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JPS6367082B2 - - Google Patents
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JPS6367082B2 - - Google Patents

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Publication number
JPS6367082B2
JPS6367082B2 JP55092631A JP9263180A JPS6367082B2 JP S6367082 B2 JPS6367082 B2 JP S6367082B2 JP 55092631 A JP55092631 A JP 55092631A JP 9263180 A JP9263180 A JP 9263180A JP S6367082 B2 JPS6367082 B2 JP S6367082B2
Authority
JP
Japan
Prior art keywords
combustion
pumping device
cylinder
particulate matter
annular
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
JP55092631A
Other languages
Japanese (ja)
Other versions
JPS5719504A (en
Inventor
Toshihiko Satake
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 JP9263180A priority Critical patent/JPS5719504A/en
Publication of JPS5719504A publication Critical patent/JPS5719504A/en
Publication of JPS6367082B2 publication Critical patent/JPS6367082B2/ja
Granted legal-status Critical Current

Links

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

Description

【発明の詳細な説明】 本発明は籾殻鋸屑等の粒状物を燃料とする燃焼
炉に関する。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a combustion furnace that uses granular materials such as rice husk sawdust as fuel.

その目的は、粒状物を自動かつ連続的に燃焼さ
せて、燃かすなど固体を含まない高温燃焼排気を
取り出すことのできる燃焼炉の提供と炉の形態を
コンパクトにすることにある。
The purpose is to provide a combustion furnace that can automatically and continuously burn particulate matter and extract high-temperature combustion exhaust that does not contain solids, and to make the furnace compact.

籾殻燐焼炉は種々のものが提案されており、第
1図に示す炉1a内への籾殻の供給を炉1aの底
部から上方へすなわち炉1aの縦軸に沿つて配置
された籾殻圧送装置イによつて行なうものでは、
この圧送装置イがその上端に当る籾殻燃焼部ロか
らの延焼を防止するため、圧送速度の関連からみ
ても相当長く設計しなければならず、結局、燃焼
炉の縦軸(高さ)が大きなものとなつてしまう。
Various types of rice husk phosphorizing furnaces have been proposed, including a rice husk pressure feeding device arranged upward from the bottom of the furnace 1a, that is, along the vertical axis of the furnace 1a, to supply the rice husks into the furnace 1a shown in FIG. What is done by A.
In order to prevent the spread of fire from the rice husk combustion part B, which is located at the upper end of this pressure feeding device A, it had to be designed to be quite long in terms of the pumping speed, and as a result, the vertical axis (height) of the combustion furnace was large. It becomes a thing.

そこで、本発明では特にこの燃焼炉の高さを減
少することに努力し、燃焼筒を環状にすること
と、これにその接線方向から粒状物圧送装置を接
続したことで成功したものである。
Therefore, in the present invention, we have made particular efforts to reduce the height of this combustion furnace, and succeeded by making the combustion cylinder annular and connecting a granular material pumping device to it from the tangential direction.

以下、図示の実施例に基いて本発明を説明す
る。
The present invention will be explained below based on illustrated embodiments.

第2図において、燃焼炉1は大略、全体として
有底円筒形の外筒2とこれの内部を上下に二分す
る環状板3および外筒内の配置された環状燃焼筒
4とからなる。そして、外筒2は頂部に燃焼排気
口5を開設し、前記環状板3より下部分の周壁に
は給気口6を備える。外筒2はまた、その内部の
上部が排塵口20を介して外筒2の周壁から接線
方向に突設された排塵管9に連通している。環状
板3は、第3図に示すように、均等に配置された
多数の孔10を有している。
In FIG. 2, the combustion furnace 1 generally consists of a bottomed cylindrical outer cylinder 2, an annular plate 3 that divides the interior of the outer cylinder into upper and lower halves, and an annular combustion cylinder 4 arranged inside the outer cylinder. The outer cylinder 2 has a combustion exhaust port 5 at the top, and an air supply port 6 in the peripheral wall below the annular plate 3. The upper part of the inside of the outer cylinder 2 also communicates with a dust exhaust pipe 9 that projects from the peripheral wall of the outer cylinder 2 in a tangential direction through a dust exhaust port 20 . The annular plate 3 has a large number of evenly spaced holes 10, as shown in FIG.

