JPH07243604A - Dust burning boiler - Google Patents

Dust burning boiler

Info

Publication number
JPH07243604A
JPH07243604A JP6550794A JP6550794A JPH07243604A JP H07243604 A JPH07243604 A JP H07243604A JP 6550794 A JP6550794 A JP 6550794A JP 6550794 A JP6550794 A JP 6550794A JP H07243604 A JPH07243604 A JP H07243604A
Authority
JP
Japan
Prior art keywords
pressurized air
combustion chamber
chamber
combustion
heat
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
JP6550794A
Other languages
Japanese (ja)
Other versions
JP2769289B2 (en
Inventor
Yutaka Sanbonmatsu
豊 三本松
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.)
Individual
Original Assignee
Individual
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 Individual filed Critical Individual
Priority to JP6065507A priority Critical patent/JP2769289B2/en
Priority to TW085206981U priority patent/TW296772U/en
Priority to US08/315,712 priority patent/US5590610A/en
Publication of JPH07243604A publication Critical patent/JPH07243604A/en
Application granted granted Critical
Publication of JP2769289B2 publication Critical patent/JP2769289B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Abstract

PURPOSE:To ensure effectual heat exchange without the need of auxiliary treatment by heating water in a heat exchange water pipe by making use of heat produced when dust is burned. CONSTITUTION:Many heat exchange water pipes 14 are disposed on a wall 8 for defining a combustion chamber. A blower 20 as external pressurized air supply means is provided dispersed substantially over the entire surface of the wall 8, to which blower 20 there are connected a pressurized air nozzle 21 having many small holes. Pressurized air supplied from the blower 20 is injected from the pressurized air nozzle 21 into the combustion chamber 7 to simultaneously burn dust in the combustion chamber 7. Water in the heat exchange water pipes 14 is heated with the combustion heat. Hereby, effectual heat exchange is ensured without the need of auxiliary treatment.

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【産業上の利用分野】本発明は、ごみを焼却する際に生
じる熱を利用して水を加熱するごみ焚きボイラに関する
ものである。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a waste fired boiler which heats water by utilizing heat generated when incinerating waste.

【0002】[0002]

【従来の技術】従来、木クズ、紙クズ、廃プラスチック
等のごみは単にごみ焼却炉にて燃やして廃棄していた。
このとき、通常のごみ焼却炉によるごみの燃焼ではその
燃焼効率が悪く、不完全燃焼による大量の排煙が生じる
ことから排気通路に補助バーナを設けて、更に燃焼させ
て排気を浄化するようになっている。
2. Description of the Related Art Conventionally, refuse such as wood waste, paper waste and waste plastic has been simply burned in a refuse incinerator and discarded.
At this time, the combustion efficiency of ordinary waste incinerators is poor, and a large amount of smoke is generated due to incomplete combustion.Therefore, an auxiliary burner should be installed in the exhaust passage to further burn and purify the exhaust gas. Has become.

【0003】一方、近年省資源、省エネルギー並びに省
コストの観点からごみの焼却時に発生する熱を利用した
ごみ焚きボイラの開発が望まれている。
On the other hand, in recent years, from the viewpoint of resource saving, energy saving, and cost saving, it has been desired to develop a refuse-fired boiler that utilizes heat generated during incineration of refuse.

【0004】[0004]

【発明が解決しようとする課題】しかしながら、一般的
なごみ焼却炉によるごみの燃焼により発生する熱量は油
焚きボイラ等に比較して低く、上記したようなごみ焼却
炉によるごみの燃焼により発生する熱量では熱交換後に
到底所要の熱量が得られないと云う問題があった。
However, the amount of heat generated by the combustion of waste in a general waste incinerator is lower than that of oil-fired boilers, etc., and the amount of heat generated by the combustion of waste in the waste incinerator as described above is There was a problem that the required amount of heat could not be obtained after heat exchange.

【0005】上記問題を解決するには熱交換率及び/ま
たは燃焼室内温度を上げると良い。そこで、例えば上記
した補助バーナを燃焼室に設けて燃焼室内の熱量を上げ
ることも考えられるが、ごみ処理の煩雑さ、燃料の消費
量などを考慮すると通常のボイラに比較して資源やコス
トの面で優位性があるとは云えず、あまり現実的ではな
い。
To solve the above problem, it is preferable to increase the heat exchange rate and / or the temperature in the combustion chamber. Therefore, for example, it is conceivable to provide the above-mentioned auxiliary burner in the combustion chamber to increase the amount of heat in the combustion chamber, but considering the complexity of waste treatment, fuel consumption, etc., resources and cost will be lower than those of ordinary boilers. It cannot be said that there is an advantage in terms of terms, and it is not very realistic.

