JPH0148308B2 - - Google Patents

Info

Publication number
JPH0148308B2
JPH0148308B2 JP56051667A JP5166781A JPH0148308B2 JP H0148308 B2 JPH0148308 B2 JP H0148308B2 JP 56051667 A JP56051667 A JP 56051667A JP 5166781 A JP5166781 A JP 5166781A JP H0148308 B2 JPH0148308 B2 JP H0148308B2
Authority
JP
Japan
Prior art keywords
chamber
funnel
combustion
fumigation
ventilation
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
JP56051667A
Other languages
Japanese (ja)
Other versions
JPS57167384A (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 JP56051667A priority Critical patent/JPS57167384A/en
Publication of JPS57167384A publication Critical patent/JPS57167384A/en
Publication of JPH0148308B2 publication Critical patent/JPH0148308B2/ja
Granted legal-status Critical Current

Links

Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J8/00Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes
    • B01J8/18Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with fluidised particles
    • B01J8/24Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with fluidised particles according to "fluidised-bed" technique
    • B01J8/44Fluidisation grids
    • 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

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  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Combustion & Propulsion (AREA)
  • Organic Chemistry (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • 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
粒状物を滞留させつつ(実際は徐々に移動してい
る)赤熱し、その際の燻蒸作用で可燃性ガスを取
り出し、これを燃焼させ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 remains in the fumigation chamber (in reality, it gradually moves) and becomes red hot. A granular combustion furnace is known that extracts flammable gas through fumigation and burns it.

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。
Further, a water-containing waste drying and incineration apparatus in which a central tower furnace and a leaning tower furnace are provided inside a cylindrical incinerator to form a cone-shaped grate is known as Japanese Patent Publication No. 45-8950.

さらに、炉本体の周壁下部に環状空室内を回転
する送入空気流をその流動方向に沿わせつつ燃焼
室に導入する送気孔を一定間隔毎に穿設した燃焼
炉が実公昭44−23501号公報として知られている。
Furthermore, a combustion furnace was published in Utility Model Publication No. 44-23501 in which air holes were drilled at regular intervals in the lower part of the peripheral wall of the furnace body to introduce the air flow rotating inside the annular cavity into the combustion chamber along the flow direction. It is known as a gazette.

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
外壁を構成する多孔板が孔を平板に直角に単に打
ち抜いているだけであるので、作動中に燻蒸室か
ら比較的多量の粒状物の微片や灰が送風室に落ち
易く、これらの落下物送風室内に徐々に貯留され
てきて、たびたび送風室の清掃をしないと、つい
には送風機能が阻害されて燃焼不調や一酸化炭素
等の有毒ガスの発生を見ることがある。
Problems to be Solved by the Invention However, in conventional granular combustion furnaces, the perforated plate constituting the outer wall of the fumigation chamber simply has holes punched out at right angles to the flat plate, so that relatively little air is removed from the fumigation chamber during operation. A large amount of granular particles and ash easily fall into the ventilation chamber, and these fallen objects gradually accumulate in the ventilation chamber, and if the ventilation chamber is not cleaned frequently, the ventilation function will be obstructed, resulting in poor combustion. Poisonous gases such as carbon monoxide may be generated.

また、特公昭45−8950号公報記載のものも、斜
塔炉が平板に噴射孔を単に抜ち抜いただけのもの
であつた。
In addition, the one described in Japanese Patent Publication No. 45-8950 was also one in which the leaning tower furnace was simply a flat plate with injection holes cut out.

さらに、実公昭44−23501号公報記載のものも、
炉本体が平板に送気孔を単に斜めに打ち抜いただ
けのものであつた。
Furthermore, those described in Utility Model Publication No. 44-23501,
The furnace body was simply a flat plate with air holes punched out diagonally.

本発明の目的は、上述する問題点に対処して、
下部漏斗体が平板に通孔を単に打ち抜いたもので
なく、通孔を膨出部の円周方向端部に形成するこ
とにより、燻蒸室内の粒状物の微片や灰が通孔か
ら送風室内に落ちることが少なく、送風室内の面
倒な清掃回数を減らし、送風室から燻蒸室への粒
状物の微片や灰による送風機能が阻害されること
がなく、燃焼不調や不完全燃焼ガスを含んだ熱風
の発生を防止す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 lower funnel is not simply a flat plate with holes punched out, but the holes are formed at the circumferential end of the bulge, allowing particles and ash in the fumigation chamber to flow through the holes into the ventilation chamber. It reduces the number of troublesome cleanings inside the ventilation chamber, prevents the ventilation function from being obstructed by particulate matter and ash from the ventilation chamber to the fumigation chamber, and eliminates combustion problems and incompletely combusted gas. An object of the present invention is to provide a granular combustion furnace capable of preventing the generation of hot air.

