合い、焼却排ガス流
の乱れもほとんど無くなり、したがって、焼却排ガスの
通風圧力損失やダストの堆積、付着などがIg滅され、
メンテナンス上の問題が軽減され、通風のための動力も
低下した。
As a result, the installation area of the equipment is completely unnecessary for the incineration exhaust gas cooling section, there is no connecting duct, the support frame is only for the incinerator, and the inspection walkway is only the one that protrudes from the incinerator and cooling section casing. In time, there is almost no turbulence in the incineration exhaust gas flow, and therefore the ventilation pressure loss of the incineration exhaust gas and the accumulation and adhesion of dust are completely eliminated.
Maintenance problems were reduced and the power required for ventilation was reduced.

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

しかしながら、焼却炉20と焼却排ガス冷却部21を一
体化すると、焼却炉20から輻射の形で多量の熱が焼却
排ガス冷却部21に伝達される結果、焼却炉20内の温
度が低下し、このことは、ある焼却物にとっては有利で
あるが、別の焼却物にとっては却って不都合となり、場
合によりこのような一体化炉を使用することができない
こともあった。
However, when the incinerator 20 and the incineration exhaust gas cooling unit 21 are integrated, a large amount of heat is transferred from the incinerator 20 to the incineration exhaust gas cooling unit 21 in the form of radiation, and as a result, the temperature inside the incinerator 20 decreases. Although this is advantageous for some types of incineration, it is rather inconvenient for other types of incineration, and in some cases, such an integrated furnace cannot be used.

即ち、発熱量の高い焼却物の場合には、炉の冷却負荷が
軽減され、さらに焼却排ガスの冷却に廃熱ボイラや空気
予熱器を用いた場合には、炉の冷却をしなくてよい分だ
け回収可能の熱量が増加する上、輻射により多量の伝熱
を受けるため、廃熱ボイラや空気予熱器の伝熱面積を増
大しなくて済むと言う点で好都合である。
In other words, in the case of incinerated materials with a high calorific value, the cooling load on the furnace is reduced, and when a waste heat boiler or air preheater is used to cool the incineration exhaust gas, there is no need to cool the furnace. This is advantageous in that there is no need to increase the heat transfer area of the waste heat boiler or air preheater because the amount of heat that can be recovered is increased and a large amount of heat is transferred by radiation.

その一方、発熱量の少ない焼却物の場合には、却に必要
な温度に保持するため、助燃材を入れたり増加したりす
ることが必要にになる。それでも十分燃焼できないとき
には、灰や排ガス中の未燃分が増加することになりかね
ない。そこで、このような場合には、焼却炉20と焼却
排ガス冷却部21を一体化せずにそれぞれ別の独立した
設備としたり、或いは、第11図のように変形したもの
として形成するのが普通であった。しかしながら、第1
1図のような設備は、焼却炉20と焼却排ガス冷却部2
1を一体化したとは言っても、接続部の構造が却って複
雑化し、輻射伝熱による焼却炉の冷却も焼却炉の上部に
ついては第1O図のものと同様であり、炉の容積に対し
てその分だけ余裕を見込む必要があった。
On the other hand, in the case of incinerated materials with a low calorific value, it is necessary to add or increase the amount of combustion aid in order to maintain the temperature required for cooling. If sufficient combustion is still not possible, the amount of unburned matter in the ash and exhaust gas may increase. Therefore, in such a case, it is common practice to not integrate the incinerator 20 and the incineration exhaust gas cooling unit 21, but to form them as separate and independent equipment, or to form them as modified pieces as shown in Fig. 11. Met. However, the first
The equipment shown in Figure 1 consists of an incinerator 20 and an incineration exhaust gas cooling section 2.
Even though 1 is integrated, the structure of the connection part is rather complicated, and the cooling of the incinerator by radiation heat transfer is the same as that in Figure 1O for the upper part of the incinerator, and the volume of the incinerator is Therefore, it was necessary to allow for some leeway.