【0006】また、ごみを細かく砕いた後、架橋剤を用
いて所望の大きさのブロックに加工して固形燃料として
使用し、燃焼室内の熱量を上げることも提案されている
が、その加工作業が煩雑であり、また加工コストも高騰
化することから、更にこのような固形燃料を用いても必
ずしも燃焼室内に所望の熱量は得られず、結局補助バー
ナ等を必要とすることから上記同様あまり現実的ではな
い。
It has also been proposed that the waste be finely crushed and then processed into a block of a desired size by using a cross-linking agent to be used as a solid fuel to increase the amount of heat in the combustion chamber. Is complicated, and the processing cost also rises. Therefore, even if such a solid fuel is used, a desired amount of heat cannot always be obtained in the combustion chamber, and an auxiliary burner or the like is eventually required, so much as above. Not realistic.

【0007】本発明は上記したような従来技術の問題点
に鑑みなされたものであり、その主な目的は、補助的な
処理を必要とすることなく、効率的に熱交換可能であ
り、かつごみを効率的に燃焼させて燃焼室内に高い熱量
を得ることができるごみ焚きボイラを提供することにあ
る。
The present invention has been made in view of the above-mentioned problems of the prior art, and its main purpose is to enable efficient heat exchange without requiring auxiliary treatment, and An object of the present invention is to provide a refuse-fired boiler capable of efficiently burning refuse and obtaining a high heat quantity in the combustion chamber.

【0008】[0008]

【課題を解決するための手段】上述した目的は本発明に
よれば、燃焼室を画定すると共に多数の熱交換用水管が
配設された壁部と、外部加圧エア供給手段と、前記燃焼
室に向けて加圧エアを噴射するべく、前記壁部の略全面
に亘り分散して開設され、かつ前記外部加圧エア供給手
段に接続された多数の小孔からなる加圧エア噴射口と、
前記燃焼室にごみを投入するためのごみ投入口とを有
し、前記加圧エア供給手段から供給された加圧エアを前
記加圧エア噴射口から前記燃焼室内に向けて噴射しつつ
該燃焼室内のごみを燃焼させ、その燃焼熱をもって前記
水管内液を加熱することを特徴とするごみ焚きボイラを
提供することにより達成される。特に、前記壁部が、多
数の水管と各水管間に設けられた吸熱フィンとを有し、
前記加圧エア噴射口が、前記吸熱フィンの略全面に亘り
分散して開設された多数の小孔からなると良い。
SUMMARY OF THE INVENTION According to the present invention, the above objects are achieved by defining a combustion chamber and a wall portion on which a large number of heat exchange water pipes are arranged, an external pressurized air supply means, and the combustion chamber. A pressurized air injection port formed of a large number of small holes connected to the external pressurized air supply means and distributed over substantially the entire surface of the wall portion to inject pressurized air toward the chamber; ,
A combustion chamber for injecting dust into the combustion chamber, and injecting the pressurized air supplied from the pressurized air supply means toward the combustion chamber from the pressurized air injection port. The present invention is achieved by providing a refuse-fired boiler characterized by burning waste in a room and heating the liquid in the water pipe with the heat of combustion. In particular, the wall portion has a large number of water pipes and heat absorbing fins provided between the water pipes,
It is preferable that the pressurized air jet port is composed of a large number of small holes that are distributed and formed over substantially the entire surface of the heat absorbing fin.

