JPH0148310B2 - - Google Patents
Info
- Publication number
- JPH0148310B2 JPH0148310B2 JP56051669A JP5166981A JPH0148310B2 JP H0148310 B2 JPH0148310 B2 JP H0148310B2 JP 56051669 A JP56051669 A JP 56051669A JP 5166981 A JP5166981 A JP 5166981A JP H0148310 B2 JPH0148310 B2 JP H0148310B2
- Authority
- JP
- Japan
- Prior art keywords
- porous wall
- inner peripheral
- combustion
- peripheral porous
- chamber
- 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
Links
- 230000002093 peripheral effect Effects 0.000 claims description 71
- 238000002485 combustion reaction Methods 0.000 claims description 69
- 238000003958 fumigation Methods 0.000 claims description 36
- 239000008187 granular material Substances 0.000 claims description 17
- 238000009423 ventilation Methods 0.000 claims description 10
- 239000013618 particulate matter Substances 0.000 description 24
- 239000007789 gas Substances 0.000 description 7
- 238000007664 blowing Methods 0.000 description 4
- 239000002956 ash Substances 0.000 description 3
- 239000011236 particulate material Substances 0.000 description 2
- 235000002918 Fraxinus excelsior Nutrition 0.000 description 1
- 240000007594 Oryza sativa Species 0.000 description 1
- 235000007164 Oryza sativa Nutrition 0.000 description 1
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 1
- 238000001035 drying Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 239000010903 husk Substances 0.000 description 1
- 238000002347 injection Methods 0.000 description 1
- 239000007924 injection Substances 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 239000001301 oxygen Substances 0.000 description 1
- 229910052760 oxygen Inorganic materials 0.000 description 1
- 235000009566 rice Nutrition 0.000 description 1
- 239000002699 waste material Substances 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 1
Classifications
-
- Y—GENERAL 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
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E50/00—Technologies for the production of fuel of non-fossil origin
- Y02E50/10—Biofuels, 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
従来の粒状物燃焼炉は、第1図に示すように、
燃焼筒bの内部に内周多孔壁aと外周多孔壁dと
からなる燻蒸室fを備え、燻蒸室fの内部で粒状
物を燻蒸して可燃性ガスを発生させるようになつ
ている。BACKGROUND TECHNOLOGY A conventional granule combustion furnace, as shown in Fig. 1,
A fumigation chamber f consisting of an inner peripheral porous wall a and an outer peripheral porous wall d is provided inside the combustion cylinder b, and particulate matter is fumigated inside the fumigation chamber f to generate combustible gas.
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.
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、内周多孔
壁aを燃焼筒bの内部に支持するに際し、内周多
孔壁aの内筒cと外周多孔壁dとの間に数本のス
テーeを溶着しているので、ステーeが燻蒸室f
の空間を横断して粒状物の移動を阻害し、内周多
孔壁aが燃焼筒bの内部から容易に取り外せず、
内周多孔壁a及び燻蒸室f内部の点検あるいは内
周多孔壁の交換が困難であつた。Problems to be Solved by the Invention However, in the conventional granular material combustion furnace, when supporting the inner peripheral porous wall a inside the combustion cylinder b, there is a gap between the inner peripheral porous wall a and the outer peripheral porous wall d. Several stays e are welded to the fumigation chamber f.
The inner peripheral porous wall a cannot be easily removed from the inside of the combustion tube b, and
It was difficult to inspect the inner peripheral porous wall a and the inside of the fumigation chamber f, or to replace the inner peripheral porous wall.
また、特公昭45−8950号公報記載のものもは、
中央塔炉および斜塔炉の噴射孔からコーン形火床
に火炎或に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焼却するもので
あつた。 In addition, those described in Japanese Patent Publication No. 45-8950 are
Flame or high-temperature hot air was injected from the injection holes of the central tower furnace and the leaning tower furnace into the cone-shaped grate, and the materials to be incinerated that fell into the cone-shaped grate from the inlet were incinerated.