本発明は、従来のものの以上の如き問題点を解決し、設
置面積が少なく、接続ダクトが不要で、支持架構や点検
歩廊も簡単でよく、焼却炉から熱が輻射伝熱により焼却
排ガス冷却部に移動するのを阻止して焼却炉内を必要な
温度に維持せしめ、ガス冷却部を焼却炉と一体化した焼
却装置を提供することを目的としている。
The present invention solves the above-mentioned problems of the conventional ones, requires a small installation area, does not require a connecting duct, has a simple support frame and inspection walkway, and transfers heat from the incinerator to the incineration exhaust gas cooling section by radiant heat transfer. It is an object of the present invention to provide an incinerator in which a gas cooling section is integrated with the incinerator, and the inside of the incinerator is maintained at a necessary temperature by preventing the gas from moving.

〔問題点を解決するための手段及び作用〕本発明は、上
記の問題点を解決する手段として、焼却炉の上部に焼却
排ガス冷却部を一体に載置した焼却装置において、前記
焼却炉と前記焼却リドガス冷却部との接続部付近の排ガ
ス流路中に外面を耐火材で覆った中空の遮蔽体を配備し
たことを特徴とする焼却装置を提供せんとするものであ
り、これにより、焼却炉から排ガス冷却部への輻射伝熱
を阻止し、焼却炉内部の温度を焼却物に応じた温度に維
持し、どのような焼却物に対しても焼却炉の使用を可能
にすることができる。
[Means and operations for solving the problems] As a means for solving the above problems, the present invention provides an incinerator in which an incineration exhaust gas cooling section is integrally mounted on the upper part of the incinerator. It is an object of the present invention to provide an incinerator characterized in that a hollow shield whose outer surface is covered with a refractory material is provided in the exhaust gas flow path near the connection part with the incineration lid gas cooling part, and thereby, the incinerator It is possible to prevent radiant heat transfer from the incinerator to the exhaust gas cooling section, maintain the temperature inside the incinerator at a temperature depending on the material to be incinerated, and make it possible to use the incinerator for any kind of material to be incinerated.

〔実施例〕〔Example〕

本発明の実施例につき図面を用いて説明する。 Embodiments of the present invention will be described with reference to the drawings.

第1図は本発明の第1の実施例を示す。FIG. 1 shows a first embodiment of the invention.

焼却炉1の上には、ガス冷却室、廃熱ボイラまたは空気
予熱器などの焼却排ガス冷却部2が、一体に載置されて
いる。焼却炉1と焼却排ガス冷却部2との接続部付近の
排ガス流路中には、横方向に単一の中空遮蔽体3が設置
されている。中空遮蔽体3は、断面角型で一端または両
端が開放し、自由な空気の流通を許すようになっている
。中空遮蔽体3の寸法、形状、配置は、焼却炉1内の熱
が焼却排ガス冷却部2に輻射によっての伝達がなるべく
行われないように遮断するが、焼却排ガスの流出を阻害
して圧力損失を生ずることのないようなものとする。
An incineration exhaust gas cooling unit 2 such as a gas cooling chamber, a waste heat boiler, or an air preheater is integrally mounted on the incinerator 1 . A single hollow shield 3 is installed laterally in the exhaust gas flow path near the connection between the incinerator 1 and the incineration exhaust gas cooling unit 2. The hollow shield 3 has a rectangular cross section and is open at one or both ends to allow free air circulation. The dimensions, shape, and arrangement of the hollow shield 3 are such that the heat inside the incinerator 1 is prevented from being transmitted to the incineration exhaust gas cooling unit 2 by radiation as much as possible, but it also prevents the outflow of the incineration exhaust gas and reduces pressure loss. shall be such that it will not occur.

第2図は、同じく第2の実施例を示す。FIG. 2 also shows a second embodiment.

焼却炉1の上には上記と同様な焼却排ガス冷却部2が、
一体に接続されている。中空遮蔽体3は、一端または両
端が開放した、多数の、小さい、断面矩形のもので、適
当な間隔を置いて同じ高さに配置されている。
Above the incinerator 1, there is an incineration exhaust gas cooling unit 2 similar to the above.
connected together. The hollow shields 3 are a large number of small, rectangular cross-sections, open at one or both ends, arranged at appropriate intervals and at the same height.

第3図は、第1図および第2図に示す中空遮蔽体の縦断
面図を示す。
FIG. 3 shows a longitudinal cross-sectional view of the hollow shield shown in FIGS. 1 and 2. FIG.