【0009】[0009]

【作用】このように、燃焼室を画定する壁部に設けられ
た多数の小孔から加圧エアを燃焼室内に供給することに
より、酸素が被燃焼物内部まで十分に供給され、かつ燃
焼室内がまんべんなく攪拌される。また、この壁部をな
す水管間の吸熱フィンに上記多数の小孔を設けることに
より、熱交換が行われる水管及び吸熱フィンの表面に極
近い燃焼室内の空気が攪拌され、熱伝達率を向上するこ
とができる。更に、燃焼室と外気との間に燃焼室に供給
する加圧エアの通路をなす空室を介在させることによ
り、この空室により燃焼室が外部から断熱され、かつこ
の空室内を通過するガスが加温され、この吸熱フィンか
らの高温(100℃以上)の加圧空気が水分の多いゴミ
に対しても有効で乾燥と焼却とを同時進行させるため、
燃焼室内の燃焼温度が相乗的に高くなる。従って、熱の
移動に最も効率的な輻射伝熱が増加し、一層熱伝達率が
向上する。
As described above, by supplying the pressurized air into the combustion chamber through the large number of small holes provided in the wall portion defining the combustion chamber, oxygen is sufficiently supplied to the inside of the combustion object and the combustion chamber is Stir evenly. Further, by providing the large number of small holes in the heat absorbing fins between the water pipes forming the wall portion, the air in the combustion chamber that is very close to the surfaces of the water pipes and the heat absorbing fins for heat exchange is agitated, and the heat transfer coefficient is improved. can do. Furthermore, by interposing an empty chamber that forms a passage for the pressurized air supplied to the combustion chamber between the combustion chamber and the outside air, the combustion chamber is thermally insulated from the outside by this empty chamber, and the gas passing through this empty chamber is also provided. Is heated, and high-temperature (100 ° C. or higher) pressurized air from the heat-absorbing fins is effective even for dust with a large amount of water, and drying and incineration proceed simultaneously,
The combustion temperature in the combustion chamber increases synergistically. Therefore, the most efficient radiant heat transfer for heat transfer increases, and the heat transfer coefficient further improves.

【0010】[0010]

【実施例】以下、添付の図面に従って本発明の好適実施
例について説明する。
DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENT A preferred embodiment of the present invention will be described below with reference to the accompanying drawings.

【0011】図1は本発明が適用されたごみ焚きボイラ
の概略構成を示す部分断面図である。このボイラは、燃
焼炉本体1と、該燃焼炉本体1に排気管2を介して接続
されたサイクロン集塵器3とを有している。集塵器3に
は、霧吹きと同様な原理により排気管2を介して燃焼炉
本体1の後記する燃焼室下流側がやや負圧になるように
排気を吸引し、煙突5に導くエゼクタ4が付設されてい
る。
FIG. 1 is a partial cross-sectional view showing a schematic structure of a refuse-fired boiler to which the present invention is applied. This boiler has a combustion furnace main body 1 and a cyclone dust collector 3 connected to the combustion furnace main body 1 via an exhaust pipe 2. The dust collector 3 is provided with an ejector 4 for sucking the exhaust gas through the exhaust pipe 2 so that the downstream side of the combustion chamber, which will be described later, has a slightly negative pressure through the exhaust pipe 2 and guiding it to the chimney 5 through the exhaust pipe 2. Has been done.

【0012】燃焼炉本体1は、ごみを燃焼するための内
部燃焼室7を画定する筒状の内壁8と、内壁8の外周面
との間に該内壁8の略全面を覆う空室9を画定する外壁
10と、燃焼室7の下流側、即ち燃焼炉本体1の図に於
ける上部に設けられ、燃焼室7から外部に向けて開口す
るごみ投入口11と灰の取り出し口12とを有してい
る。ここで、図2に併せて示すように、内壁8は多数の
水管14と各水管14間に設けられた吸熱フィン15と
から構成されている。各水管14はその下部にて環状の
分配管16に接続されている。この分配管16は図示さ
れない水の供給手段に接続管17をもって接続されてい
る。また、各水管14はその上部にて集合管18に接続
されている。この集合管18は排出管19を介して図示
されない蒸気を利用する不図示の設備に接続されてい
る。
The combustion furnace body 1 has a cylindrical inner wall 8 defining an internal combustion chamber 7 for burning dust, and an empty chamber 9 covering substantially the entire inner wall 8 between the outer peripheral surface of the inner wall 8. The defining outer wall 10, a downstream side of the combustion chamber 7, that is, an upper part of the combustion furnace main body 1 in the figure, which is provided with a dust inlet 11 and an ash outlet 12 that are open to the outside from the combustion chamber 7 are provided. Have Here, as also shown in FIG. 2, the inner wall 8 is composed of a large number of water pipes 14 and heat absorbing fins 15 provided between the water pipes 14. Each water pipe 14 is connected at its lower part to an annular distribution pipe 16. The distribution pipe 16 is connected to a water supply means (not shown) with a connection pipe 17. Further, each water pipe 14 is connected to the collecting pipe 18 at the upper part thereof. The collecting pipe 18 is connected via a discharge pipe 19 to a facility (not shown) that uses steam (not shown).