課題を解決するための手段 本発明の粒状物燃焼炉は、上部漏斗体の下部に
間隔を置いて下部漏斗体を設け、前記上部漏斗体
と前記下部漏斗体との間に粒状物の滞留する漏斗
状の燻蒸室を形成し、前記下部漏斗体の下部に前
記燻蒸室と連通する送風室を形成し、前記下部漏
斗体は円周方向一側に向かつて開口する多数の膨
出部を形成した多孔板よりなることを特徴とする
構成を有するものである。
Means for Solving the Problems In the granular material combustion furnace of the present invention, a lower funnel is provided at an interval below the upper funnel, and the granular material is retained between the upper funnel and the lower funnel. A funnel-shaped fumigation chamber is formed, a ventilation chamber communicating with the fumigation chamber is formed at the lower part of the lower funnel, and the lower funnel forms a number of bulges opening toward one side in the circumferential direction. It has a structure characterized by being made of a perforated plate.

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.

第1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 FIG. 1, 1 is a combustion furnace, and the combustion furnace 1
A machine room 3 is provided in the lower part of the combustion section 2.

燃焼部2の筒体の内部には上部漏斗体4が設け
られると共に、上部漏斗体4の下部には所定間隔
を置いて下部漏斗体5が設けられ、下部漏斗体5
の外部には環状送風路6が形成され、下部漏斗体
5の下方には多孔底板7が設けられている。
An upper funnel body 4 is provided inside the cylindrical body of the combustion section 2, and a lower funnel body 5 is provided at a predetermined interval below the upper funnel body 4.
An annular air passage 6 is formed on the outside of the funnel 5, and a perforated bottom plate 7 is provided below the lower funnel body 5.

上部漏斗体4は、その周縁を除いて多孔の板体
から形成され、第1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 upper funnel body 4 is formed of a porous plate except for its periphery, and as shown in FIG. 1, its center is recessed into a cylindrical shape, and its lower part is a conical part 8.

下部漏斗体5は、上部漏斗体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 lower funnel body 5 is disposed below the conical portion 8 of the upper funnel body 4 at a predetermined interval, and is formed from a conical perforated plate.

下部漏斗体5の上縁は環状送風路6の内側壁に
接しており、下部漏斗体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 lower funnel 5 is in contact with the inner wall of the annular air passage 6, and the lower end of the lower funnel 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、その周縁を環状送風路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内部の下部漏斗体5の下部には環状送
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、上部漏斗体4と下部漏斗体5との
間には送風室10と連通する漏斗状の燻蒸室11
が形成され、上部漏斗体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、上部漏斗体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 ventilation chamber 1 surrounded by an inner wall of an annular ventilation passage 6 and a perforated bottom plate 7 is provided at a lower part of the lower funnel body 5 inside the combustion section 2.
A funnel-shaped fumigation chamber 11 is formed between the upper funnel body 4 and the lower funnel body 5 and communicates with the ventilation chamber 10.
A primary combustion chamber 12 communicating with the fumigation chamber 11 is formed inside the cylindrical recessed part and conical part 8 of the upper funnel body 4, and a primary combustion chamber 12 communicating with the primary combustion chamber 12 is formed in the upper part of the upper funnel body 4. A secondary combustion chamber 13 is formed as a space in the combustion section 2, and the primary combustion chamber 12 communicates with the ventilation chamber 10 via the fumigation 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、燃焼部2の二次燃焼室1
3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 a buffer plate 15 is provided inside the secondary combustion chamber 13 of the combustion section 2.
An on-off valve 16 is provided on the upper wall facing 3 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、下部漏斗体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、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、送風機20の送風口は燃
焼部2の環状送風路6と送風室10の下部とに分
岐してそれぞれ接続されている。
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 lower funnel body 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, and a granular material supply chute 24 is provided near the bottom end of the pressure feed pipe 22. The air outlet of the blower 20 is connected to the annular air passage 6 of the combustion section 2 and the lower part of the air chamber 10, respectively.

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.

燃焼部2内部の燻蒸室11の外壁となる下部漏
斗体5は、第2図に示すように、多数の膨出部が
形成され、膨出部の円周方向端部には円周方向に
沿つて開口する通孔が形成された多孔板よりなつ
ている。
As shown in FIG. 2, the lower funnel body 5, which serves as the outer wall of the fumigation chamber 11 inside the combustion section 2, has a number of bulges formed therein, and the circumferential ends of the bulges have bulges extending in the circumferential direction. It is made of a perforated plate with through holes that open along its length.

この下部漏斗体5の通孔は、平板に単に打ち抜
かれたものではなく、平板に多数の切り込みを入
れた後、切り込みの片側周縁を外部より燻蒸室1
1側または送風室10側へくさび状あるいは半円
錘状に嵌入させて多数の膨出部を形成し、円周方
向一側に向かつて開口する通孔を形成している。
The holes in the lower funnel body 5 are not simply punched in a flat plate, but after making numerous cuts in the flat plate, one side of the periphery of the cuts is inserted into the fumigation chamber 1 from the outside.
1 side or the ventilation chamber 10 side in a wedge shape or a semicircular cone shape to form a large number of bulges, and a through hole that opens toward one side in the circumferential direction is formed.

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及び送風室10
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 are respectively driven, and the motor 21 rotates the spiral body 23, and the blower 20 rotates the annular air passage 6 and the air blower chamber 10.
blow air to.