図に示すように、中空遮蔽体3は、両端が焼却炉1のケ
ーシング7から突出し、かつその一方または両方の端面
ば大気に開放している。中空遮蔽体3は、中空遮蔽体ケ
ーシング4の周囲に断熱材5と耐火材6を施したもので
、これにより、焼却炉壁とほぼ同様の断熱性、耐火性を
保持させている。
As shown in the figure, both ends of the hollow shield 3 protrude from the casing 7 of the incinerator 1, and one or both end faces are open to the atmosphere. The hollow shield 3 is formed by applying a heat insulating material 5 and a fireproof material 6 around a hollow shield casing 4, thereby maintaining almost the same heat insulation properties and fire resistance as the incinerator wall.

なお、焼却炉ケーシング7と中空遮蔽体ケーシング4と
の熱膨張差を逃がすために、中空遮蔽体ケーシング4は
一端(図面では左端)を固定し、他端をフリーとし、ア
スベスト等の耐火布を巻付はバンド9によって固定した
エキスパンション8により、炉の内外を遮断し、空気や
焼却排ガスの漏洩を防止している。
In addition, in order to release the difference in thermal expansion between the incinerator casing 7 and the hollow shield casing 4, the hollow shield casing 4 has one end (the left end in the drawing) fixed, the other end free, and is covered with fireproof cloth such as asbestos. The expansion 8 is fixed by a band 9 to isolate the inside and outside of the furnace and prevent air and incineration exhaust gas from leaking.

また、中空遮蔽体3を中空とするとともに、一端または
両端を大気に開放することにより、その温度上昇を内部
を流通する大気との熱交換により抑制している。そのた
め、中空遮蔽体3の耐火物6も、焼却炉壁と同様に、中
空遮蔽体ケーシング4へ断熱材5を通して若干の放熱を
行うことで保護されている。しかし、この中空遮蔽体3
を介して、焼却炉1内の熱が大量に外部に放散されるよ
うなことは避けなければならない。
Moreover, by making the hollow shield 3 hollow and opening one or both ends to the atmosphere, the temperature increase is suppressed by heat exchange with the atmosphere circulating inside. Therefore, like the incinerator wall, the refractory 6 of the hollow shield 3 is also protected by passing a heat insulating material 5 through the hollow shield casing 4 to radiate some heat. However, this hollow shield 3
It must be avoided that a large amount of heat within the incinerator 1 is dissipated to the outside through the incinerator.

耐火レンガ等、通常比重が1〜3のものが、また断熱材
5としては、セラミックス断熱ボードや、断熱キャスタ
ブル等、比重が0.1〜0.3の小さいものを用いるの
が望ましい。
It is desirable to use a material with a specific gravity of usually 1 to 3, such as a refractory brick, and as the heat insulating material 5, a material with a small specific gravity of 0.1 to 0.3, such as a ceramic heat insulating board or a heat insulating castable, is used.

中空遮蔽体ケーシング4を鋼製とするときは、耐火材6
自体断熱効果があって中空遮蔽体ケーシング4の温度が
300℃望ましくは200℃前後以下に抑えることがで
きるならば、とくに断熱材を施す必要はない。耐熱鋼を
中空遮蔽体ケーシング4に用いるならば、その温度をさ
らに上げることもできる。中空遮蔽体ケーシング4内の
空気を強制換気することは、中空遮蔽体3の温度を抑え
るのに有効である。
When the hollow shield casing 4 is made of steel, the fireproof material 6
If the hollow shield casing 4 itself has a heat insulating effect and the temperature of the hollow shield casing 4 can be suppressed to 300° C., preferably around 200° C. or less, there is no need to provide any particular heat insulating material. If heat-resistant steel is used for the hollow shield casing 4, its temperature can also be increased further. Forced ventilation of the air within the hollow shield casing 4 is effective in suppressing the temperature of the hollow shield 3.

第4図は中空遮蔽体3の別の構造を示す。FIG. 4 shows another structure of the hollow shield 3. In FIG.

