JPH0145522B2 - - Google Patents

Info

Publication number
JPH0145522B2
JPH0145522B2 JP2326482A JP2326482A JPH0145522B2 JP H0145522 B2 JPH0145522 B2 JP H0145522B2 JP 2326482 A JP2326482 A JP 2326482A JP 2326482 A JP2326482 A JP 2326482A JP H0145522 B2 JPH0145522 B2 JP H0145522B2
Authority
JP
Japan
Prior art keywords
cylindrical
wood
storage tank
air supply
swash plates
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
JP2326482A
Other languages
Japanese (ja)
Other versions
JPS58140502A (en
Inventor
Saburo Katayose
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.)
Individual
Original Assignee
Individual
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 Individual filed Critical Individual
Priority to JP2326482A priority Critical patent/JPS58140502A/en
Publication of JPS58140502A publication Critical patent/JPS58140502A/en
Publication of JPH0145522B2 publication Critical patent/JPH0145522B2/ja
Granted legal-status Critical Current

Links

Classifications

    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23BMETHODS OR APPARATUS FOR COMBUSTION USING ONLY SOLID FUEL
    • F23B90/00Combustion methods not related to a particular type of apparatus
    • F23B90/04Combustion methods not related to a particular type of apparatus including secondary combustion
    • F23B90/06Combustion methods not related to a particular type of apparatus including secondary combustion the primary combustion being a gasification or pyrolysis in a reductive atmosphere

Landscapes

  • Engineering & Computer Science (AREA)
  • Physics & Mathematics (AREA)
  • Chemical & Material Sciences (AREA)
  • Combustion & Propulsion (AREA)
  • Thermal Sciences (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Solid-Fuel Combustion (AREA)
  • Gasification And Melting Of Waste (AREA)

Description

【発明の詳細な説明】 本発明は木質系粉粒状物類を燃料とする熱風発
生装置に関するものである。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a hot air generator using wood-based powder and granules as fuel.

石油資源の枯渇に伴う高油価対策として、代替
エネルギーへの転換がさかんになりつつあり、そ
の代替エネルギーのひとつとして未利用木質資源
が注目を集めている。この未利用木質資源には樹
皮(バーク)、チツプ、製材屑、おが屑、モミ殻、
麦わら、間伐材、廃船、建設廃材や木製廃家具等
の廃木材などがあり、有効発熱量が4500〜
5000Kcalとからなり高く、資源が豊富で入手が
容易かつ安価であり、かつ硫黄分などが少なく公
害を起しにくいことなどのメリツトがあるため、
燃料化の機運が高まつている。
As a countermeasure to high oil prices due to the depletion of petroleum resources, a shift to alternative energy is gaining momentum, and unused wood resources are attracting attention as one of these alternative energies. This unused wood resource includes bark, chips, sawdust, sawdust, rice husks,
Waste wood such as wheat straw, thinned wood, scrapped ships, construction waste, and waste wood furniture, etc., has an effective calorific value of 4500~
It has the merits of being 5000 Kcal, abundant in resources, easy to obtain, and inexpensive, and low in sulfur and less likely to cause pollution.
There is growing momentum to turn it into a fuel.

しかし、この種木質資源は、一般に吸湿性から
表面および組織中に水分を多量に含んだ状態のも
のが多いこと、形状が粉粒状および小片状である
ため、目詰りによる自己消火が生じやすく従つ
て、一括投入による処理が難いこと、さらに残灰
による目詰りによつて自己消火が生じやすいこと
などから、この種木質系廃棄物を簡単にしかも効
率よく燃焼してエネルギーを取出すことのできる
機器がないという問題があつた。
However, this type of wood resource is generally hygroscopic and often contains a large amount of water on its surface and in its structure, and because it is powder-like or small-sized, it is prone to self-extinguishing due to clogging. Therefore, since it is difficult to process by bulk input, and self-extinguishment is likely to occur due to clogging with residual ash, it is possible to easily and efficiently burn this type of wood waste to extract energy. There was a problem of not having the equipment.