【0013】一方、空室9には外部加圧エア供給手段と
してのブロワ20がダンパ22を介して接続され、空室
9内に加圧エアを供給するようになっている。内壁8を
なす吸熱フィン15には、空室9と燃焼室7とを連通す
るべく加圧エア噴射口としての多数の小孔21が略等間
隔に開設され、ブロワ20から空室9に送られた加圧エ
アを各小孔21から燃焼室7に供給するようになってい
る。また、ブロワ20はダンパ22を介してエゼクタ4
にも接続され、後記するように燃焼室7の下流側を負圧
にするようになっている。
On the other hand, a blower 20 as an external pressurized air supply means is connected to the vacant chamber 9 via a damper 22 so as to supply pressurized air into the vacant chamber 9. The heat-absorbing fins 15 forming the inner wall 8 are provided with a number of small holes 21 as pressurized air injection ports at substantially equal intervals so as to connect the chamber 9 and the combustion chamber 7 to each other. The pressurized air thus obtained is supplied to the combustion chamber 7 through the small holes 21. Further, the blower 20 is connected to the ejector 4 via the damper 22.
Also, the downstream side of the combustion chamber 7 is made to have a negative pressure as described later.

【0014】以下に本実施例の作動要領について説明す
る。まず、所定の点火方法により燃焼室内にて燃焼を開
始し、同時にブロワ20から加圧エアを供給する。する
と、この加圧エアは空室9を通過して各小孔21から略
均等に燃焼室7内に噴射される(図3)。このとき、加
圧エアが充満する空室9による断熱作用が期待できるば
かりでなく、加圧エアが空室9を通過する間に加温され
ることから、更に燃焼室7内に加圧エアが噴射される際
に高温の吸熱フィン15により加熱されることから燃焼
室7内の燃焼温度を上昇させ、燃焼効率を向上できる。
また、加圧エアが各小孔21から略均等に燃焼室7内に
噴射されることにより、酸素が燃焼内部まで十分に供給
されると共に燃焼室7内が攪拌され、これよっても燃焼
効率を向上できる。
The operating procedure of this embodiment will be described below. First, combustion is started in the combustion chamber by a predetermined ignition method, and at the same time, pressurized air is supplied from the blower 20. Then, the pressurized air passes through the empty chamber 9 and is sprayed from the small holes 21 into the combustion chamber 7 substantially uniformly (FIG. 3). At this time, not only can the insulating chamber 9 filled with the pressurized air be expected to have a heat insulating effect, but since the pressurized air is heated while passing through the chamber 9, the compressed air is further introduced into the combustion chamber 7. Since the fuel is heated by the high temperature endothermic fins 15 when injected, the combustion temperature in the combustion chamber 7 can be increased and the combustion efficiency can be improved.
Further, the pressurized air is injected into the combustion chamber 7 from each of the small holes 21 substantially uniformly, so that oxygen is sufficiently supplied to the inside of the combustion and the inside of the combustion chamber 7 is agitated. Can be improved.

【0015】一方、一般に水管や吸熱フィンの表面近傍
の燃焼室内温度は水管内部温度に近く、水管から離れる
に従い高温になっているが、図3に示すように、吸熱フ
ィン15に各小孔21を設けることにより、熱交換が行
われる水管14及び吸熱フィン15の表面に極近い燃焼
室7内の空気が攪拌され、水管14及び吸熱フィン15
の表面に極近い空気をも高温にすることができ、熱伝達
率を向上することができる。また、本ボイラは直焚きで
あることから炎から直接輻射伝熱を受けることができる
ため、一般的な廃熱ボイラに比して全体として熱伝達率
を向上することができ、総括伝熱係数も油焚きボイラに
匹敵する高い値が得られる。加えて、加圧空気による乱
流は水管14及び吸熱フィン15に灰等の不純物が付着
することを防止し、熱伝達率の低下を防いでいる。
On the other hand, generally, the temperature of the combustion chamber near the surface of the water pipe or the heat absorbing fin is close to the temperature inside the water pipe and becomes higher as the distance from the water pipe increases, but as shown in FIG. By providing the above, the air in the combustion chamber 7 that is very close to the surfaces of the water tubes 14 and the heat absorbing fins 15 where heat is exchanged is stirred, and the water tubes 14 and the heat absorbing fins 15 are
The temperature of the air very close to the surface can be raised to a high temperature, and the heat transfer coefficient can be improved. In addition, since this boiler is directly fired, it can receive radiant heat directly from the flame, so it can improve the heat transfer coefficient as a whole compared to general waste heat boilers, and the overall heat transfer coefficient. Also, high values comparable to oil-fired boilers can be obtained. In addition, the turbulent flow due to the pressurized air prevents impurities such as ash from adhering to the water pipe 14 and the heat absorbing fins 15 and prevents the heat transfer coefficient from decreasing.