第1図の実施例のように、中空部分の断面積が大きく、
しかも中空遮蔽体ケーシング4と焼却炉ケーシング7と
の温度差が小さく、熱膨張差による発生応力が無視でき
る場合には、第4図に示すように、焼却炉ケーシング7
と中空遮蔽体ケーシある。
As in the embodiment shown in Fig. 1, the cross-sectional area of the hollow part is large;
Moreover, if the temperature difference between the hollow shield casing 4 and the incinerator casing 7 is small and the stress generated due to the difference in thermal expansion can be ignored, as shown in FIG.
and a hollow shield casing.

なお、中空遮蔽体3の形状は、その上にダストが溜まる
ことや、排ガス流を乱すことを考えてその形状を定める
必要があり、第1図のように傾斜させたり、第2図のよ
うに幅を狭くするのが好ましい。
Note that the shape of the hollow shield 3 must be determined taking into account the possibility that dust will accumulate on it and the exhaust gas flow will be disturbed. It is preferable to narrow the width.

上記のような構成を備えることにより、焼却炉1と焼却
排ガス冷却部2とが一体に構成されているにも関わらず
、焼却炉1から排ガス冷却部2への輻射による熱伝達が
ほぼ阻止され、第7図ないし第9図に示す別体型と同様
に熱的関係を断つことができる。
By having the above-described configuration, heat transfer by radiation from the incinerator 1 to the exhaust gas cooling unit 2 is almost prevented, even though the incinerator 1 and the incineration exhaust gas cooling unit 2 are integrally configured. , the thermal relationship can be severed in the same way as with the separate type shown in FIGS. 7 to 9.

第5図は別の実施例を示す。FIG. 5 shows another embodiment.

この実施例においては、中空遮蔽体3は、焼却炉1の上
部の排ガス冷却部2と接続部の付近の排ガス流路中に千
鳥状に設置された多数の中空管から構成されている。こ
の実施例においては、焼却炉lから排ガス冷却部2への
輻射熱伝達は殆ど完全に阻止される。
In this embodiment, the hollow shield 3 is composed of a large number of hollow tubes installed in a staggered manner in the exhaust gas flow path near the exhaust gas cooling section 2 and the connection section in the upper part of the incinerator 1. In this embodiment, the radiation heat transfer from the incinerator I to the exhaust gas cooling section 2 is almost completely prevented.

第6図はさらに別の実施例を示し、焼却炉1は流動床1
0およびフリーボード部11を備えたものとして構成さ
れている。
FIG. 6 shows yet another embodiment, in which the incinerator 1 is a fluidized bed 1.
0 and a freeboard section 11.

焼却炉lの側壁にはバーナ12が設けられ、助燃物と燃
焼用空気の一部が供給される。燃焼用空気の大部分は流
動床10の下方から供給され、流動床10の流動化後上
方から投入された焼却物を焼却する。このような流動床
式焼却炉においては、流動床IOの温度を少なくとも5
00℃以上、望ましくは 600°C以上に保持するこ
とが焼却炉1の運転に不可欠であり、そのためには、と
くに低発熱量の焼却物の場合、極力流動床1oからの熱
の流出を抑え或いは熱の流入を高めることが燃焼の安定
や助燃物の使用量の低減につながることになる。
A burner 12 is provided on the side wall of the incinerator 1, to which auxiliary combustion materials and a portion of combustion air are supplied. Most of the combustion air is supplied from below the fluidized bed 10, and after fluidization of the fluidized bed 10, the incineration material introduced from above is incinerated. In such a fluidized bed incinerator, the temperature of the fluidized bed IO is at least 5
It is essential for the operation of the incinerator 1 to maintain the temperature at 00°C or higher, preferably at 600°C or higher, and for this purpose, it is necessary to suppress the outflow of heat from the fluidized bed 1o as much as possible, especially in the case of incinerated materials with a low calorific value. Alternatively, increasing the inflow of heat leads to stabilization of combustion and a reduction in the amount of combustion aids used.