本発明の目的は、上述する問題点に対処して、
粒状物搬送手段が粒状物を下方から燻蒸室内に送
込み、燻蒸室内の粒状物を粒状物搬送手段の送込
む新しい粒状物により下方から押し上げて上方に
移動し、燻蒸室にステーのような阻害物が全くな
く、燻蒸室内における粒状物の上方への移動がス
ムーズに行えて燻蒸室内部の粒状物の上昇の均一
性を確保し、内周多孔壁の取付部を燃焼筒の支持
体より取外せば、内周多孔壁を燃焼筒の外部に取
出せ、内周多孔壁及び燻蒸室の点検あるいは内周
多孔壁の交換を容易に行う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 granular material conveying means feeds the granular materials into the fumigation chamber from below, and the granular materials in the fumigation chamber are pushed up from below by the new granular materials fed by the granular material conveying means and moved upwards, creating an obstruction like a stay in the fumigation chamber. There are no objects at all, and the movement of particulates upwards in the fumigation chamber is smooth, ensuring uniformity in the rise of particulates inside the fumigation chamber, and the attachment part of the inner peripheral porous wall can be removed from the support of the combustion tube. It is an object of the present invention to provide a granular material combustion furnace in which the inner peripheral porous wall can be taken out to the outside of the combustion cylinder by removing it, and the inner peripheral porous wall and the fumigation chamber can be inspected or the inner peripheral porous wall can be easily replaced.
課題を解決するための手段
本発明の粒状物燃焼炉は、燃焼筒の内部に上方
を大径にした円錘形の外周多孔壁を配設すると共
に、この外周多孔壁の上方に所定間隔を置いてこ
れとは別体の内周多孔壁を配設し、この内周多孔
壁は中央を凹陥させて内筒を形成し、その上部周
縁には取付部を形成すると共にに下部には上方を
大径にした円錘形部を形成し、前記内周多孔壁の
周囲に送風室を形成し、前記外周多孔壁と前記内
周多孔壁の円錘形との間は燻蒸室とすると共に、
前記内周多孔壁の内部は燃焼室とし、前記燃焼筒
の内部に前記内周多孔壁の取付部を着脱自在に支
持する支持体を設け、前記外周多孔壁の下部に前
記燻蒸室と連通する粒状物搬送手段を設けたこと
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 a conical outer peripheral porous wall with a larger diameter at the top inside the combustion cylinder, and a predetermined interval above the outer peripheral porous wall. A separate inner peripheral porous wall is provided, and the inner peripheral porous wall is recessed in the center to form an inner cylinder, and a mounting part is formed on the upper peripheral edge of the inner cylinder, and an upper wall is formed on the lower part. A conical part having a large diameter is formed, a ventilation chamber is formed around the inner peripheral porous wall, and a space between the outer peripheral porous wall and the conical shape of the inner peripheral porous wall is used as a fumigation chamber. ,
The inside of the inner peripheral porous wall is a combustion chamber, a support body for removably supporting the attachment part of the inner peripheral porous wall is provided inside the combustion cylinder, and a lower part of the outer peripheral porous wall communicates with the fumigation chamber. The structure is characterized in that a particulate material conveying means is provided.
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2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. 2, 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の燃焼筒bの内部には上方を大径にし
た円錘形の外周多孔壁dが配設されると共に、外
周多孔壁dの上方には所定間隔を置いて外周多孔
壁dと別体の内周多孔壁aが配設され、外周多孔
壁dの外部には環状送風路4が形成され、外周多
孔壁dの下方には多孔底板5が設けられている。 Inside the combustion cylinder b of the combustion section 2, a conical outer porous wall d with a larger diameter at the top is disposed, and an outer porous wall d is provided at a predetermined interval above the outer porous wall d. A separate inner peripheral porous wall a is provided, an annular air passage 4 is formed outside the outer peripheral porous wall d, and a porous bottom plate 5 is provided below the outer peripheral porous wall d.
