Deprecated: The each() function is deprecated. This message will be suppressed on further calls in /home/zhenxiangba/zhenxiangba.com/public_html/phproxy-improved-master/index.php on line 456
JPH0148309B2 - - Google Patents
[go: Go Back, main page]

JPH0148309B2 - - Google Patents

Info

Publication number
JPH0148309B2
JPH0148309B2 JP56051668A JP5166881A JPH0148309B2 JP H0148309 B2 JPH0148309 B2 JP H0148309B2 JP 56051668 A JP56051668 A JP 56051668A JP 5166881 A JP5166881 A JP 5166881A JP H0148309 B2 JPH0148309 B2 JP H0148309B2
Authority
JP
Japan
Prior art keywords
chamber
combustion
porous wall
air
fumigation
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
Application number
JP56051668A
Other languages
Japanese (ja)
Other versions
JPS57167385A (en
Inventor
Yutaka Ikeda
Kyo Usui
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.)
Satake Engineering Co Ltd
Original Assignee
Satake Engineering Co Ltd
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 Satake Engineering Co Ltd filed Critical Satake Engineering Co Ltd
Priority to JP56051668A priority Critical patent/JPS57167385A/en
Publication of JPS57167385A publication Critical patent/JPS57167385A/en
Publication of JPH0148309B2 publication Critical patent/JPH0148309B2/ja
Granted legal-status Critical Current

Links

Classifications

    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02EREDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E50/00Technologies for the production of fuel of non-fossil origin
    • Y02E50/10Biofuels, e.g. bio-diesel

Landscapes

  • Solid-Fuel Combustion (AREA)
  • Gasification And Melting Of Waste (AREA)
  • Coke Industry (AREA)

Description

【発明の詳細な説明】 産業上の利用分野 本発明は、特に、籾殻、おがくず等の可燃性小
片よりなる粒状物を効率良く連続的に燃焼して、
その燃焼熱を熱風の形で取り出せるようにした粒
状物燃焼炉に関するものである。
DETAILED DESCRIPTION OF THE INVENTION Field of Industrial Application The present invention is particularly aimed at efficiently and continuously burning particulate matter consisting of small combustible pieces such as rice husks and sawdust.
This relates to a granular combustion furnace that can extract the combustion heat in the form of hot air.

従来の技術 従来より、内部に内・外壁共に多孔板からなる
燻蒸室を送風室上部に接続し、作業中は燻蒸室内
に粒状物を滞留させながら導入し、燻蒸室の粒状
物を送風室から空気流と共に赤熱し、その際の燻
蒸作用で粒状物が可燃性ガスを遊離し、可燃性ガ
スが空気流に乗つて一次燃焼室及び二次燃焼室で
燃焼し、その際の燃焼熱を送風機からの空気流に
伝えて熱風とする粒状物燃焼炉が知られている。
Conventional technology Conventionally, a fumigation chamber consisting of perforated plates on both the inner and outer walls is connected to the upper part of the ventilation chamber, and during work, particulate matter is introduced while remaining in the fumigation chamber, and the particulate matter in the fumigation chamber is removed from the ventilation chamber. It becomes red hot with the airflow, and the fumigation action at that time liberates flammable gas from the particulate matter, which combusts in the primary combustion chamber and secondary combustion chamber along with the airflow, and the combustion heat at that time is transferred to the blower. Particulate matter combustion furnaces are known in which hot air is generated by transferring the air flow from the

また、円筒状焼却炉の内部に中央塔炉および斜
塔炉を設けてコーン形火床を構成し、焼却炉の下
部に焚室を形成した含水廃物乾燥焼却装置が特公
昭45−8950号公報として知られている。
In addition, a water-containing waste drying and incinerator in which a central tower furnace and a leaning tower furnace are installed inside a cylindrical incinerator to form a cone-shaped fire bed, and a combustion chamber is formed in the lower part of the incinerator is disclosed in Japanese Patent Publication No. 45-8950. known as.

さらに、燃焼室内に燃焼器を具備し、燃焼器へ
フアンを介して空気を送風し、籾穀を燃焼器にス
クリユーコンベアで下から上へ送り込むようにし
た籾穀の焼却装置が特公昭45−8592号公報として
知られている。
Furthermore, a rice grain incineration device was developed in 1977, which was equipped with a combustor in the combustion chamber, blown air into the combustor through a fan, and fed the rice grains into the combustor from bottom to top using a screw conveyor. It is known as Publication No.-8592.

