JPS6260604B2 - - Google Patents
Info
- Publication number
- JPS6260604B2 JPS6260604B2 JP55118699A JP11869980A JPS6260604B2 JP S6260604 B2 JPS6260604 B2 JP S6260604B2 JP 55118699 A JP55118699 A JP 55118699A JP 11869980 A JP11869980 A JP 11869980A JP S6260604 B2 JPS6260604 B2 JP S6260604B2
- Authority
- JP
- Japan
- Prior art keywords
- combustion
- chamber
- furnace body
- air
- swirling airflow
- 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
- 238000002485 combustion reaction Methods 0.000 claims description 62
- 239000008187 granular material Substances 0.000 claims description 17
- 238000009423 ventilation Methods 0.000 claims description 10
- 230000014759 maintenance of location Effects 0.000 claims description 7
- 230000002093 peripheral effect Effects 0.000 claims description 7
- 241000209094 Oryza Species 0.000 description 4
- 235000007164 Oryza sativa Nutrition 0.000 description 4
- 230000000694 effects Effects 0.000 description 4
- 239000010903 husk Substances 0.000 description 4
- 235000009566 rice Nutrition 0.000 description 4
- 239000000428 dust Substances 0.000 description 3
- 239000002245 particle Substances 0.000 description 3
- 235000013339 cereals Nutrition 0.000 description 2
- 239000003818 cinder Substances 0.000 description 2
- 238000009792 diffusion process Methods 0.000 description 2
- 238000001035 drying Methods 0.000 description 2
- 230000000630 rising effect Effects 0.000 description 2
- 244000249914 Hemigraphis reptans Species 0.000 description 1
- 230000001174 ascending effect Effects 0.000 description 1
- 238000000926 separation method Methods 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
- 239000004071 soot Substances 0.000 description 1
- 239000002699 waste material Substances 0.000 description 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10B—DESTRUCTIVE DISTILLATION OF CARBONACEOUS MATERIALS FOR PRODUCTION OF GAS, COKE, TAR, OR SIMILAR MATERIALS
- C10B53/00—Destructive distillation, specially adapted for particular solid raw materials or solid raw materials in special form
- C10B53/02—Destructive distillation, specially adapted for particular solid raw materials or solid raw materials in special form of cellulose-containing material
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10B—DESTRUCTIVE DISTILLATION OF CARBONACEOUS MATERIALS FOR PRODUCTION OF GAS, COKE, TAR, OR SIMILAR MATERIALS
- C10B21/00—Heating of coke ovens with combustible gases
- C10B21/10—Regulating and controlling the combustion
- C10B21/18—Recirculating the flue gases
-
- 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
- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Combustion & Propulsion (AREA)
- Materials Engineering (AREA)
- Organic Chemistry (AREA)
- Solid-Fuel Combustion (AREA)
- Coke Industry (AREA)
- Carbon And Carbon Compounds (AREA)
Description
【発明の詳細な説明】
本発明は旋回流を利用して籾殻などの粒体物を
燃焼させる粒体物燃焼装置に関し、特に籾殻等の
粒体物を連続的に燃焼させると共に、燃焼室内に
おいて燃えかすをサイクロン効果によつて遠心分
離して自動的に除去し、穀類等の乾燥に利用でき
る固体の燃えかすを含まない高温燃焼排気を取出
すことができる粒体物燃焼装置に関する。DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a granular material combustion device that burns granular materials such as rice husks using swirling flow, and in particular, it continuously burns granular materials such as rice husks and burns granular materials such as rice husks in a combustion chamber. The present invention relates to a granular material combustion device that can automatically remove combustion residue by centrifuging it using a cyclone effect and extract high-temperature combustion exhaust that does not contain solid combustion residue and can be used for drying grains, etc.