内周多孔壁aの中央には凹陥させた内筒cが設
けられ、内筒cの上部周縁には取付部としてフラ
ンジ6が一体に形成されると共に、内筒cの下部
には上方を大径にした円錘形部が一体の形成さ
れ、内周多孔壁aはフランジ6を除いて多孔の板
体から形成されている。 A recessed inner cylinder c is provided in the center of the inner peripheral porous wall a, and a flange 6 is integrally formed on the upper peripheral edge of the inner cylinder c as a mounting part, and a lower part of the inner cylinder c has a large upper part. A conical portion with a diameter is integrally formed, and the inner circumferential porous wall a is formed from a porous plate except for the flange 6.
外周多孔壁dの上縁は環状送風路4の内側壁に
接しており、外周多孔壁dの下部部は後述の圧送
管18に接続され、外周多孔壁dは円錘形の多孔
板から形成されている。 The upper edge of the outer peripheral porous wall d is in contact with the inner wall of the annular air blowing passage 4, the lower part of the outer peripheral porous wall d is connected to a pressure feed pipe 18, which will be described later, and the outer peripheral porous wall d is formed from a conical perforated plate. has been done.
外周多孔壁dは燃焼筒bに対して実質的に固定
されている。 The outer peripheral porous wall d is substantially fixed to the combustion tube b.
多孔底板5は、その周縁を環状送風路4の内壁
に固着されている。 The peripheral edge of the porous bottom plate 5 is fixed to the inner wall of the annular air passage 4.
燃焼筒b内部の外周多孔壁dの周囲には環状送
風路4の内壁と多孔底板5とで囲まれた送風室7
が形成されると共に、内周多孔壁aの円錘形部と
外周多孔壁dとの間には送風室7と連通する燻蒸
室fが形成され、内周多孔壁aの内筒c及び円錘
形部の内部には燻蒸室fと連通する一次燃焼室9
が形成され、内周多孔壁aの上方空間には一次燃
焼室9と連通する二次燃焼室10が形成され、一
次燃焼室9は燻蒸室fを介して送風室7と通じる
ようになつている。 A ventilation chamber 7 surrounded by the inner wall of the annular ventilation passage 4 and the porous bottom plate 5 is located around the outer peripheral porous wall d inside the combustion cylinder b.
is formed, and a fumigation chamber f communicating with the ventilation chamber 7 is formed between the conical part of the inner peripheral porous wall a and the outer peripheral porous wall d, and the inner cylinder c of the inner peripheral porous wall a and the circular A primary combustion chamber 9 communicating with the fumigation chamber f is provided inside the conical part.
A secondary combustion chamber 10 communicating with the primary combustion chamber 9 is formed in the space above the inner peripheral porous wall a, and the primary combustion chamber 9 communicates with the ventilation chamber 7 via the fumigation chamber f. There is.
環状送風路4の上部には上板11が設けられ、
上板11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 11 is provided at the top of the annular air passage 4,
The upper plate 11 is formed from a perforated plate with holes having a circumferential component.
燃焼筒bの側壁には燻蒸室fに連通する除灰用
のサイクロン12が接続されると共に、サイクロ
ン12の上部には二次燃焼室10に連通する熱風
導出ダクト13が接続されてる。 A ash removal cyclone 12 communicating with the fumigation chamber f is connected to the side wall of the combustion tube b, and a hot air outlet duct 13 communicating with the secondary combustion chamber 10 is connected to the upper part of the cyclone 12.
燃焼部bの内周面には内周多孔壁aのフランジ
6を着脱自在に支持する環状の支持体14が突出
して設けられ、内周多孔壁aのフランジ6は燃焼
筒bの支持体14に対してボルト等により固定さ
れている。 An annular support 14 that removably supports the flange 6 of the inner porous wall a is protruded from the inner circumferential surface of the combustion part b, and the flange 6 of the inner porous wall a is attached to the support 14 of the combustion tube b. It is fixed with bolts etc.