発明が解決しようとする課題 ところが、従来の粒状物燃焼炉では、燻蒸室の
外周多孔壁の周囲を取りまく送風室と送風室に対
して空気を送風する送風機との連通口が送風機側
に片寄り、しかも、送風室と送風機との連通口を
一箇所にすると、送風機からの空気流が送風室の
全域に均等に分散せず、燻蒸室内における粒状物
の燃焼が不均一となつていた。
Problems to be Solved by the Invention However, in conventional particulate matter combustion furnaces, the communication port between the ventilation chamber surrounding the outer peripheral porous wall of the fumigation chamber and the blower that blows air into the ventilation chamber is biased toward the blower side. Moreover, when the communication port between the blower chamber and the blower is placed in one place, the air flow from the blower is not evenly distributed over the entire area of the blower chamber, resulting in uneven combustion of particulate matter in the fumigation chamber.

燻蒸室内における粒状物の燃焼の不均一は、一
方で粒状物の異常燃焼による高温で燻蒸室に歪み
を与えたり、他方で粒状物の燃焼不良のために連
続運転を停止してしまうなどの不都合をもたらし
た。
Uneven combustion of particulate matter in the fumigation chamber causes inconveniences such as, on the one hand, distortion of the fumigation room due to high temperatures due to abnormal combustion of particulate matter, and on the other hand, continuous operation may be stopped due to poor combustion of particulate matter. brought about.

また、特公昭45−8950号公報記載のものは、火
炎或いは高温熱風が焚室内に充満し、これらが火
炎通孔を通つて中央塔炉および斜塔炉内の空隙に
順次充満し、中央塔炉および斜塔炉の噴射孔から
コーン形火床に火炎或いは高温熱風を噴射し、投
入口からコーン形火床内に落下する被焼却物を散
布器から噴出する二次空気により焼却するように
するものあつた。
In addition, in the method described in Japanese Patent Publication No. 45-8950, the flame or high-temperature hot air fills the combustion chamber, passes through the flame vent, sequentially fills the gaps in the central tower furnace and the leaning tower furnace, and the central tower Flame or high-temperature hot air is injected from the injection holes of the furnace and leaning tower furnace onto the cone-shaped grate, and the materials to be incinerated that fall into the cone-shaped grate from the inlet are incinerated by the secondary air ejected from the sprinkler. There was something to do.

さらに、特公昭45−8592号公報記載のものは、
送風がフアンを介した送風管から多数の分岐小管
を通じて燃焼器内へ導入されると共に、送風管よ
り燃焼器の上下位置から分岐管により送風するよ
うにしたものであつた。
Furthermore, what is described in Japanese Patent Publication No. 45-8592,
Air is introduced into the combustor from a blow pipe via a fan through a large number of branched small pipes, and is also blown from the blow pipe through the branch pipes from above and below the combustor.

本発明の目的は、上述する問題点に対処して、
空気貯留室内への送風機の送風により空気流の方
向性と運動力を失わせ、多孔板が空気貯留室から
送風室内への空気流に抵抗を与え、送風室から燻
蒸室への空気の供給を均等に分散させ、燻蒸室に
おける粒状物の燃焼を安定した状態で行え、燻蒸
室に粒状物の異常燃焼による歪みを与えることが
なく、連続運転を維持して熱風の熱量安定化を図
ることが可能な粒状物燃焼炉を提供することにあ
る。
It is an object of the present invention to address the above-mentioned problems and to
The blower blows air into the air storage chamber, causing the airflow to lose its direction and momentum, and the perforated plate provides resistance to the airflow from the air storage chamber to the ventilation chamber, thereby preventing the supply of air from the ventilation chamber to the fumigation chamber. By distributing the particles evenly, the combustion of particulates in the fumigation chamber can be performed in a stable state, and the fumigation chamber is not distorted by abnormal combustion of particulates, and continuous operation can be maintained to stabilize the amount of heat in the hot air. The object of the present invention is to provide a possible granular combustion furnace.