この対策として、空気の流れをよくするためお
よび灰の目詰りを防止するため、樹皮や製材屑、
間伐材などをいつたん完全乾燥し粉砕した上で所
定形状のペレツトに加工し、燃料とする方法も検
討されているが、乾燥、高圧高温成形などの煩雑
な工程とかなり大掛りの設備を要するためコスト
が高くなり、実用性に乏しいという不具合があつ
た。
As a countermeasure for this, to improve air flow and prevent clogging of ash, bark, sawmill waste,
A method of using thinned wood, etc., as fuel after completely drying it, pulverizing it, and processing it into pellets of a specific shape is also being considered, but this requires complicated processes such as drying and high-pressure, high-temperature molding, and fairly large-scale equipment. This resulted in high costs and poor practicality.

本発明は前記のような事情から研究を重ねて創
案されたもので、その基本的な目的は、水分を多
量に含む各種木質系廃棄物類をことさらペレツト
化処理する要なく単に一括投入するだけでこれを
安定して連続的に燃焼させ、クリーンエネルギー
として供給することのできる構造簡単な熱風発生
装置を提供することにある。
The present invention was devised after repeated research in view of the above-mentioned circumstances, and its basic purpose is to simply input all types of wood waste containing a large amount of water in one batch without having to process it into pellets. The object of the present invention is to provide a hot air generator with a simple structure that can stably and continuously burn this hot air and supply it as clean energy.

また本発明の他の目的とするところは、原料中
の水分を蒸気として直接取出し、これを利用して
燃焼効率を高めると共に一括投入された資料量の
低減時に一時的に発生する大量の未燃ガスを外部
に放出することなく円滑に完全燃焼させることの
できる上記熱風発生装置を提供することにある。
Another object of the present invention is to directly extract the moisture in the raw materials as steam, and use this to increase combustion efficiency, as well as to create a large amount of unburned material that is temporarily generated when the amount of materials input at once is reduced. It is an object of the present invention to provide the above-mentioned hot air generator capable of smoothly and completely burning gas without releasing it to the outside.

この目的を達成するため本発明は基本的に内熱
乾留によるガス化−ガス燃焼方式を採用し、しか
も粉粒状形態という燃料特性に基因する炭化物や
灰分の機器への目詰りおよび燃焼エア供給の不十
分さによる黒煙や未燃ガスの臭気などの不安定現
象の発生を内燃部の特殊構造により解決し、さら
に、この構造と貯槽内の特殊構造との組合せによ
り、含水資料から生ずる水分の有効利用と、作業
終了時における未燃ガスによる黒煙発生防止を図
るようにしたものである。
In order to achieve this objective, the present invention basically adopts a gasification-gas combustion method using internal heat carbonization, and furthermore, it prevents clogging of equipment due to carbide and ash due to the fuel characteristics of powdery form, and reduces the supply of combustion air. The special structure of the internal combustion section solves the occurrence of unstable phenomena such as black smoke and the odor of unburned gas due to insufficient heat, and the combination of this structure and the special structure inside the storage tank eliminates moisture generated from water-containing materials. This is to ensure effective utilization and to prevent the generation of black smoke due to unburned gas at the end of work.

すなわち、本発明は灰取出口を有する下槽に資
料投入口を有する貯槽を重設し、この貯槽と下槽
との境界域に、全周にわたり斜板を間隔的に張設
してなる円筒形ロストルを回転可能に配すと共
に、この円筒形ロストル側方にエア供給部を設
け、木質系粉粒状物を静止状態の円筒形ロストル
の斜板を介して堆積させつつ円筒形ロストルおよ
びその周辺からの輻射熱で順次乾燥、ガス化さ
せ、乾留ガスをエア供給部からの供給エアと共に
斜板を介して蓄熱高温化した円筒形ロストル内に
流入させることにより完全なガス燃焼を行つて熱
分解せしめ、かつ適宜円筒形ロストルを回転させ
ることにより灰分の除去と未燃分の撹拌移動を行
うようにしたことを特徴とするものである。
That is, the present invention provides a cylindrical structure in which a storage tank having a material input port is superimposed on a lower tank having an ash removal port, and swash plates are stretched at intervals over the entire circumference in the boundary area between the storage tank and the lower tank. In addition to rotatably disposing the cylindrical rostol, an air supply section is provided on the side of the cylindrical rostol, and wood powder and granules are deposited through the swash plate of the cylindrical rostol in a stationary state. The carbonized gas is sequentially dried and gasified using radiant heat from the air supply section, and the carbonized gas is flowed through a swash plate into a cylindrical rostrum where heat is stored and heated to a high temperature, resulting in complete gas combustion and thermal decomposition. The present invention is characterized in that the ash content is removed and the unburned content is stirred and transferred by appropriately rotating the cylindrical rooster.