燃焼筒bの上部には上蓋15が着脱自在に設け
られ、燃焼筒bの開口上端が上蓋15により閉塞
されている。 A top cover 15 is removably provided on the top of the combustion tube b, and the top end of the opening of the combustion tube b is closed by the top cover 15.
燃焼部2下部の機械室3の内部には送風室7へ
空気を送風する送風機16が設けられ、送風機1
6の側部には内部に搬送用のらせん体19を備え
た粒状物搬送手段となる圧送管18が設けられ、
外周多孔壁dの下端部には燻蒸室fに連通する圧
送管18の上端部が接続され、圧送管18の送風
機16と反対の側部にはらせん体19を駆動する
モーター17が設けられ、らせん体19の下端が
ベルト・プーリーを介してモーター17に連動連
結されている。 A blower 16 for blowing air to the blower chamber 7 is provided inside the machine room 3 at the bottom of the combustion section 2.
A pressure feeding pipe 18, which serves as a granular material conveying means and is equipped with a conveying spiral body 19 inside, is provided on the side of 6.
The upper end of a pressure feed pipe 18 communicating with the fumigation chamber f is connected to the lower end of the outer peripheral porous wall d, and a motor 17 for driving a spiral body 19 is provided on the side of the pressure feed pipe 18 opposite to the blower 16. The lower end of the spiral body 19 is operatively connected to the motor 17 via a belt pulley.
圧送管18の下端寄りには粒状物供給シユート
20が接続されている。 A particulate material supply chute 20 is connected near the lower end of the pressure feed pipe 18 .
送風機16の送風口は燃焼部2の環状送風路4
と送風部7の下部とに分岐してそれぞれ接続され
ている。 The air outlet of the blower 16 is connected to the annular air passage 4 of the combustion section 2.
and the lower part of the ventilation section 7, which are branched and connected to each other.
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17及び送風機16がそれぞれ駆動
され、モーター17がらせん体19を回転すると
共に、送風機16が環状送風路4及び送風室7へ
と空気を送る。 First, when the power to the combustion furnace 1 is turned on, the machine room 3
The motor 17 and the blower 16 inside are respectively driven, and the motor 17 rotates the spiral body 19, and the blower 16 sends air to the annular air passage 4 and the air blowing chamber 7.
次いで、粒状物供給シユート20から粒状物を
供給すると、粒状物がらせん体19の回転に伴つ
て圧送管18内を上方に送られながら燻蒸室fに
充満する。 Next, when the particulate matter is supplied from the particulate matter supply chute 20, the particulate matter is sent upward through the pressure feed pipe 18 as the spiral body 19 rotates, and the fumigation chamber f is filled with the particulate matter.
そこで、燻蒸室f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fの全域にわ
たり、燻蒸室f内のほぼ全域がやがて高温状態と
なり、燻蒸室f内部の粒状物は燻蒸されて可燃性
ガスを放出する。 Therefore, when the particulate matter that has risen to the top of the fumigation chamber f is ignited, the fire eventually spreads over the entire area of the fumigation chamber f, and almost the entire area inside the fumigation chamber f becomes high temperature, and the particulate matter inside the fumigation chamber f is and releases flammable gases.
この可燃性ガスは、第2図の図面矢印で示すよ
うに、送風機16による空気流に乗つて一次燃焼
室9に入る。 This combustible gas enters the primary combustion chamber 9 on the air flow generated by the blower 16, as shown by arrows in FIG.
一次燃焼室9では、この可燃性ガスが送風機1
6から送風室7、燻蒸室f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10に入る。 In the primary combustion chamber 9, this flammable gas is transferred to the blower 1.