課題を解決するための手段 本発明の粒状物燃焼炉は、筒体の内部に内周多
孔壁を配設すると共に、前記内周多孔壁の下部に
間隔を置いて上方を大径にした円錘状の外周多孔
壁を設け、前記外周多孔壁の周囲に送風室を形成
し、前記内周多孔壁と前記外周多孔壁との間に前
記送風室と連通する燻蒸室を形成し、前記内周多
孔壁の内部に前記燻蒸室と連通する燃焼室を形成
し、前記送風室の底部に多孔板を設け、前記多孔
板の下部に前記送風室と連通する空気貯留室を設
け、前記空気貯留室に送風機を連絡したことを特
徴とする構成を有するものである。
Means for Solving the Problems The granular material combustion furnace of the present invention includes an inner peripheral porous wall disposed inside a cylindrical body, and a circle having a larger diameter on the upper side spaced apart from the lower part of the inner peripheral porous wall. A conical outer peripheral porous wall is provided, a ventilation chamber is formed around the outer peripheral porous wall, a fumigation chamber communicating with the ventilation chamber is formed between the inner peripheral porous wall and the outer peripheral porous wall, and a fumigation chamber is formed between the inner peripheral porous wall and the outer peripheral porous wall. A combustion chamber communicating with the fumigation chamber is formed inside the peripheral porous wall, a perforated plate is provided at the bottom of the ventilation chamber, an air storage chamber communicating with the ventilation chamber is provided at the bottom of the perforation plate, and the air storage The structure is characterized in that a blower is connected to the room.

実施例 以下、本発明の実施例を図面に基づいて詳細に
説明する。
Embodiments Hereinafter, embodiments of the present invention will be described in detail based on the drawings.

図において、1は燃焼炉であり、燃焼炉1の燃
焼部2の下部には機械室3が設けられている。
In the figure, 1 is a combustion furnace, and a machine room 3 is provided below a combustion section 2 of the combustion furnace 1.

燃焼部2の筒体の内部には内周多孔壁4が設け
られると共に、内周多孔壁4の下部には間隔を置
いて上方を大径にした外周多孔壁5が設けられ、
外周多孔壁5の外部には環状送風路6が形成さ
れ、外周多孔壁5の下方には抵抗板となる多孔底
板7が設けられている。
An inner peripheral porous wall 4 is provided inside the cylindrical body of the combustion section 2, and an outer peripheral porous wall 5 whose upper diameter is larger is provided at a lower part of the inner peripheral porous wall 4 at intervals,
An annular air passage 6 is formed outside the outer peripheral porous wall 5, and a porous bottom plate 7 serving as a resistance plate is provided below the outer peripheral porous wall 5.

内周多孔壁4は、その周縁を除いて多孔の板体
から形成され、図に示すように、その中央が筒状
に凹陥され、その下部が円錘部分8とされてい
る。
The inner peripheral porous wall 4 is formed of a porous plate except for its peripheral edge, and as shown in the figure, the center thereof is recessed into a cylindrical shape, and the lower part thereof is a conical portion 8.

外周多孔壁5は、内周多孔壁4の円錘部分8の
下部に所定間隔を置いて配置され、円錘形の多孔
板から形成されている。
The outer peripheral porous wall 5 is disposed below the conical portion 8 of the inner peripheral porous wall 4 at a predetermined interval, and is formed from a conical porous plate.

外周多孔壁5の上縁は、環状送風路6の内側壁
に接しており、外周多孔壁5の下端部は後述の圧
送管22に接続されている。
The upper edge of the outer peripheral porous wall 5 is in contact with the inner wall of the annular air blowing passage 6, and the lower end of the outer peripheral porous wall 5 is connected to a pressure feed pipe 22, which will be described later.

環状送風路6の上部には上板9が設けられ、上
板9は円周方向成分を有する孔をあけた多孔板か
ら形成されている。
An upper plate 9 is provided above the annular air passage 6, and the upper plate 9 is formed from a perforated plate having holes having a circumferential component.

多孔底板7は、その周縁が環状送風路6の内壁
に固着されている。
The peripheral edge of the porous bottom plate 7 is fixed to the inner wall of the annular air passage 6.