本発明を実施例図について説明する。図中符号
1は内部に燃焼室2を構成する周壁で、該周壁1
の上部中央に燃焼排出口3を設けると共に、その
内部にじやま板4を装架し、燃焼室2の下部に環
状の旋回気流室5を設けて基台6上に一体的に載
設し、前記気流室5上部を燃焼室2の軸まわりの
方向成分をもつた多数の通孔を開口した通気壁面
7に形成し、該壁面7を前記燃焼室2の周壁1に
開設した燃えかす排出口8に連絡し、前記旋回気
流室5の内環筒部9に上部を開放したすり鉢状の
通気性炉体10を装設すると共に、該炉体10の
底部をスクリユーコンベアから成る粒体供給装置
11に連絡し、12はその他端側に設けた供給ホ
ツパーである。また通気性炉体10の内部中央に
多孔壁の未燃ガス燃焼筒13を粒体の燃焼通路1
4を介して吊架すると共に、該燃焼筒13の筒壁
と前記通気性炉体10の壁部を複数個の通気管1
5…によつて連結し、また通気性炉体10の周囲
に設けた空気滞留室16と前記気流室5とを切換
弁17を備えた送管18を介して送風装置19に
連結してある。また前記燃焼室2の燃焼排出口3
はその外周に風洞部20を介して燃焼排気筒21
を装着し、該排気筒21は排風機22を備えた排
風路23に接続され、該排風路23には前記燃焼
室2の周壁1に設けた燃えかす排出口8に連絡す
るサイクロンコレクター24の排気筒25が接続
してある。 The present invention will be explained with reference to embodiment figures. Reference numeral 1 in the figure indicates a peripheral wall that constitutes a combustion chamber 2 inside, and the peripheral wall 1
A combustion exhaust port 3 is provided at the center of the upper part of the combustion chamber 2, and a rainbow board 4 is installed inside the combustion chamber 2. An annular swirling airflow chamber 5 is provided at the bottom of the combustion chamber 2, and the combustion chamber 2 is integrally mounted on a base 6. , the upper part of the air flow chamber 5 is formed into a ventilation wall surface 7 having a large number of through holes having a directional component around the axis of the combustion chamber 2, and the wall surface 7 is formed in the peripheral wall 1 of the combustion chamber 2. A mortar-shaped ventilated furnace body 10 connected to the outlet 8 and having an open upper part is installed in the inner ring cylinder part 9 of the swirling air flow chamber 5, and the bottom part of the furnace body 10 is connected to a granular body consisting of a screw conveyor. It communicates with the supply device 11, and 12 is a supply hopper provided at the other end. In addition, an unburnt gas combustion tube 13 with a porous wall is installed in the center of the interior of the ventilated furnace body 10.
4, and the cylinder wall of the combustion tube 13 and the wall of the ventilation furnace body 10 are connected to a plurality of ventilation pipes 1.
5..., and the air retention chamber 16 provided around the ventilated furnace body 10 and the airflow chamber 5 are connected to a blower device 19 via a feed pipe 18 equipped with a switching valve 17. . Further, the combustion exhaust port 3 of the combustion chamber 2
A combustion exhaust pipe 21 is installed on its outer periphery via a wind tunnel section 20.
The exhaust pipe 21 is connected to an exhaust passage 23 equipped with an exhaust fan 22, and the exhaust passage 23 has a cyclone collector connected to the combustion residue outlet 8 provided on the peripheral wall 1 of the combustion chamber 2. 24 exhaust pipes 25 are connected.
26はサイクロンコレクターの集塵箱、27は
粒体供給装置を駆動する電動機、28は燃焼排気
筒の給気口、29は粒体供給装置11のスクリユ
ーコンベアの軸端部に装着した拡散翼、30は燃
焼排気筒21の上壁に設けた排気調節弁である。 26 is a dust collection box of the cyclone collector, 27 is an electric motor that drives the granule supply device, 28 is an air supply port of the combustion exhaust stack, and 29 is a diffusion blade attached to the shaft end of the screw conveyor of the granule supply device 11. , 30 are exhaust control valves provided on the upper wall of the combustion exhaust stack 21.