環状燃焼筒4は前記環状板3の中央に上部をこ
の板3の上方に、下部はこの板3の下方となるよ
う配置したもので、底部中央に給気筒11が突設
され、その周囲に環状で有底の燃料室12が形成
され、かつ、燃焼炉1の外部から外筒2を貫通し
たスクリユーコンベア等による粒状物圧送装置1
3が環状燃焼筒4の下部外周壁へその接線方向に
横に接続されている。
The annular combustion cylinder 4 is arranged in the center of the annular plate 3 so that the upper part is above this plate 3 and the lower part is below this plate 3. A granular material pumping device 1 is formed with an annular bottomed fuel chamber 12 and is provided with a screw conveyor or the like that penetrates an outer cylinder 2 from the outside of a combustion furnace 1.
3 is laterally connected to the lower outer circumferential wall of the annular combustion tube 4 in a tangential direction thereof.

給気筒11は底部が開口した円筒形で頂部壁1
4およびその周壁15に多数の孔16を備える。
The supply cylinder 11 has a cylindrical shape with an open bottom and a top wall 1.
4 and its peripheral wall 15 are provided with a large number of holes 16.

燃料室12内には、粒状物圧送装置13との接
続部を始点として上方へ緩く捻回するらせんに沿
つたらせん体17を一回転分備える。このらせん
体17は粒状物の上方への移動を助勢する案内板
であつて、前記らせんに沿つて一枚又は数枚を配
置する。
Inside the fuel chamber 12, a helical body 17 is provided for one rotation along a spiral that gently twists upward starting from the connection with the particulate matter pumping device 13. This spiral body 17 is a guide plate that assists the upward movement of the granules, and one or several pieces are arranged along the spiral.

そして、前記環状板3の孔10は、第4図に示
すように板面に直角に貫通するものではなく、空
気の噴出方向に水平成分Lが含まれ、この水平成
分Lの方向が燃焼炉内に一定方向に旋回する気流
を生じるように配置されている。
The holes 10 in the annular plate 3 do not penetrate perpendicularly to the plate surface as shown in FIG. It is arranged to create an airflow that swirls in a certain direction within the air.

なお、18は燃焼排気口5の直下に設けられた
除塵のための邪魔板、19,25は給気口6およ
び給気筒11の下部に設けられた風量調節用ダン
パーである。22は外筒2の側壁及び上壁の内側
に形成された冷却室で、給気口6及び燃焼排気口
5に連通し、給気口6から冷却空気を導入してこ
れを燃焼排気口5に排出する。
Note that 18 is a baffle plate for dust removal provided directly below the combustion exhaust port 5, and 19 and 25 are dampers for adjusting air volume provided at the lower portions of the air supply port 6 and the supply cylinder 11. 22 is a cooling chamber formed inside the side wall and top wall of the outer cylinder 2, which communicates with the air supply port 6 and the combustion exhaust port 5, introduces cooling air from the air supply port 6, and transfers it to the combustion exhaust port 5. to be discharged.