燃焼部2内部の外周多孔壁5の周囲には環状送
風路6の内壁と多孔底板7とで囲まれた送風室1
0が形成され、多孔底板7は送風室10の底部に
配置されている。
A ventilation chamber 1 surrounded by an inner wall of an annular ventilation passage 6 and a porous bottom plate 7 is provided around the outer peripheral porous wall 5 inside the combustion section 2.
0 is formed, and the porous bottom plate 7 is arranged at the bottom of the ventilation chamber 10.

内周多孔壁4と外周多孔壁5との間には送風室
10と連通する燻蒸室11が形成され、内周多孔
壁4の筒状凹陥部及び円錘部分8の内部には燻蒸
室11と連通する一次燃焼室12が形成され、内
周多孔壁4の上部には一次燃焼室12と連通する
燃焼部2の空間である二次燃焼室13がそれぞれ
形成され、一次燃焼室12は燻蒸室11を介して
送風室10と通じるようになつている。
A fumigation chamber 11 communicating with the ventilation chamber 10 is formed between the inner peripheral porous wall 4 and the outer peripheral porous wall 5, and the fumigation chamber 11 is provided inside the cylindrical recess and conical portion 8 of the inner peripheral porous wall 4. A primary combustion chamber 12 is formed in communication with the primary combustion chamber 12, and a secondary combustion chamber 13, which is a space in the combustion section 2 communicating with the primary combustion chamber 12, is formed in the upper part of the inner peripheral porous wall 4. It communicates with the ventilation chamber 10 via the chamber 11.

燃焼部2の二次燃焼室13の内部上方にはバツ
フア板15が設けられると共に、燃焼部2の二次
燃焼室13に臨む上壁には開閉弁16が開閉自在
に設けられている。
A buffer plate 15 is provided inside and above the secondary combustion chamber 13 of the combustion section 2, and an on-off valve 16 is provided on the upper wall of the combustion section 2 facing the secondary combustion chamber 13 so as to be openable and closable.

燃焼部2の側壁には上部を多孔とした環状隔壁
17を介して二次燃焼室13に連通する熱風導出
ダクト18が接続されると共に、熱風導出ダクト
18の下部には燻蒸室11に連通する除灰用のサ
イクロン19が接続されている。
A hot air outlet duct 18 communicating with the secondary combustion chamber 13 is connected to the side wall of the combustion section 2 via an annular partition wall 17 with a perforated upper part, and a lower part of the hot air outlet duct 18 communicates with the fumigation chamber 11. A cyclone 19 for ash removal is connected.

燃焼部2下部の機械室3の内部には送風室10
へ空気を送風する送風機20が設けられ、送風機
20の側部には内部に搬送用のらせん体23を備
えた圧送管22が設けられ、外周多孔壁5の下端
部には燻蒸室11に連通する圧送管22の上端部
が接続され、圧送管22の送風機20と反対の側
部にはらせん体23を駆動するモーター21が設
けられている。
There is a ventilation chamber 10 inside the machine room 3 at the bottom of the combustion section 2.
A blower 20 is provided for blowing air into the air, a pressure pipe 22 having a conveying spiral body 23 inside is provided on the side of the blower 20, and the lower end of the outer peripheral porous wall 5 communicates with the fumigation chamber 11. A motor 21 for driving a spiral body 23 is provided on the side of the pressure feed pipe 22 opposite to the blower 20 .

らせん体23の下端がベルト・プーリーを介し
てモーター21に連動連結されている。
The lower end of the spiral body 23 is operatively connected to the motor 21 via a belt pulley.

圧送管22の下端寄りには粒状物供給シユート
24が接続されている。
A particulate material supply chute 24 is connected near the lower end of the pressure feed pipe 22 .

多孔底板7の下部には送風室10と連通する空
気貯留室25が設けられ、空気貯留室25には送
風機20が連絡されている。
An air storage chamber 25 communicating with the ventilation chamber 10 is provided at the lower part of the porous bottom plate 7, and a blower 20 is connected to the air storage chamber 25.

送風室10は燻蒸室11の円錘状の外周多孔壁
5の外側を取り囲み、多孔底板7を底とした室で
あり、空気貯留室25はその多孔底板7を上壁と
した室であり、送風室10と連通して平たく形成
されている。
The ventilation chamber 10 is a chamber that surrounds the outside of the conical outer peripheral porous wall 5 of the fumigation chamber 11 and has the porous bottom plate 7 as the bottom wall, and the air storage chamber 25 is a chamber that has the porous bottom plate 7 as the top wall. It communicates with the ventilation chamber 10 and is formed flat.