また本発明は上記構成に加え、貯槽内に下端開
孔が円筒形ロストルに指向する気送パイプを設
け、この気送パイプの上半部ことに貯槽の乾燥ゾ
ーンに対応する部分に蒸気吸引孔を形成し、乾燥
ゾーンで資料から発生した蒸気を蒸気吸引孔から
送気パイプに集めつつ下降中に昇温させ、円筒形
ロストル内で残留ガスと混合燃焼せしめるように
し、さらに貯槽内の資料源少時には、未燃ガスを
集気してグウンドラフト方式にて円筒形ロストル
内に送り込み完全燃焼させるようにしたことをも
特徴とする。
In addition to the above configuration, the present invention also provides a pneumatic pipe in which the opening at the lower end is directed toward the cylindrical rostrum in the storage tank, and a steam suction hole is provided in the upper half of the pneumatic pipe, in a portion corresponding to the drying zone of the storage tank. The steam generated from the material in the drying zone is collected from the steam suction hole into the air supply pipe and raised in temperature during the descent, mixed with residual gas in the cylindrical rostre and burned, and the material source in the storage tank is Another feature is that when the gas is low, the unburned gas is collected and sent into the cylindrical rostre using a ground draft method for complete combustion.

以下本発明を添付図面に示すものについて説明
する。
The present invention will now be described with reference to the accompanying drawings.

第1図ないし第5図は本発明に係る木質系粉粒
状物を燃料とする熱風発生装置の一例を示すもの
で、1は外面を水冷ジヤケツト6により囲続した
下槽であり、ベース7により地上に設置されるよ
うになつていると共に、一側には熱風取出し管8
が連設され、栽培、養魚、室内暖房などの必要部
位へと接続されるようになつている。また下槽1
の他側には灰取出口9が形成され、この灰取出口
9にはのぞき窓11を有する開閉扉10が取付け
られている。
1 to 5 show an example of a hot air generator using wood-based powder or granules as fuel according to the present invention. Reference numeral 1 denotes a lower tank whose outer surface is surrounded by a water cooling jacket 6, and a base 7. It is designed to be installed on the ground, and there is a hot air outlet pipe 8 on one side.
are installed in series and connected to necessary areas such as cultivation, fish farming, and indoor heating. Also, lower tank 1
An ash outlet 9 is formed on the other side, and an opening/closing door 10 having a viewing window 11 is attached to the ash outlet 9.

2は前記下槽1に対して重設された筒状の貯槽
であり、上部には投入口13を有する蓋体12が
取付けられており、底部は下槽1の天井部に形成
した開口14を介して下槽内部15と連通してい
る。この貯槽2は資料の収容と乾燥および乾留の
ための部材である。
Reference numeral 2 denotes a cylindrical storage tank installed over the lower tank 1. A lid body 12 having an input port 13 is attached to the upper part, and an opening 14 formed in the ceiling of the lower tank 1 is attached to the bottom part. It communicates with the inside of the lower tank 15 via. This storage tank 2 is a member for storing, drying, and carbonizing materials.

3は本発明で特徴とする円筒形ロストルであ
り、対向する一対の端板16,16とそれら端板
16,16の間に長手方向両端を連結した多数の
斜板17と、端板16,16を介して中心を貫通
する支軸18とからなつている。前記各斜板16
は図示のごとく垂直方向又は水平方向の中心線に
対し所定の傾斜角α(一般に30〜50゜)を持たされ
ており、全体として第5図のごとく羽根車状をな
し、垂直から見た状態において常に前方の斜板に
後方の斜板が重合するように板幅と間隔を設定し
ている。
Reference numeral 3 designates a cylindrical rotor that is a feature of the present invention, and includes a pair of opposing end plates 16, 16, a number of swash plates 17 whose longitudinal ends are connected between the end plates 16, 16, and the end plates 16, 16. It consists of a support shaft 18 passing through the center via a support shaft 16. Each of the swash plates 16
has a predetermined inclination angle α (generally 30 to 50°) with respect to the center line in the vertical or horizontal direction as shown in the figure, and as a whole, it has an impeller shape as shown in Figure 5, when viewed from the vertical direction. The plate width and spacing are set so that the rear swash plate always overlaps the front swash plate.