上述の構成であるから、通気性炉体10内の燃
焼通路14に適量の籾殻等の粒体が供給ホツパー
12から粒体供給装置11によつて送り込まれた
状態で、粒体が適宜な手段(図示省略)で着火さ
れる。粒体は引続いて粒体供給装置11によつて
燃焼通路14に供給される。また燃焼開始時は、
切換弁17によつて旋回気流室5側を閉塞するの
で、送風装置19から送風される空気(一次空
気)は、空気滞留室16を介して燃焼通路14に
供給されて通路内の粒体を赤火状に燃焼すると共
に、余剰の空気(未燃ガス)は未燃ガス燃焼筒1
3に流出し、筒内の未燃ガスは通気管15からの
一次空気の混入によつて燃焼する。前記燃焼通路
14内に充満した赤火状の粒体の上層部が周囲の
旋回気流室5の通気壁面7に雪崩状に流動するよ
うになると直ちに切換弁17を操作して旋回気流
室5側を開口する。旋回気流室5に送風される空
気(二次空気)は、その上部に設けた通気壁面7
の多数の通孔から燃焼室2の軸まわりの方向に噴
出して該壁面7上に流出した粒体を再燃焼すると
共に、燃焼により生じたすすや灰分等の燃えかす
は前記通孔から噴出する上昇旋回流により遠心分
離作用を受けて即ちサイクロン効果によつて周壁
1の壁面に押し付けられ、続いて燃えかす自体の
自重により落下しながら流動して燃えかす排出口
8から排出されサイクロンコレクター24に流入
して除塵される。また、前記未燃ガス燃焼筒13
に流出した未燃ガスは、該筒13の上方の燃焼室
2に上昇する間に、前記旋回流(二次空気)と合
流して再燃焼して高温の排ガスを発生する。した
がつて燃えかすが旋回流による遠心分離作用によ
り除去された燃焼室内の高温燃焼排気は、燃焼排
気筒21を介して所定の温室または穀物乾燥装置
等(図示省略)に送られて使用される。 With the above-described configuration, when an appropriate amount of granules such as rice husks are fed into the combustion passage 14 in the ventilated furnace body 10 from the supply hopper 12 by the granule supply device 11, the granules are fed by an appropriate means. (not shown) is ignited. The granules are subsequently supplied to the combustion channel 14 by means of a granule supply device 11 . Also, at the start of combustion,
Since the swirling airflow chamber 5 side is closed by the switching valve 17, the air (primary air) blown from the blower 19 is supplied to the combustion passage 14 via the air retention chamber 16 and removes particles in the passage. It burns like a red flame, and excess air (unburnt gas) is sent to the unburned gas combustion tube 1.
3, and the unburned gas in the cylinder is mixed with primary air from the vent pipe 15 and combusted. As soon as the upper part of the red flame-like particles filling the combustion passage 14 begins to flow like an avalanche onto the ventilation wall surface 7 of the surrounding swirling airflow chamber 5, the switching valve 17 is operated to move the swirling airflow chamber 5 side. Open. The air (secondary air) blown into the swirling airflow chamber 5 is passed through the ventilation wall surface 7 provided above.
The particles ejected from the numerous holes in the direction around the axis of the combustion chamber 2 and flowed onto the wall surface 7 are re-burned, and the embers such as soot and ash generated by the combustion are ejected from the holes. The ascending swirling flow causes the cinders to be centrifuged and pressed against the wall surface of the peripheral wall 1 by the cyclone effect, and then flow while falling due to their own weight and are discharged from the cinders discharge port 8 into the cyclone collector 24. The dust flows into the air and is removed. Further, the unburned gas combustion tube 13
While rising to the combustion chamber 2 above the cylinder 13, the unburned gas that has flowed out merges with the swirling flow (secondary air) and is re-burned to generate high-temperature exhaust gas. Therefore, the high-temperature combustion exhaust gas in the combustion chamber, from which the embers have been removed by the centrifugal action of the swirling flow, is sent to a predetermined greenhouse, grain drying device, etc. (not shown) via the combustion exhaust stack 21 for use.