送風機20の送風口は、燃焼部2の環状送風路
6と空気貯留室25とに分岐してそれぞれ接続さ
れている。
The air outlet of the blower 20 is branched and connected to the annular air passage 6 of the combustion section 2 and the air storage chamber 25, respectively.

次に、この実施例の作用について説明する。 Next, the operation of this embodiment will be explained.

まず、燃焼炉1の電源を投入すると、機械室3
内のモーター21及び送風機20がそれぞれ駆動
され、モーター21がらせん体23を回転すると
共に、送風機20が環状送風路6及び空気貯留室
25へと空気を送風する。
First, when the power to the combustion furnace 1 is turned on, the machine room 3
The motor 21 and the blower 20 inside are respectively driven, and the motor 21 rotates the spiral body 23, and the blower 20 blows air into the annular blowing passage 6 and the air storage chamber 25.

次いで、粒状物供給シユート24から粒状物を
供給すると、粒状物がらせん体23の回転に伴つ
て圧送管22内を上方に送られながら燻蒸室11
に充満する。
Next, when the granules are supplied from the granule supply chute 24, the granules are sent upward through the pressure feed pipe 22 and into the fumigation chamber 11 as the spiral body 23 rotates.
filled with.

そこで、燻蒸室11上部にせり上がつてきた粒
状物に点火すると、火はやがて燻蒸室11の全域
にわたり、燻蒸室11内のほぼ全域がやがて赤熱
状態となり、燻蒸室11内部の粒状物は燻蒸され
て可燃性ガスを遊離する。
Therefore, when the particulate matter that has risen to the top of the fumigation chamber 11 is ignited, the fire eventually spreads over the entire area of the fumigation chamber 11, and almost the entire area inside the fumigation chamber 11 becomes red hot, and the particulate matter inside the fumigation chamber 11 becomes fumigated. and liberate flammable gases.

この可燃性ガスは、図に矢印で示すように、送
風機20による空気流に乗つて一次燃焼室12に
入る。
This combustible gas enters the primary combustion chamber 12 on the air flow generated by the blower 20, as shown by the arrow in the figure.

一次燃焼室12では、この可燃性ガスが送風機
20から空気貯留室25、送風室10及び燻蒸室
11を通過して送られる充分な酸素を得て大部分
が燃焼し、空気流と共に熱風となつて二次燃焼室
13に入る。
In the primary combustion chamber 12, this combustible gas is sent from the blower 20 through the air storage chamber 25, the blowing chamber 10, and the fumigation chamber 11 to obtain sufficient oxygen, where most of it is combusted and becomes hot air with the air flow. and enters the secondary combustion chamber 13.

二次燃焼室13では、残余の未燃性ガスも完全
燃焼し、空気流は熱風となる。
In the secondary combustion chamber 13, the remaining unburned gas is also completely combusted, and the airflow becomes hot air.

可燃性ガスの燃焼熱は、送風機20からの空気
を熱して熱風となり、二次燃焼室13内の熱風は
通常時に環状隔壁17の上部の多孔部分を通つて
熱風導出ダクト18に至り、籾乾燥機や温室等に
送られる。
The combustion heat of the combustible gas heats the air from the blower 20 to become hot air, and the hot air in the secondary combustion chamber 13 normally passes through the porous part at the top of the annular partition wall 17 and reaches the hot air outlet duct 18, where it dries the paddy. They are sent to plants, greenhouses, etc.

燃焼部2の二次燃焼室13内の熱風の不用時等
は、開閉弁16を開けて熱風を燃焼炉1の外部へ
と逃がす。
When the hot air in the secondary combustion chamber 13 of the combustion section 2 is not used, the on-off valve 16 is opened to release the hot air to the outside of the combustion furnace 1.

ここで、送風機20からの送風は、まず、空気
貯留室25に入り、空気貯留室25から多孔底板
7を介して送風室10に入る。
Here, the air from the blower 20 first enters the air storage chamber 25, and from the air storage chamber 25 enters the air blowing chamber 10 via the porous bottom plate 7.