6, passing through the blowing chamber 7 and fumigation chamber f, most of the oxygen is combusted, and enters the secondary combustion chamber 10 as hot air along with the air flow.
二次燃焼室10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 10, 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16からの空気
を熱して熱風となり、二次燃焼室10から熱風導
出ダクト13入つて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 16 to become hot air, which enters the hot air outlet duct 13 from the secondary combustion chamber 10 and is sent to a paddy dryer, a greenhouse, etc.
燻蒸室fは、粒状物供給シユート20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f内の粒状物はらせん体19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 20, particulate matter remains in the fumigation chamber f, and the particulate matter in the fumigation chamber f is pushed up from below by new particulate matter sent in by the spiral body 19. gradually move upwards.
燻蒸室f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f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4の多孔の上板11に乗り、送風機16か
ら送られる環状送風路4の上板11から噴き出す
旋回風で搬送されてサイクロン12に導かれ、こ
こで空気と分離される。 The particulate matter that reaches the upper part of the fumigation chamber f becomes ash from which all combustible gases have been liberated, and the ashes of the particulate matter in the fumigation chamber f are distributed over the porous upper plate of the annular ventilation passage 4 as the particulate matter rises from below. 11, and is carried by the swirling wind blown from the upper plate 11 of the annular air passage 4 sent from the blower 16 and guided to the cyclone 12, 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f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13から取り出された種々の日的に
有効に利用される。 In this way, the particulate matter in the fumigation chamber f is continuously and efficiently combusted, and the combustion heat is effectively utilized in various ways as hot air taken out from the hot air outlet duct 13.
また、燃焼筒bの上部より上蓋15を取外し、
次いで、内周多孔壁aのフランジ6と燃焼筒bの
支持体14とを固定するボルトを螺脱することに
より、内周多孔壁aのフランジ6を燃焼筒bの支
持体14から取外した後、内周多孔壁aを燃焼筒
bの開口上端から外部に取出せば、内周多孔壁a
及び燃焼筒b内部の点検あるいは内周多孔壁aの
交換が行える。 Also, remove the upper cover 15 from the upper part of the combustion cylinder b,
Next, the flange 6 of the inner peripheral porous wall a is removed from the support 14 of the combustion cylinder b by unscrewing the bolts that fix the flange 6 of the inner peripheral porous wall a and the support 14 of the combustion cylinder b. , if the inner peripheral porous wall a is taken out from the upper end of the opening of the combustion cylinder b, the inner peripheral porous wall a
It is also possible to inspect the inside of the combustion cylinder b or replace the inner peripheral porous wall a.
さらに、内周多孔壁a及び燃焼筒b内部の点検
あるいは内周多孔壁aの交換が終了したら、内周
多孔壁aを燃焼筒bの開口上端より燃焼筒bの内
部に嵌挿し、内周多孔壁aのフランジ6を燃焼筒
bの支持体14に乗せた後、内周多孔壁aのフラ
ンジ6と燃焼筒bの支持体14とをボルトにより
固定する。 Furthermore, after inspecting the inside of the inner peripheral porous wall a and the combustion tube b or replacing the inner peripheral porous wall a, insert the inner peripheral porous wall a into the combustion tube b from the upper end of the opening of the combustion tube b, and After the flange 6 of the porous wall a is placed on the support 14 of the combustion tube b, the flange 6 of the inner peripheral porous wall a and the support 14 of the combustion tube b are fixed with bolts.
第3図は本発明の他の実施例を示すものであ
り、内周多孔壁aのフランジ6に間隔を置いて複
数の係止孔を設け、内周多孔壁aのフランジ6が
係止孔を利用して燃焼筒bの支持体14にバヨネ
ツト結合により着脱自在に固定されるようになつ
ている。 FIG. 3 shows another embodiment of the present invention, in which a plurality of locking holes are provided at intervals in the flange 6 of the inner peripheral porous wall a, and the flange 6 of the inner peripheral porous wall a is provided with a plurality of locking holes. It is designed to be removably fixed to the support body 14 of the combustion tube b by bayonet connection.