以上の説明のように、本発明によると、すり鉢
状の通気性炉体10の側部外周に空気滞留室16
を設けると共に、前記炉体10の内部に粒体の燃
焼通路14を介して未燃ガス燃焼筒13を吊架し
たので、空気滞留室16からの一次空気は、余剰
空気を未燃ガス燃焼筒13に流出しその必要量の
みを路内の粒体に供給して常時温度斑のない安定
した燃焼を実施させることができ、また燃焼室2
の軸まわりの方向成分をもつた多数の通孔を開口
した通気壁面7を備えた環状の旋回気流室5の内
環筒部9にすり鉢状の通気性炉体10を装設した
ので、燃えかすが旋回流による遠心分離作用によ
つて自動的に排除できると共に、その上昇する旋
回流(二次空気)が燃焼室中央の未燃ガスと合流
して再燃焼し、高温の排ガスを発生して熱効率を
向上でき、また燃焼室2の燃焼排出口3に燃焼排
気筒21を設けたので、任意所定の温度および風
量等の調節を簡単に、かつ継続的に実施できると
共に、燃焼室の周壁の温度上昇を適宜に防止する
ことができる等の効果がある。 As described above, according to the present invention, the air retention chamber 16 is provided on the outer periphery of the side of the mortar-shaped ventilated furnace body 10.
At the same time, the unburnt gas combustion tube 13 is suspended inside the furnace body 10 via the granular combustion passage 14, so that the primary air from the air retention chamber 16 is used to direct excess air to the unburnt gas combustion tube. It is possible to supply only the necessary amount to the granules in the combustion chamber 13 and to perform stable combustion without temperature irregularities at all times.
Since the mortar-shaped ventilated furnace body 10 is installed in the inner ring cylinder part 9 of the annular swirling airflow chamber 5, which has a ventilation wall surface 7 with a large number of holes with a directional component around the axis of The waste can be automatically removed by the centrifugal separation effect of the swirling flow, and the rising swirling flow (secondary air) joins with the unburned gas in the center of the combustion chamber and re-burns, generating high-temperature exhaust gas. Thermal efficiency can be improved, and since the combustion exhaust pipe 21 is provided at the combustion exhaust port 3 of the combustion chamber 2, it is possible to easily and continuously adjust the temperature, air volume, etc. as desired. There are effects such as being able to appropriately prevent temperature rise.
図面は本発明の実施例図である。第1図は本装
置の側断面図、第2図はその要部を一部切開した
平面図である。
1…周壁、2…燃焼室、3…燃焼排出口、4…
じやま板、5…旋回気流室、6…基台、7…通気
壁面、8…燃えかす排出口、9…内環筒部、10
…通気性炉体、11…粒体供給装置、12…供給
ホツパー、13…未燃ガス燃焼筒、14…燃焼通
路、15…通気管、16…空気滞留室、17…切
換弁、18…送管、19…送風装置、20…風洞
部、21…燃焼排気筒、22…排風機、23…排
風路、24…サイクロンコレクター、25…排気
筒、26…集塵箱、27…電動機、28…給気
口、29…拡散翼、30…排気調節弁。
The drawings are illustrations of embodiments of the present invention. FIG. 1 is a side sectional view of the present device, and FIG. 2 is a partially cutaway plan view of the main part thereof. 1... Peripheral wall, 2... Combustion chamber, 3... Combustion exhaust port, 4...
Yama board, 5... swirling airflow chamber, 6... base, 7... ventilation wall surface, 8... ember discharge port, 9... inner ring cylinder part, 10
... Breathable furnace body, 11 ... Granular material supply device, 12 ... Supply hopper, 13 ... Unburnt gas combustion cylinder, 14 ... Combustion passage, 15 ... Ventilation pipe, 16 ... Air retention chamber, 17 ... Switching valve, 18 ... Sending Pipe, 19...Blower device, 20...Wind tunnel section, 21...Combustion exhaust stack, 22...Exhaust fan, 23...Exhaust channel, 24...Cyclone collector, 25...Exhaust stack, 26...Dust collection box, 27...Electric motor, 28 ...Air supply port, 29...Diffusion vane, 30...Exhaust control valve.