【0016】上記燃焼により発生した排気はエゼクタ4
により排気管2を介してサイクロン集塵器3に導かれ、
その後煙突5から排出される。このとき、エゼクタ4に
て排気を吸引していることにより燃焼室7の下流側(図
に於ける上側)がやや負圧になっており、ごみ投入口1
1を解放したままであっても外部に炎が吹き出す心配が
ない。従って、燃焼中でも随時ごみを燃焼室7内に投入
することができる。
The exhaust gas generated by the above combustion is ejector 4
Is guided to the cyclone dust collector 3 via the exhaust pipe 2,
After that, it is discharged from the chimney 5. At this time, the exhaust side is sucked by the ejector 4, so that the downstream side (upper side in the drawing) of the combustion chamber 7 is slightly negative pressure, and the dust inlet 1
Even if 1 is left open, there is no concern that the flame will blow out to the outside. Therefore, dust can be thrown into the combustion chamber 7 at any time even during combustion.

【0017】一方、上記した燃焼を行っている間に水を
分配管16から各水管14に供給し、熱交換してその蒸
気を集合管18及び排出管19を介して外部設備で利用
することとなる。
On the other hand, during the above-mentioned combustion, water is supplied from the distribution pipe 16 to each water pipe 14, heat is exchanged, and the steam is used in an external facility through the collecting pipe 18 and the discharge pipe 19. Becomes

【0018】尚、本実施例に於ては内壁と外壁との間に
空室を画定し、その空室を介して加圧エアを噴射口とし
ての多数の小孔に供給したが、例えば空室を画定せず、
パイプなどを介して各噴射口にブロワから直接加圧エア
を供給しても良い。
In this embodiment, an empty chamber is defined between the inner wall and the outer wall, and pressurized air is supplied to a large number of small holes as the injection ports through the empty chamber. Without demarcating the chamber,
Pressurized air may be directly supplied from a blower to each injection port via a pipe or the like.

【0019】[0019]

【発明の効果】上述の説明により明らかなように、本発
明によるごみ焚きボイラによれば、燃焼室を画定する壁
部に設けられた多数の小孔から加圧エアを燃焼室内に供
給することにより、酸素が燃焼内部まで十分に供給さ
れ、かつ燃焼室内がまんべんなく攪拌される。従って、
通常、廃棄物の燃焼は理論的必要空気量の2倍程度の空
気を供給する(空気過剰率m=2)ことで燃焼を維持す
るがこの高温加圧空気では空気過剰率m=1.5程度で
ゴミ焼却が可能であり、炎の温度は高温白色化し、燃焼
室内にて高い熱量の効率的な燃焼が行われる。また、こ
の壁部をなす水管間の吸熱フィンに上記多数の小孔を設
けることにより、熱交換が行われる水管及び吸熱フィン
の表面に極近い燃焼室内の空気が攪拌され、熱伝導効率
を向上することができ、熱伝達率が向上する。更に、燃
焼室と外気との間に燃焼室に供給する加圧エアの通路を
なす空室を介在させることにより、この空室により燃焼
室が外部から断熱される、かつこの空室内を通過するガ
スが加温され、燃焼室内の温度が相乗的に高くなる。以
上のことから油焚きボイラと同等若しくはそれ以上の性
能をごみの燃焼により確保できるため、その効果は大で
ある。
As is apparent from the above description, according to the dust-burning boiler of the present invention, the pressurized air is supplied into the combustion chamber through the large number of small holes provided in the wall portion defining the combustion chamber. As a result, oxygen is sufficiently supplied to the inside of the combustion, and the inside of the combustion chamber is evenly stirred. Therefore,
Normally, for combustion of waste, combustion is maintained by supplying about twice the theoretically required amount of air (air excess ratio m = 2), but with this high temperature pressurized air, the air excess ratio m = 1.5. It is possible to incinerate dust with a certain degree, the temperature of the flame becomes white at high temperature, and efficient combustion with a high heat quantity is performed in the combustion chamber. Further, by providing the above-mentioned many small holes in the heat absorbing fins between the water pipes forming the wall portion, the air in the combustion chamber which is very close to the surfaces of the water pipes and the heat absorbing fins for heat exchange is agitated, and the heat transfer efficiency is improved. It is possible to improve the heat transfer coefficient. Further, by interposing a vacant chamber that forms a passage for pressurized air supplied to the combustion chamber between the combustion chamber and the outside air, the combustion chamber is insulated from the outside by the vacant chamber and passes through the vacant chamber. The gas is heated and the temperature inside the combustion chamber is increased synergistically. From the above, it is possible to secure the performance equal to or higher than that of the oil-fired boiler by burning the waste, and the effect is great.