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、粒状物搬送手段が粒状物を下方から燻蒸
室内に送込むので、燻蒸室内の粒状物を粒状物搬
送手段によつて送込まれる新しい粒状物により下
方から押し上げて上方に移動することができ、燻
蒸室にステーのような阻害物が全くないので、燻
蒸室内における粒状物の上方への移動がスムーズ
に行え、燻蒸室内部の粒状物の上昇の均一性を確
保することができ、また、このような燃焼炉にあ
つては内周多孔壁が粒状物との摩擦や高温によつ
て損傷を受けやすいが、内周多孔壁の取付部を燃
焼筒の支持体より取外せば、内周多孔壁を燃焼筒
の外部に取出せるので、内周多孔壁及び燻蒸室の
点検あるいは内周多孔壁の交換を容昇に行うこと
ができる。Effects of the Invention As described above, according to the particulate matter combustion furnace of the present invention, the particulate matter conveying means sends the particulate matter into the fumigation chamber from below, so that the particulate matter in the fumigation chamber is transported by the particulate matter conveying means. The new granules brought in can be pushed up from below and moved upwards, and since there are no obstructions such as stays in the fumigation chamber, the granules can be moved upwards smoothly in the fumigation chamber. It is possible to ensure the uniformity of the rise of particulate matter inside the chamber, and in the case of such combustion furnaces, the inner peripheral porous wall is easily damaged by friction with particulate matter and high temperature. By removing the attachment part of the peripheral porous wall from the support of the combustion tube, the inner peripheral porous wall can be taken out to the outside of the combustion tube, making it easier to inspect the inner peripheral porous wall and the fumigation chamber or to replace the inner peripheral porous wall. can be done.
第1図は、従来の粒状物燃焼炉の概略縦断面
図、第2図は、本発明の実施例の粒状物燃焼炉の
縦断面図、第3図は、本発明の他の実施例の内周
多孔壁の平面図である。
1…燃焼炉、2…燃焼部、3…機械室、4…環
状送風路、5…多孔底板、6…フランジ、7…送
風室、9…一次燃焼室、10…二次燃焼室、11
…上板、12…サイクロン、13…熱風導出ダク
ト、14…支持体、15…上蓋、16…送風機、
17…モーター、18…圧送管、19…らせん
体、20…粒状物供給シユート、a…内周多孔
壁、b…燃焼筒、c…内筒、d…外周多孔壁、e
…ステー、f…燻蒸室。
FIG. 1 is a schematic vertical cross-sectional view of a conventional granular material combustion furnace, FIG. 2 is a vertical sectional view of a granular material combustion furnace according to an embodiment of the present invention, and FIG. 3 is a schematic longitudinal sectional view of a conventional granular material combustion furnace. FIG. 3 is a plan view of an inner peripheral porous wall. DESCRIPTION OF SYMBOLS 1... Combustion furnace, 2... Combustion part, 3... Machine room, 4... Annular ventilation path, 5... Porous bottom plate, 6... Flange, 7... Ventilation chamber, 9... Primary combustion chamber, 10... Secondary combustion chamber, 11
...Top plate, 12...Cyclone, 13...Hot air outlet duct, 14...Support, 15...Top lid, 16...Blower,
17...Motor, 18...Pressure pipe, 19...Spiral body, 20...Particulate matter supply chute, a...Inner peripheral porous wall, b...Combustion cylinder, c...Inner cylinder, d...Outer peripheral porous wall, e
...stay, f...fumigation chamber.