このような円筒形ロストル3は前記貯槽2と下
槽1の境界域に内装されると共に当該部分に外設
した軸受19,19に支軸18を挿通することに
より、中空状に支承され、支軸18の端部に設け
たハンドル20又は図示しないモータやシリンダ
の如き駆動源により適宜回転自在となつており、
斜板17,17の間は気体成分の流路21が、ま
た斜板17で囲まれた中空部分は蓄熱ガス燃焼室
22が構成される。
Such a cylindrical rotor 3 is supported in a hollow shape by inserting a support shaft 18 into bearings 19, 19 installed internally in the boundary area between the storage tank 2 and the lower tank 1 and provided externally in the area. It can be rotated as appropriate by a handle 20 provided at the end of the shaft 18 or by a drive source such as a motor or cylinder (not shown).
A gas component flow path 21 is formed between the swash plates 17, and a heat storage gas combustion chamber 22 is formed in the hollow portion surrounded by the swash plate 17.

前記の支軸18は中実に構成してもよいが、好
ましくは中空状に構成しエアや水などの流体を導
通させるようにすべきであり、さらにより好まし
くは第4図および第5図のように、端板16,1
6間の軸部分に噴孔33を形成すると共に、支軸
18の一端をエア供給源に接続し、操業中この噴
孔からエア類を噴出させて燃焼室内のガス燃焼を
促進させるようにするものである。こうすれば支
軸18の空冷もあわせて達成される。
Although the support shaft 18 may be solid, it is preferably hollow so that fluids such as air and water can be conducted therethrough, and even more preferably as shown in FIGS. 4 and 5. As shown, the end plate 16,1
A nozzle hole 33 is formed in the shaft portion between 6 and one end of the support shaft 18 is connected to an air supply source, and air is jetted from this nozzle hole during operation to promote gas combustion in the combustion chamber. It is something. In this way, air cooling of the support shaft 18 is also achieved.

4は内熱部分のエア供給部で、軸線方向が前記
円筒形ロストル3に指向するごとくこれの近傍位
置、すなわち円筒形ロストル3の上半部側の貯槽
部分に挿設固定されており、その供給口23は水
平に対し約30のごとき所要の角度βをもつて形成
され、背部の取入口24には供給量調整用の可動
シヤツタ25が取付けられている。
Reference numeral 4 denotes an air supply section for the internal heating section, which is inserted and fixed in the vicinity of the cylindrical rooster 3, that is, in the storage tank part on the upper half side of the cylindrical rooster 3, so that its axial direction is directed toward the cylindrical rooster 3. The supply port 23 is formed at a required angle .beta. of about 30 degrees with respect to the horizontal, and a movable shutter 25 for adjusting the supply amount is attached to the intake port 24 on the back.

5は下槽1の上面又は下槽1の外方に設置され
た熱交換手段であり、一部をもつて下槽1又は熱
風取出管8と接続され、内部に水管26が間隔的
に形成されると共に、上側には排気筒27が設け
られている。そして前記水管26の一部に水冷ジ
ヤケツト6が接続管をもつて連結されている。
Reference numeral 5 denotes a heat exchange means installed on the upper surface of the lower tank 1 or outside the lower tank 1, which is partially connected to the lower tank 1 or the hot air outlet pipe 8, and water pipes 26 are formed inside at intervals. At the same time, an exhaust pipe 27 is provided on the upper side. A water cooling jacket 6 is connected to a part of the water pipe 26 through a connecting pipe.