従って、中空遮蔽体3によりフリーボード部11に高温
を維持し、フリーボード部11がら流動床10への熱の
流入を増加し、流動床1oから排ガス冷却部2への熱の
流出を抑制することは、そのまま焼却機能の向上や助燃
費の低減につらなり、とくに効果が大きい。
Therefore, the hollow shield 3 maintains a high temperature in the freeboard section 11, increases the flow of heat from the freeboard section 11 into the fluidized bed 10, and suppresses the outflow of heat from the fluidized bed 1o to the exhaust gas cooling section 2. This directly leads to improved incineration function and reduced fuel consumption, which is particularly effective.

上記第5図および第6図における中空遮蔽体3は、事情
に応じて、第3図または゛第4図のいずれかの如き構造
とすることができる。
The hollow shielding body 3 in FIGS. 5 and 6 above may have a structure as shown in either FIG. 3 or FIG. 4 depending on the circumstances.

〔発明の効果〕〔Effect of the invention〕

本発明により、焼却炉の上部に焼却排ガス冷却部が一体
に載置された焼却装置において、て焼却炉内の熱が輻射
の形で焼却排ガス冷却部に伝達されるのを阻止すること
が容易となったので、どのような焼却物に対しても、焼
却炉と排ガス冷却部を一体化した単純な構造の焼却炉を
使用することが可能になり、敷地面積の節約、構造物の
単純化排ガス圧力損失の低減、ダスト付着の減少等が可
能となり、建設費、運転費の低下および維持管理に与え
る効果は著しく大きい。
According to the present invention, in an incinerator in which the incineration exhaust gas cooling section is integrally mounted on the upper part of the incinerator, it is easy to prevent the heat in the incinerator from being transmitted to the incineration exhaust gas cooling section in the form of radiation. As a result, it is now possible to use an incinerator with a simple structure that integrates the incinerator and exhaust gas cooling section for any type of incineration material, saving site space and simplifying the structure. This makes it possible to reduce exhaust gas pressure loss, reduce dust adhesion, etc., and has a significant effect on lowering construction costs, operating costs, and maintenance management.

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

第1図、第2図、第5図、および第6図は、本発明の実
施例を示す線図的側断面図、第3図および第4図は上記
実施例における中空遮蔽体の縦断側面図、第7図、第8
図および第9図は従来の別図は従来の一体型の焼却炉の
線図的側断面図である。 1・・・焼却炉  2・・・排ガス冷却部3・・・中空
遮蔽体 4・・・中空遮蔽体ケーシング 5・・・断熱材   6・・・耐火材 7・・・ケーシング 8・・・エキスパンション  9・・・バンド10・・
流動床   11・・フリーボード部12・・バーナ 
   20・・・焼却炉21・・排ガス冷却部 22・・ガス冷却室  23・・空気予熱器24・・電
気集塵器  25・・誘引送風機26・・煙突   2
7・・噴射水加圧ポンプ28・・押込送風機  29・
・廃熱ボイラ30・・空気予熱器 31・・白煙対策用熱交換器 32・・サイクロン  33・・スクラバ34・・白煙
対策用ファン。 第4図 第5図
1, 2, 5, and 6 are schematic side sectional views showing embodiments of the present invention, and FIGS. 3 and 4 are longitudinal sectional side views of the hollow shield in the above embodiments. Figure, Figure 7, Figure 8
FIG. 9 is a diagrammatic side sectional view of a conventional integrated incinerator. 1... Incinerator 2... Exhaust gas cooling unit 3... Hollow shield 4... Hollow shield casing 5... Heat insulating material 6... Refractory material 7... Casing 8... Expansion 9...Band 10...
Fluidized bed 11...Freeboard section 12...Burner
20...Incinerator 21...Exhaust gas cooling unit 22...Gas cooling room 23...Air preheater 24...Electric precipitator 25...Induced blower 26...Chimney 2
7. Injection water pressure pump 28. Forced blower 29.
・Waste heat boiler 30・・Air preheater 31・・Heat exchanger 32・・Cyclone 33・・Scrubber 34・・Fan for white smoke prevention. Figure 4 Figure 5

Claims (1)