送風は空気貯留室25で、まず、その方向性と
運動力を失い、次いで、多孔底板7の多数の孔を
介して送風室10に静圧的に作用し、送風室10
の空気が外周多孔壁5の全域の孔から均等に燻蒸
室11に流入する。
The blowing air first loses its directionality and kinetic force in the air storage chamber 25, and then acts statically on the blower chamber 10 through the many holes of the porous bottom plate 7, and the blower chamber 10
The air flows uniformly into the fumigation chamber 11 from the holes throughout the entire area of the outer peripheral porous wall 5.

燻蒸室11は、粒状物供給シユート24から粒
状物が供給される限り、常時粒状物が滞留し、燻
蒸室11内の粒状物はらせん体23が送り込む新
しい粒状物によつて下方から押し上げられて徐々
に上方に移動しながら赤熱されて可燃性ガスを放
出して連続燃焼が行われる。
As long as particulate matter is supplied from the particulate supply chute 24, particulate matter remains in the fumigation chamber 11 at all times, and the particulate matter in the fumigation chamber 11 is pushed up from below by new particulate matter sent in by the spiral body 23. As it gradually moves upward, it becomes red hot and releases flammable gas, resulting in continuous combustion.

燻蒸室11の上部に到達した粒状物は可燃性ガ
スが遊離し尽くした灰となり、燻蒸室11内の粒
状物の灰は粒状物が下方からせり上るにつれて環
状送風路6の多孔の上板9に乗り、送風機20か
ら送られる環状送風路6の上板9から噴き出す旋
回風で搬送されてサイクロン19に導かれ、ここ
で空気と分離される。
The particulate matter that has reached the upper part of the fumigation chamber 11 becomes ash from which all combustible gases have been liberated, and the ashes of the particulate matter in the fumigation chamber 11 are disposed of in the porous upper plate 9 of the annular ventilation passage 6 as the particulate matter rises from below. The air is conveyed by the swirling wind blown from the upper plate 9 of the annular air passage 6 sent from the air blower 20 and guided to the cyclone 19, where it is separated from the air.

以上の燃焼過程が連続的に行われる。 The above combustion process is performed continuously.

このようにして、燻蒸室11内の粒状物は連続
的に効率良く燃焼され、その燃焼熱は熱風として
熱風導出ダクト18から取り出されて種々の目的
に有効に利用される。
In this way, the particulate matter in the fumigation chamber 11 is continuously and efficiently combusted, and the combustion heat is taken out as hot air from the hot air outlet duct 18 and effectively used for various purposes.

発明の効果 以上に述べたように、本発明の粒状物燃焼炉に
よれば、空気貯留室内への送風機の送風により空
気流の方向性と運動力を失わせると共に、多孔板
が空気貯留室から送風室内への空気流に抵抗を与
えるので、送風室から燻蒸室への空気の供給を均
等に分散させることができ、燻蒸室における粒状
物の燃焼を安定した状態で行え、燻蒸室に粒状物
の異常燃焼による歪みを与えることがなく、連続
運転を維持して熱風の熱量安定化を図ることがで
きる。
Effects of the Invention As described above, according to the particulate combustion furnace of the present invention, the directionality and kinetic force of the air flow are lost by the blower blowing into the air storage chamber, and the perforated plate removes the air from the air storage chamber. Since it provides resistance to the air flow into the ventilation chamber, the air supply from the ventilation chamber to the fumigation chamber can be evenly distributed, and the combustion of particulate matter in the fumigation chamber can be carried out in a stable state. It is possible to maintain continuous operation and stabilize the amount of heat in the hot air without causing distortion due to abnormal combustion.