Claims (1)
周多孔壁を配設すると共に、この外周多孔壁の上
方に所定間隔を置いてこれとは別体の内周多孔壁
を配設し、この内周多孔壁は中央を凹陥させて内
筒を形成し、その上部周縁には取付部を形成する
と共に下部には上方を大径にした円錘形部を形成
し、前記外周多孔壁の周囲に送風室を形成し、前
記外周多孔壁と前記内周多孔壁の円錘形との間は
燻蒸室とすると共に、前記内周多孔壁の内部は燃
焼室とし、前記燃焼筒の内部に前記内周多孔壁の
取付部を着脱自在に支持する支持体を設け、前記
外周多孔壁の下部に前記燻蒸室と連通する粒状物
搬送手段を設けたことを特徴とする粒状物燃焼
炉。1 A conical outer peripheral porous wall with a larger diameter at the top is provided inside the combustion cylinder, and a separate inner peripheral porous wall is provided above this outer peripheral porous wall at a predetermined interval. This inner peripheral porous wall is recessed in the center to form an inner cylinder, the upper peripheral edge of which is formed with a mounting part, the lower part of which is formed with a conical part with a larger diameter at the top, and the outer peripheral porous wall A ventilation chamber is formed around the wall, a fumigation chamber is formed between the outer peripheral porous wall and the conical shape of the inner peripheral porous wall, and a combustion chamber is formed inside the inner peripheral porous wall, and a combustion chamber is formed between the outer peripheral porous wall and the conical shape of the inner peripheral porous wall. A granular material combustion furnace, characterized in that a support body for removably supporting a mounting portion of the inner peripheral porous wall is provided therein, and a granular material conveying means communicating with the fumigation chamber is provided at a lower part of the outer peripheral porous wall. .
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP56051669A JPS57167386A (en) | 1981-04-08 | 1981-04-08 | Granule burning oven |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP56051669A JPS57167386A (en) | 1981-04-08 | 1981-04-08 | Granule burning oven |
Publications (2)
Publication Number | Publication Date |
---|---|
JPS57167386A JPS57167386A (en) | 1982-10-15 |
JPH0148310B2 true JPH0148310B2 (en) | 1989-10-18 |
Family
ID=12893281
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP56051669A Granted JPS57167386A (en) | 1981-04-08 | 1981-04-08 | Granule burning oven |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS57167386A (en) |
-
1981
- 1981-04-08 JP JP56051669A patent/JPS57167386A/en active Granted
Also Published As
Publication number | Publication date |
---|---|
JPS57167386A (en) | 1982-10-15 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
WO1998048219A1 (en) | Solid fuel burner for a heating apparatus | |
US4836115A (en) | Vertical furnace | |
US3566809A (en) | Incinerator for waste material | |
US2725950A (en) | Centrifuge furnace | |
US4147115A (en) | Incinerator with gas generation | |
US3645218A (en) | Solid waste incinerator | |
JPS6119307Y2 (en) | ||
JP3151271U (en) | Dry biofuel powder combustion furnace | |
JP2007322098A (en) | Combustion waste heat utilizing facility | |
JPH0148310B2 (en) | ||
US4699070A (en) | Secondary grate for rotary combustor | |
CN210219785U (en) | Garbage incinerator | |
WO2011161724A1 (en) | Continuous combustion device for solid fuel | |
JP2860875B2 (en) | Two-stage hearth moving bed incinerator | |
CN107120654B (en) | Sanitary garbage disposal method | |
CN218599733U (en) | Industrial waste burns mechanism and industrial waste system of burning | |
JP2985058B2 (en) | Two-stage swirling fluidized bed incinerator | |
RU2718384C1 (en) | Heat generator furnace for burning wood wastes and heat generator | |
JPH0148309B2 (en) | ||
JPH0148308B2 (en) | ||
JPWO2010150523A1 (en) | Organic sludge treatment equipment | |
JPS6367082B2 (en) | ||
JPH0129410Y2 (en) | ||
RU2110014C1 (en) | Furnace-boiler for burning waste wood | |
SU1451462A1 (en) | Furnace for burning up waste |