以上の構成において、今、粒状物圧送装置13
を駆動して籾殻等の粒状物を環状燃焼筒4に供給
すると籾殻は燃料室12内に充満する。ついで燃
料室12上部の籾殻に点火して給気口6より空気
を導入すると、空気は第2図に失視するように環
状板3で区分された外筒2の下部空間から環状燃
焼筒4の孔21及び籾殻間の空間を通つて燃焼室
24へ流れて籾殻を燃焼し、同時に給気筒11の
孔16より可燃成分を含んだガスを燃焼室24内
に送り込む。さらに空気は環状板3の孔10、給
気筒11の孔16を介して二次燃焼室24に抜け
るので、燃料室12上部で燃焼中の籾殻は燃焼に
よる軽量化と、高温化した周辺気体の上昇および
前記孔10から供給される空気の旋回成分を引き
起こす外筒2の二次燃焼室24内における旋回気
流に乗つて舞い上がり二次的に燃焼する。
In the above configuration, now the granular material pressure feeding device 13
When the fuel chamber 12 is driven to supply particulate matter such as rice husks to the annular combustion tube 4, the rice husks fill the fuel chamber 12. Next, when the rice husks in the upper part of the fuel chamber 12 are ignited and air is introduced from the air supply port 6, the air flows from the lower space of the outer cylinder 2 divided by the annular plate 3 into the annular combustion cylinder 4 as shown in FIG. The gas flows into the combustion chamber 24 through the holes 21 and the space between the rice husks and burns the rice husks, and at the same time, gas containing combustible components is sent into the combustion chamber 24 from the holes 16 of the feed cylinder 11. Furthermore, air escapes to the secondary combustion chamber 24 through the hole 10 in the annular plate 3 and the hole 16 in the feed cylinder 11, so that the rice husks being burned in the upper part of the fuel chamber 12 are reduced in weight by combustion, and the surrounding gas that has become high in temperature is The air rises up and rides the swirling airflow in the secondary combustion chamber 24 of the outer cylinder 2, which causes a swirling component of the air supplied from the holes 10, and is secondarily combusted.

粒状物圧送装置13を継続して作動すれば、燃
料室12内には下方より籾殻が供給されて上部で
の籾殻の燃焼が持続する。
If the granular material pumping device 13 continues to operate, rice husks are supplied into the fuel chamber 12 from below, and the combustion of the rice husks continues in the upper part.

さて、外筒2の上部空間で旋回する高温気体は
上部の排気口5から穀類の乾燥や温室の暖房等の
所定の目的のために取出されるが、それ以前に旋
回気流中の固形物(燃えかすなど)は遠心作用を
受けて外筒2内を旋回する間に排塵口20を通つ
て排気筒9から炉外に排出される。また、邪魔板
18は気流中の固形物が直接排気口5に飛び込む
のを防止する。
Now, the high temperature gas swirling in the upper space of the outer cylinder 2 is taken out from the upper exhaust port 5 for a predetermined purpose such as drying grains or heating a greenhouse, but before that, the solids in the swirling airflow ( Cinders, etc.) are discharged from the exhaust pipe 9 to the outside of the furnace through the dust exhaust port 20 while rotating inside the outer cylinder 2 due to centrifugal action. Further, the baffle plate 18 prevents solid matter in the airflow from directly jumping into the exhaust port 5.

以上の構成・作動であるから、本発明は次の作
用効果を有する。
With the above configuration and operation, the present invention has the following effects.

粒状物圧送装置を横に配置したから燃焼炉の
高さを低くでき、取扱いが便利である。
Since the granular material pumping device is placed on the side, the height of the combustion furnace can be reduced, making handling convenient.

燃焼筒を環状とし、これに粒状物圧送装置を
接線方向から偏心して接続し、燃焼筒の底面
を、粒状物圧送装置との接続部を下部として、
らせん状の上り勾配に形成したので、前記のよ
うに圧送装置を単に横に接続したものと異な
り、燃料が燃料室の側壁に押圧されて滞溜する
ようなことがなく、縦方向の移送機器を用いる
ことなくスムーズに上方に移動できる。
The combustion tube is annular, the particulate matter pumping device is connected eccentrically from the tangential direction, and the bottom surface of the combustion tube is set at the bottom of the connection part with the particulate matter pumping device,
Because it is formed in a spiral upward slope, unlike the case where the pumping device is simply connected horizontally as described above, the fuel is not pressed against the side wall of the fuel chamber and accumulates, and it is possible to use a vertical transfer device. You can move upwards smoothly without using the .

粒状物の連続燃焼が可能で、しかも固形物の
混らないきれいな排気を得ることができ、乾燥
機、温室等の熱源として経済的な燃焼炉を提供
できる。
It is possible to continuously burn particulate matter, and also to obtain clean exhaust gas that is not mixed with solid matter, and it is possible to provide an economical combustion furnace as a heat source for dryers, greenhouses, etc.