【図面の簡単な説明】[Brief description of drawings]

【図1】本発明が適用されたごみ焚きボイラの概略構成
を示す部分断面図である。
FIG. 1 is a partial cross-sectional view showing a schematic configuration of a refuse-fired boiler to which the present invention has been applied.

【図2】図1のII−II線について見た断面図である。FIG. 2 is a sectional view taken along line II-II in FIG.

【図3】燃焼室内のエアの流れを説明する図2の拡大図
である。
FIG. 3 is an enlarged view of FIG. 2 illustrating the flow of air in the combustion chamber.

【符号の説明】[Explanation of symbols]

1 燃焼炉本体 2 排気管 3 集塵器 4 エゼクタ 5 煙突 7 燃焼室 8 内壁 9 空室 10 外壁 11 ごみ投入口 12 灰取り出し口 14 水管 15 吸熱フィン 16 分配管 17 接続管 18 集合管 19 排出管 20 ブロワ 21 小孔 22 ダンパ 1 Combustion furnace main body 2 Exhaust pipe 3 Dust collector 4 Ejector 5 Chimney 7 Combustion chamber 8 Inner wall 9 Vacancy 10 Outer wall 11 Waste input port 12 Ash removal port 14 Water pipe 15 Endothermic fin 16 Minute pipe 17 Connection pipe 18 Collecting pipe 19 Exhaust pipe 20 Blower 21 Small hole 22 Damper

Claims (3)

【特許請求の範囲】[Claims] 【請求項1】 燃焼室を画定すると共に多数の熱交換
用水管が配設された壁部と、 外部加圧エア供給手段と、 前記燃焼室に向けて加圧エアを噴射するべく、前記壁部
の略全面に亘り分散して開設され、かつ前記外部加圧エ
ア供給手段に接続された多数の小孔からなる加圧エア噴
射口と、 前記燃焼室にごみを投入するためのごみ投入口とを有
し、 前記加圧エア供給手段から供給された加圧エアを前記加
圧エア噴射口から前記燃焼室内に向けて噴射しつつ該燃
焼室内のごみを燃焼させ、その燃焼熱をもって前記水管
内液を加熱することを特徴とするごみ焚きボイラ。
1. A wall portion which defines a combustion chamber and in which a large number of heat exchange water pipes are arranged, external pressurized air supply means, and the wall for injecting pressurized air toward the combustion chamber. And a dust injection port for injecting dust into the combustion chamber, which has a plurality of small holes connected to the external pressurized air supply means. And injecting the pressurized air supplied from the pressurized air supply means toward the combustion chamber from the pressurized air injection port, burns the dust in the combustion chamber, and heats the combustion to generate the water. A waste-fired boiler characterized by heating the liquid in the pipe.
【請求項2】 前記壁部が、多数の水管と各水管間に
設けられた吸熱フィンとを有し、 前記加圧エア噴射口が、前記吸熱フィンの略全面に亘り
分散して開設された多数の小孔からなることを特徴とす
る請求項1に記載のごみ焚きボイラ。
2. The wall portion has a large number of water pipes and heat-absorbing fins provided between the water pipes, and the pressurized air jet ports are opened over substantially the entire surface of the heat-absorbing fins. The refuse-fired boiler according to claim 1, comprising a plurality of small holes.
【請求項3】 前記壁部の外面を略覆うように、前記
壁部と該壁部を外囲する外壁との間に空室が画定され、 前記外部加圧エア供給手段が前記空室に接続され、 前記多数の小孔が前記空室と前記燃焼室とを連通するよ
うに前記内壁に開設され、 前記加圧エア供給手段から供給された加圧エアが前記空
室を介して前記加圧エア噴射口から前記燃焼室内に向け
て噴射されることを特徴とする請求項1若しくは請求項
2に記載のごみ焚きボイラ。
3. A vacant chamber is defined between the wall portion and an outer wall surrounding the wall portion so as to substantially cover the outer surface of the wall portion, and the external pressurized air supply means is provided in the vacant chamber. The plurality of small holes are connected to the inner wall so as to connect the chamber and the combustion chamber to each other, and pressurized air supplied from the pressurized air supply means is added to the chamber through the chamber. The refuse-fired boiler according to claim 1 or 2, wherein the compressed air is injected toward the combustion chamber from the injection port.
JP6065507A 1994-03-08 1994-03-08 Garbage boiler Expired - Lifetime JP2769289B2 (en)