【特許請求の範囲】[Claims] 1、焼却炉の上部に焼却排ガス冷却部を一体に載置した
焼却装置において、前記焼却炉と前記焼却排ガス冷却部
との接続部付近の排ガス流路中に外面を耐火材で覆った
中空の遮蔽体を配備したことを特徴とする焼却装置。
1. In an incinerator in which an incineration exhaust gas cooling unit is integrally mounted on the upper part of the incinerator, a hollow space whose outer surface is covered with a refractory material is provided in the exhaust gas flow path near the connection between the incinerator and the incineration exhaust gas cooling unit. An incinerator characterized by being equipped with a shield.
JP60034497A 1985-02-25 1985-02-25 Incinerator Granted JPS61195208A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP60034497A JPS61195208A (en) 1985-02-25 1985-02-25 Incinerator

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP60034497A JPS61195208A (en) 1985-02-25 1985-02-25 Incinerator

Publications (2)

Publication Number Publication Date
JPS61195208A true JPS61195208A (en) 1986-08-29
JPH0160729B2 JPH0160729B2 (en) 1989-12-25

Family

ID=12415885

Family Applications (1)

Application Number Title Priority Date Filing Date
JP60034497A Granted JPS61195208A (en) 1985-02-25 1985-02-25 Incinerator

Country Status (1)

Country Link
JP (1) JPS61195208A (en)

Cited By (12)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS61282713A (en) * 1985-06-06 1986-12-12 Ngk Insulators Ltd Combustion furnace
JPS62175511A (en) * 1986-01-30 1987-08-01 Ebara Corp Method for operating combustion device and combustion device
JPS63189709A (en) * 1987-02-03 1988-08-05 Ebara Infilco Co Ltd Recombustion apparatus for incinerator
JPS63251715A (en) * 1987-04-09 1988-10-19 Ngk Insulators Ltd Heat recovery type incinerator
JPS63315821A (en) * 1987-06-15 1988-12-23 Kobe Steel Ltd Incinerating apparatus
JPH01247911A (en) * 1988-03-30 1989-10-03 Ebara Corp Burner
JPH01170833U (en) * 1988-05-16 1989-12-04
JPH03244908A (en) * 1990-02-22 1991-10-31 Hitachi Zosen Corp Combustion promoting device in incinerator
JPH03244907A (en) * 1990-02-22 1991-10-31 Hitachi Zosen Corp Incinerator
US5178531A (en) * 1989-02-17 1993-01-12 Ebara Corporation Fluidized bed combustion furnace
US5257585A (en) * 1991-04-15 1993-11-02 Ebara Corporation Incinerator
JP2007170682A (en) * 2005-12-19 2007-07-05 Takuma Co Ltd Dioxins suppressing method for incineration facility

Cited By (15)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH0549892B2 (en) * 1985-06-06 1993-07-27 Ngk Insulators Ltd
JPS61282713A (en) * 1985-06-06 1986-12-12 Ngk Insulators Ltd Combustion furnace
JPS62175511A (en) * 1986-01-30 1987-08-01 Ebara Corp Method for operating combustion device and combustion device
JPH0361086B2 (en) * 1986-01-30 1991-09-18 Ebara Mfg
JPS63189709A (en) * 1987-02-03 1988-08-05 Ebara Infilco Co Ltd Recombustion apparatus for incinerator
JPS63251715A (en) * 1987-04-09 1988-10-19 Ngk Insulators Ltd Heat recovery type incinerator
JPS63315821A (en) * 1987-06-15 1988-12-23 Kobe Steel Ltd Incinerating apparatus
JPH0366564B2 (en) * 1987-06-15 1991-10-17 Kobe Steel Ltd
JPH01247911A (en) * 1988-03-30 1989-10-03 Ebara Corp Burner
JPH01170833U (en) * 1988-05-16 1989-12-04
US5178531A (en) * 1989-02-17 1993-01-12 Ebara Corporation Fluidized bed combustion furnace
JPH03244907A (en) * 1990-02-22 1991-10-31 Hitachi Zosen Corp Incinerator
JPH03244908A (en) * 1990-02-22 1991-10-31 Hitachi Zosen Corp Combustion promoting device in incinerator
US5257585A (en) * 1991-04-15 1993-11-02 Ebara Corporation Incinerator
JP2007170682A (en) * 2005-12-19 2007-07-05 Takuma Co Ltd Dioxins suppressing method for incineration facility

Also Published As

Publication number Publication date
JPH0160729B2 (en) 1989-12-25

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