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
状態の高温となり、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 granules that have risen to the top of the fumigation chamber 11 are 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, causing the granules inside the fumigation chamber 11 to become red-hot. is fumigated to liberate flammable gases.

この可燃性ガスは送風機20から送風室10を
経て燻蒸室11の外壁(下部漏斗体5の多数の通
孔)から入り、燻蒸室11の内壁(上部漏斗体4
の孔)を通過する空気と共に一次燃焼室12へ搬
送される。
This combustible gas enters from the blower 20 through the blow chamber 10, through the outer wall of the fumigation chamber 11 (numerous holes in the lower funnel 5), and enters through the inner wall of the fumigation chamber 11 (through the upper funnel 4).
It is conveyed to the primary combustion chamber 12 together with the air passing through the holes).

一次燃焼室12では、この可燃性ガスが送風機
20から送風室10、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 passes through the blower chamber 10 and the fumigation chamber 11 from the blower 20, obtains sufficient oxygen, burns most of it, and becomes hot air with the air flow, and is converted into a secondary combustion chamber. Enter 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.

二次燃焼室13内の熱風は通常時には、環状間
隔17上部の多孔箇所を経て熱風導出ダクト18
に至り、籾乾燥機や温室等に導かれる。
Under normal conditions, the hot air in the secondary combustion chamber 13 passes through the porous area in the upper part of the annular space 17 to the hot air outlet duct 18.
The paddy is then taken to dryers, 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.

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
に上方に移動する。
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. gradually move upwards.

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、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 on the perforated 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, guided to the cyclone 19, and 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、下部漏斗体が平板に通孔を単に打ち抜い
たものでなく、通孔が多数の膨出部の円周方向一
側に向かつて形成されているので、燻蒸室内の粒
状物の微片や灰が通孔から送風室内に落ちること
が少なく、送風室内の面倒な清掃回数を減らすこ
とができ、送風室から燻蒸室への粒状物の微片や
灰による送風機能が阻害されることがないので、
燃焼不調や不完全燃焼ガスを含んだ熱風の発生を
防止することができる。
Effects of the Invention As described above, according to the granular material combustion furnace of the present invention, the lower funnel is not simply formed by punching through holes in a flat plate, but the through holes are aligned in the circumferential direction of a large number of bulges. Since it is formed facing towards the side, it is less likely that particulate matter and ash in the fumigation chamber will fall into the ventilation chamber from the ventilation holes, reducing the number of troublesome cleanings inside the ventilation chamber. Since the ventilation function is not obstructed by particles or ash,
It is possible to prevent poor combustion and generation of hot air containing incomplete combustion gas.

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

第1図は、本発明の実施例の粒状物燃焼炉の縦
断面図、第2図は、第1図の下部漏斗体の要部拡
大斜視図である。 1…燃焼炉、2…燃焼部、3…機械室、4…上
部漏斗体、5…下部漏斗体、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。
FIG. 1 is a longitudinal cross-sectional view of a granular combustion furnace according to an embodiment of the present invention, and FIG. 2 is an enlarged perspective view of a main part of the lower funnel shown in FIG. DESCRIPTION OF SYMBOLS 1... Combustion furnace, 2... Combustion part, 3... Machine room, 4... Upper funnel, 5... Lower funnel, 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 feeding pipe, 23... Spiral body, 24... Granular material supply chute.

Claims (1)

【特許請求の範囲】[Claims] 1 上部漏斗体の下部に間隔を置いて下部漏斗体
を設け、前記上部漏斗体と前記下部漏斗体との間
に粒状物の滞留する漏斗状の燻蒸室を形成し、前
記下部漏斗体の下部に前記燻蒸室と連通する送風
室を形成し、前記下部漏斗体は円周方向一側に向
かつて開口する多数の膨出部を形成した多孔板よ
りなることを特徴とする粒状物燃焼炉。
1. A lower funnel is provided below the upper funnel at an interval, a funnel-shaped fumigation chamber in which particulate matter accumulates is formed between the upper funnel and the lower funnel, and the lower funnel A granular material combustion furnace characterized in that a blowing chamber communicating with the fumigation chamber is formed, and the lower funnel is made of a perforated plate having a large number of bulges opening toward one side in the circumferential direction.
JP56051667A 1981-04-08 1981-04-08 Granule burning oven Granted JPS57167384A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP56051667A JPS57167384A (en) 1981-04-08 1981-04-08 Granule burning oven

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP56051667A JPS57167384A (en) 1981-04-08 1981-04-08 Granule burning oven

Publications (2)

Publication Number Publication Date
JPS57167384A JPS57167384A (en) 1982-10-15
JPH0148308B2 true JPH0148308B2 (en) 1989-10-18

Family

ID=12893227

Family Applications (1)

Application Number Title Priority Date Filing Date
JP56051667A Granted JPS57167384A (en) 1981-04-08 1981-04-08 Granule burning oven

Country Status (1)

Country Link
JP (1) JPS57167384A (en)

Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS4423501Y1 (en) * 1967-04-03 1969-10-03

Patent Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS4423501Y1 (en) * 1967-04-03 1969-10-03

Also Published As

Publication number Publication date
JPS57167384A (en) 1982-10-15

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