第6図と第7図は本発明の別の実施例を示すも
ので、下槽1と貯槽2との境界域に前述のごとく
円筒形ロストル3を回転可能に内設すると共に、
この円筒形ロストル3の半径方向好ましくは貯槽
2の中心部に、下端開孔29が円筒形ロストル3
の外周に指向する数本の気送パイプ28を設け、
この気送パイプ28の上半部とりわけ貯槽内乾燥
ゾーンに対応する部分に蒸気吸引孔30を配設し
たものである。気送パイプ28の貯槽2への取付
けは任意であり、たとえば蓋体12の下面に支持
材を介して垂下せしめてもよいし、図示のように
気送パイプの半径方向にステーを形成して貯槽内
面に連結せしめてよい。その他の構造は第1図な
いし第5図の実施例と同様であるため同符号をも
つて示すに止める。
FIGS. 6 and 7 show another embodiment of the present invention, in which the cylindrical rostol 3 is rotatably installed in the boundary area between the lower tank 1 and the storage tank 2 as described above, and
A lower end opening 29 is formed in the radial direction of the cylindrical rooster 3, preferably in the center of the storage tank 2.
Several pneumatic pipes 28 are provided oriented toward the outer periphery of the
A steam suction hole 30 is provided in the upper half of the pneumatic pipe 28, particularly in a portion corresponding to the drying zone within the storage tank. The pneumatic pipe 28 may be attached to the storage tank 2 at any time, for example, it may be suspended from the bottom surface of the lid 12 via a support material, or it may be provided with stays formed in the radial direction of the pneumatic pipe as shown in the figure. It may be connected to the inner surface of the storage tank. Other structures are similar to those of the embodiment shown in FIGS. 1 to 5, and therefore are designated by the same reference numerals.

なお、装置全体は溶融亜鉛メツキが施され、円
筒形ロストルは耐熱合金で構成することが好まし
く、円筒形ロストルは場合によつては複数個を並
列又は直列状に取付けるようにしてもよいのは勿
論である。
The entire device is preferably hot-dip galvanized, and the cylindrical rostle is preferably made of a heat-resistant alloy. Depending on the case, multiple cylindrical rostles may be installed in parallel or in series. Of course.

本発明は上記のような構成からなるので、使用
にあたつては投入口13から貯槽内へ任意の木質
系粉粒状物たとえば、チツプ、樹皮、木屑、おが
屑、もみ殻あるいはさらに家庭生活から生ずる一
般ゴミや石炭粉を一括投入する。このとき貯蔵の
底には斜板17を周面に張設した円筒形ロストル
3が位置しているため、斜板17を介してのブリ
ツジ現象によつて下槽1への落下が止められ、投
入資料は円筒形ロストル3を底として収容堆積さ
れる。始業にあたつて円筒形ロストル3の近傍に
着火材を装入しておき、エア供給部4を通して所
要量の内燃用エアを送りつつ着火バーナーなどに
より着火材を点火燃焼させ円筒形ロストル3を予
熱しておくことが好ましい。
Since the present invention has the above-mentioned configuration, in use, any wood-based powder or granules such as chips, bark, wood shavings, sawdust, rice husks, or even those generated from household life can be fed into the storage tank from the inlet 13. General garbage and coal powder are thrown in all at once. At this time, since the cylindrical roaster 3 with the swash plate 17 stretched around its circumferential surface is located at the bottom of the storage, the bridging phenomenon via the swash plate 17 prevents it from falling into the lower tank 1. The materials to be input are stored and deposited using the cylindrical Roster 3 as the bottom. Before starting work, igniting material is charged near the cylindrical rostre 3, and while feeding the required amount of internal combustion air through the air supply section 4, the igniting material is ignited and burned using an ignition burner, etc., and the cylindrical rostol 3 is heated. It is preferable to preheat.