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

図は、本発明の実施例の粒状物燃焼炉の縦断面
図である。 1…燃焼炉、2…燃焼部、3…機械室、4…内
周多孔壁、5…外周多孔壁、6…環状送風路、7
…多孔底板、8…円錘部分、9…上板、10…送
風室、11…燻蒸室、12…一次燃焼室、13…
二次燃焼室、15…バツフア板、16…開閉弁、
17…環状隔壁、18…熱風導出ダクト、19…
サイクロン、20…送風機、21…モーター、2
2…圧送管、23…らせん体、24…粒状物供給
シユート、25…空気貯留室。
The figure is a longitudinal sectional view of a granular material combustion furnace according to an embodiment of the present invention. DESCRIPTION OF SYMBOLS 1... Combustion furnace, 2... Combustion part, 3... Machine room, 4... Inner peripheral porous wall, 5... Outer peripheral porous wall, 6... Annular air duct, 7
... Porous bottom plate, 8... Conical portion, 9... Upper plate, 10... Blow chamber, 11... Fumigation chamber, 12... Primary combustion chamber, 13...
Secondary combustion chamber, 15... Buffer plate, 16... Open/close valve,
17... Annular partition wall, 18... Hot air outlet duct, 19...
Cyclone, 20...Blower, 21...Motor, 2
2... Pressure feed pipe, 23... Spiral body, 24... Granular material supply chute, 25... Air storage chamber.

Claims (1)

【特許請求の範囲】[Claims] 1 筒体の内部に内周多孔壁を配設すると共に、
前記内周多孔壁の下部に間隔を置いて上方を大径
にした円錘状の外周多孔壁を設け、前記外周多孔
壁の周囲に送風室を形成し、前記内周多孔壁と前
記外周多孔壁との間に前記送風室と連通する燻蒸
室を形成し、前記内周多孔壁の内部に前記燻蒸室
と連通する燃焼室を形成し、前記送風室の底部に
多孔板を設け、前記多孔板の下部に前記送風室と
連通する空気貯留室を設け、前記空気貯留室に送
風機を連絡したことを特徴とする粒状物燃焼炉。
1 In addition to disposing an inner peripheral porous wall inside the cylindrical body,
A conical outer porous wall having a larger diameter on the upper side is provided at a spaced interval below the inner porous wall, a ventilation chamber is formed around the outer porous wall, and the inner porous wall and the outer porous wall are connected to each other. A fumigation chamber communicating with the ventilation chamber is formed between the wall, a combustion chamber communicating with the fumigation chamber is formed inside the inner peripheral porous wall, a perforated plate is provided at the bottom of the ventilation chamber, and the porous A granular material combustion furnace characterized in that an air storage chamber communicating with the ventilation chamber is provided at a lower part of the plate, and a blower is connected to the air storage chamber.
JP56051668A 1981-04-08 1981-04-08 Granule burning oven Granted JPS57167385A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP56051668A JPS57167385A (en) 1981-04-08 1981-04-08 Granule burning oven

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP56051668A JPS57167385A (en) 1981-04-08 1981-04-08 Granule burning oven

Publications (2)

Publication Number Publication Date
JPS57167385A JPS57167385A (en) 1982-10-15
JPH0148309B2 true JPH0148309B2 (en) 1989-10-18

Family

ID=12893255

Family Applications (1)

Application Number Title Priority Date Filing Date
JP56051668A Granted JPS57167385A (en) 1981-04-08 1981-04-08 Granule burning oven

Country Status (1)

Country Link
JP (1) JPS57167385A (en)

Also Published As

Publication number Publication date
JPS57167385A (en) 1982-10-15

Similar Documents

Publication Publication Date Title
US4323018A (en) Method for generation of hot gas by incineration of combustile material and apparatus for generation of hot gas by incineration of combustible material
JP5009265B2 (en) Biomass fuel burner
US4856438A (en) Furnace
US4777889A (en) Fluidized bed mass burner for solid waste
RU2175421C1 (en) Furnace device
JP2008064370A (en) Woody pellet burning steam boiler
US4377117A (en) Particulate waste wood firing system
US3881870A (en) Effluent control apparatus
JPS6363801B2 (en)
JPH0148309B2 (en)
JPH06100325B2 (en) Air control of incinerator
CN217635659U (en) Smokeless garbage incinerator
GB2303201A (en) Refuse incinerator
JP2860875B2 (en) Two-stage hearth moving bed incinerator
JP2007322098A (en) Combustion waste heat facility
JPH0148308B2 (en)
US4377115A (en) Furnace for burning particulate wood waste material
JP2985058B2 (en) Two-stage swirling fluidized bed incinerator
RU2718384C1 (en) Heat generator furnace for burning wood wastes and heat generator
JPH0148310B2 (en)
JPH07310913A (en) Incinerator
JP4047996B2 (en) Rice husk incinerator
JPH0129410Y2 (en)
JPS6367082B2 (en)
JPH0116913Y2 (en)