Claims (1)
状の旋回気流室を装設し、旋回気流室上部の通気
壁面を前記燃焼室の周壁に開設した燃かす排出口
に連絡すると共に、旋回気流室の内環筒部にすり
鉢状の通気性炉体を装設し、該炉体内部に粒体の
燃焼通路を介して未燃ガス燃焼筒を吊架すると共
に、該燃焼筒の筒壁と前記通気性炉体の壁部を複
数個の通気管で連結し、また前記炉体の底部に粒
体供給装置を連結すると共に、前記炉体の周囲に
空気滞留室を設け、該空気滞留室と前記旋回気流
室とを送風装置に連絡した粒体物燃焼装置。 2 前記燃焼室の燃焼排出口は燃焼排気筒を有し
ている特許請求の範囲第1項記載の粒体物燃焼装
置。[Scope of Claims] 1. A combustion exhaust port in which an annular swirling airflow chamber is installed in the lower part of a combustion chamber with a combustion exhaust port provided in the upper part, and a ventilation wall surface in the upper part of the swirling airflow chamber is provided in the peripheral wall of the combustion chamber. At the same time, a mortar-shaped ventilated furnace body is installed in the inner ring cylinder part of the swirling airflow chamber, and an unburned gas combustion cylinder is suspended inside the furnace body through a granular combustion passage. The cylindrical wall of the combustion tube and the wall of the air permeable furnace body are connected by a plurality of ventilation pipes, and a granule supply device is connected to the bottom of the furnace body, and an air retention chamber is provided around the furnace body. A granular material combustion device, wherein the air retention chamber and the swirling airflow chamber are connected to an air blower. 2. The granular material combustion device according to claim 1, wherein the combustion exhaust port of the combustion chamber has a combustion exhaust stack.
Priority Applications (12)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP55118699A JPS5743103A (en) | 1980-08-27 | 1980-08-27 | Combustion device for granular material |
| CH543581A CH657201B (en) | 1980-08-27 | 1981-08-24 | |
| US06/295,712 US4377116A (en) | 1980-08-27 | 1981-08-24 | Furnace for burning husk |
| AU74500/81A AU527606B2 (en) | 1980-08-27 | 1981-08-25 | Furnace |
| EG482/81A EG15114A (en) | 1980-08-27 | 1981-08-26 | Furnace for burning musk |
| GB8126035A GB2083184B (en) | 1980-08-27 | 1981-08-26 | Husk burning furnace |
| IT68151/81A IT1144641B (en) | 1980-08-27 | 1981-08-26 | OVEN FOR BURNING PULA AND OTHER GRANULAR FUELS |
| FR8116307A FR2496232B1 (en) | 1980-08-27 | 1981-08-26 | COMBUSTION OVEN FOR PLANT ENVELOPES |
| KR1019810003123A KR850000497B1 (en) | 1980-08-27 | 1981-08-26 | Chaff carbonization furnace |
| DE3133696A DE3133696C2 (en) | 1980-08-27 | 1981-08-26 | Oven for coking shells |
| PH26098A PH18021A (en) | 1980-08-27 | 1981-08-26 | Furnace for burning husk |
| MY702/85A MY8500702A (en) | 1980-08-27 | 1985-12-30 | Furnace for burning husk |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP55118699A JPS5743103A (en) | 1980-08-27 | 1980-08-27 | Combustion device for granular material |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS5743103A JPS5743103A (en) | 1982-03-11 |
| JPS6260604B2 true JPS6260604B2 (en) | 1987-12-17 |
Family
ID=14742952
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP55118699A Granted JPS5743103A (en) | 1980-08-27 | 1980-08-27 | Combustion device for granular material |
Country Status (2)
| Country | Link |
|---|---|
| JP (1) | JPS5743103A (en) |
| KR (1) | KR850000497B1 (en) |
Families Citing this family (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| KR20020046401A (en) * | 2000-12-14 | 2002-06-21 | 이호춘 | Boiler powered by chaff and sawdust |
| KR100602732B1 (en) * | 2005-04-25 | 2006-07-20 | 주식회사 대원지에스아이 | Vertical continuous rice husk carbonization machine |
-
1980
- 1980-08-27 JP JP55118699A patent/JPS5743103A/en active Granted
-
1981
- 1981-08-26 KR KR1019810003123A patent/KR850000497B1/en not_active Expired
Also Published As
| Publication number | Publication date |
|---|---|
| JPS5743103A (en) | 1982-03-11 |
| KR830006620A (en) | 1983-09-28 |
| KR850000497B1 (en) | 1985-04-11 |
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