Priority Applications (3)

Application Number Priority Date Filing Date Title
JP6065507A JP2769289B2 (en) 1994-03-08 1994-03-08 Garbage boiler
TW085206981U TW296772U (en) 1994-03-08 1994-09-23 Waste burning boiler
US08/315,712 US5590610A (en) 1994-03-08 1994-09-30 Waste burning boiler

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP6065507A JP2769289B2 (en) 1994-03-08 1994-03-08 Garbage boiler

Publications (2)

Publication Number Publication Date
JPH07243604A true JPH07243604A (en) 1995-09-19
JP2769289B2 JP2769289B2 (en) 1998-06-25

Family

ID=13289056

Family Applications (1)

Application Number Title Priority Date Filing Date
JP6065507A Expired - Lifetime JP2769289B2 (en) 1994-03-08 1994-03-08 Garbage boiler

Country Status (1)

Country Link
JP (1) JP2769289B2 (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN108458350A (en) * 2018-02-12 2018-08-28 蒯进永 A kind of garbage combustion device with waste gas purification function

Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH02259325A (en) * 1989-03-30 1990-10-22 Babu Hitachi Eng Service Kk Waste ignition device having boiler

Patent Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH02259325A (en) * 1989-03-30 1990-10-22 Babu Hitachi Eng Service Kk Waste ignition device having boiler

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN108458350A (en) * 2018-02-12 2018-08-28 蒯进永 A kind of garbage combustion device with waste gas purification function

Also Published As

Publication number Publication date
JP2769289B2 (en) 1998-06-25

Similar Documents

Publication Publication Date Title
CN2893437Y (en) Waste liquid and/or waste gas incinerator
US5590610A (en) Waste burning boiler
CN102042602B (en) Processing method and device for incinerating toxic waste liquid by smoke concentration and gasification
CN209165440U (en) A kind of rice husk burning device
JP2014524006A (en) Combustion device
JPH07243604A (en) Dust burning boiler
JPH07243603A (en) Dust burning boiler
JP3210859B2 (en) Secondary combustion gas supply mechanism of garbage incinerator
KR20010079051A (en) High pressure steam boiler
RU2133409C1 (en) Wood waste incinerator
KR100282670B1 (en) Boiler device using waste tire incineration heat
JP3850823B2 (en) Liquid heating device
US6332411B1 (en) Furnace
JPH0523938Y2 (en)
JPS59212616A (en) Generator for combustion heat of waste plastic, waste oil, etc.
CN218914898U (en) Water pipe type superheated steam boiler
CN210153754U (en) Firewood-burning steam generator
KR200184241Y1 (en) A water boiler
JPH0249465Y2 (en)
KR200244119Y1 (en) Waste incinerator
JP2002061808A (en) Burner for liquid fuel combustion device
JP2002267101A (en) Method for superheating steam in incinerator
KR100295291B1 (en) Incinerator of waste synthetic resin and industrial boiler of substitute fuel type using the same
JP2002048333A (en) High temperature gas emission equipment provided with heat absorption path
JPS6138309A (en) Combustion equipment