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

第1図は、先行の粒状物燃焼炉の概略断面図、
第2図は、本発明の実施例の縦断面図、第3図
は、第2図のA―A線に沿う断面図、第4図は、
同上の要部の斜視図。 1……燃焼炉、2……外筒、3……環状板、4
……環状燃焼筒、5……燃焼排気口、6……給気
口、9……排塵筒、10……孔、11……給気
筒、12……燃料室、13……粒状物圧送装置、
16……孔、18……邪魔板、20……排塵口、
21……孔。
Figure 1 is a schematic cross-sectional view of a previous granular combustion furnace;
FIG. 2 is a longitudinal sectional view of an embodiment of the present invention, FIG. 3 is a sectional view taken along line AA in FIG. 2, and FIG.
A perspective view of the main part same as the above. 1... Combustion furnace, 2... Outer cylinder, 3... Annular plate, 4
... Annular combustion tube, 5 ... Combustion exhaust port, 6 ... Air supply port, 9 ... Dust exhaust pipe, 10 ... Hole, 11 ... Supply cylinder, 12 ... Fuel chamber, 13 ... Particulate matter pumping Device,
16... hole, 18... baffle plate, 20... dust exhaust port,
21... hole.

Claims (1)

【特許請求の範囲】[Claims] 1 上部に燃焼排気口を備えると共に、下部に給
気口を備えた外筒内を多孔の環状板で上下に二分
し、底部が開口し周壁に多数の孔が備えられた給
気筒を、周囲に多数の孔が備えられた有底の燃焼
筒の中央に立設して両筒間に燃料室を形成すると
共に、これらを、前記環状板を貫通して配置し、
前記有底環状の燃焼筒の周壁下部には、その周壁
の接線に沿つて粒状物圧送装置を偏心して横に接
続し、前記燃焼筒の底面は、粒状物圧送装置との
接続部を始点として、前記給気筒の外周に沿つて
らせん状の上り勾配を有することを特徴とする粒
状物燃焼炉。
1 The inside of the outer cylinder, which has a combustion exhaust port at the top and an air supply port at the bottom, is divided into upper and lower halves by a perforated annular plate. erected in the center of a bottomed combustion cylinder provided with a large number of holes to form a fuel chamber between the two cylinders, and arranged through the annular plate;
A particulate matter pumping device is eccentrically connected laterally to the bottom of the peripheral wall of the bottomed annular combustion cylinder along a tangent to the peripheral wall, and the bottom surface of the combustion pipe is connected to the particulate matter pumping device starting from the connection point with the particulate matter pumping device. , A granular material combustion furnace characterized by having a spiral upward slope along the outer periphery of the feed cylinder.
JP9263180A 1980-07-09 1980-07-09 Granular material combustion furnace Granted JPS5719504A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP9263180A JPS5719504A (en) 1980-07-09 1980-07-09 Granular material combustion furnace

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP9263180A JPS5719504A (en) 1980-07-09 1980-07-09 Granular material combustion furnace

Publications (2)

Publication Number Publication Date
JPS5719504A JPS5719504A (en) 1982-02-01
JPS6367082B2 true JPS6367082B2 (en) 1988-12-23

Family

ID=14059783

Family Applications (1)

Application Number Title Priority Date Filing Date
JP9263180A Granted JPS5719504A (en) 1980-07-09 1980-07-09 Granular material combustion furnace

Country Status (1)

Country Link
JP (1) JPS5719504A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2017009240A (en) * 2015-06-25 2017-01-12 卓司 中尾 High temperature furnace and energy generation system using the same

Families Citing this family (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH032071Y2 (en) * 1986-09-26 1991-01-21
SE9701775L (en) * 1997-05-14 1998-11-15 Sven Lindberg Heating device
JP2018185141A (en) * 2018-07-25 2018-11-22 アナログシステム有限会社 Incinerator having secondary combustion furnace

Family Cites Families (1)

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

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2017009240A (en) * 2015-06-25 2017-01-12 卓司 中尾 High temperature furnace and energy generation system using the same

Also Published As

Publication number Publication date
JPS5719504A (en) 1982-02-01

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