上記のようにすれば、円筒形ロストル3の加熱
された斜板17を通して輻射熱が分散状に供給さ
れ、これにより周辺の資料がガス化を開始し、発
生したCHガスやCOなどの有機ガスは上側からの
エアと共に斜板17,17の間の流路21を通つ
て円筒形ロストル内の蓄熱高温ガス燃焼室22に
流入する。そして、これと共に支軸18にエアを
供給すれば、このエアは高温化して噴孔33から
上記ガス燃焼室22に吹込まれ、さきの有機ガス
と混合して旺盛なガス燃焼を起し、円筒形ロスト
ル内は蓄熱高温雰囲気となる。そのため円筒形ロ
ストル3のまわりの資料はこれの輻射熱で急速に
ガス化し、ガス化残部の固形分が主としてエア供
給部4の前方ゾーンでオキ燃焼(内燃)する。そ
して発生有機ガスは上部が湿つた資料層により閉
止されているため、各斜板17,17を介して円
筒形ロストル3に旋回状に流入し、一部のエアは
円筒形ロストル3の斜め上方から斜板17,17
の表裏に反射しジグザグ状に円筒形ロストル内に
流入し、これらが噴孔33からのエアと混合す
る。そのため有機ガスとエアとの混合がきわめて
良好となり、円筒形ロストルを通過する短い時間
のあいだで効率よく熱分解される。
In the above manner, radiant heat is supplied in a distributed manner through the heated swash plate 17 of the cylindrical roaster 3, and as a result, the surrounding materials start to gasify, and the generated organic gases such as CH gas and CO are Together with the air from above, it flows through the flow path 21 between the swash plates 17, 17 into the heat storage hot gas combustion chamber 22 in the cylindrical rooster. When air is supplied to the support shaft 18 at the same time, this air becomes high temperature and is blown into the gas combustion chamber 22 from the nozzle hole 33, mixes with the organic gas and causes vigorous gas combustion, causing the cylinder to burn. The inside of the Roster is a heat-storing, high-temperature atmosphere. Therefore, the material around the cylindrical rotor 3 is rapidly gasified by its radiant heat, and the solid content remaining after gasification is mainly oxidized (internal combustion) in the front zone of the air supply section 4. Since the upper part of the generated organic gas is closed by the moist material layer, it flows into the cylindrical rostre 3 in a swirling manner through the swash plates 17, 17, and some of the air flows diagonally upward into the cylindrical rostrum 3. From swash plate 17, 17
The air is reflected on the front and back sides of the air and flows into the cylindrical rooster in a zigzag pattern, where it mixes with air from the nozzle hole 33. Therefore, the organic gas and air are mixed very well, and the organic gas is thermally decomposed efficiently during the short time it passes through the cylindrical rooster.

かくして操業中においては第8図のごとく円筒
形ロストル3のまわりに内燃ゾーンCが形成さ
れ、この内燃ゾーンCの輻射熱が順次上方に作用
するため上層にはガス化ゾーンBが形成され、さ
らにその上には乾燥ゾーンAが形成され、これら
が内燃によるボリユームの減少に伴い次第に下降
していく。このことから水分を40〜50%含むよう
な資料も円滑に処理できることになり、乾燥ガス
化によりさらさらとなつた資料は円筒形ロストル
3の斜板17,17で落下が防止され、その位置
でオキ燃焼する。なお、斜板17,17間の流路
21を通つて落下したものは、円筒形ロストル内
又は下槽1において輻射熱により分解燃焼される
ため問題ない。
Thus, during operation, an internal combustion zone C is formed around the cylindrical rooster 3 as shown in Fig. 8, and since the radiant heat of this internal combustion zone C acts upward in sequence, a gasification zone B is formed in the upper layer, and furthermore, the radiant heat of this internal combustion zone C acts upward. A drying zone A is formed above and gradually descends as the volume decreases due to internal combustion. This means that materials containing 40 to 50% moisture can be processed smoothly, and materials that have become smooth due to dry gasification are prevented from falling by the swash plates 17, 17 of the cylindrical roaster 3, and remain in that position. Oki burns. Incidentally, there is no problem because the material falling through the flow path 21 between the swash plates 17 and 17 is decomposed and burned by radiant heat in the cylindrical rooster or in the lower tank 1.

上記のようにして湿分の多い粉粒状の資料は貯
槽2に投入されることにより、順次乾燥、ガス化
およびガス燃焼されるため無煙無臭の完全燃焼が
連続し、熱風管8又は排気筒27のドラフトによ
りクリーンな高温熱風となつて暖房機器および裁
培用、養魚用、養蚕用などの各必要設備に供給さ
れる。また、図示の場合には熱交換手段5に装入
され、ここで熱交換により温水又は蒸気を生成さ
せる。
As described above, the powdery materials with high moisture content are put into the storage tank 2, where they are sequentially dried, gasified, and gas-combusted, resulting in continuous smokeless, odorless, and complete combustion. The draft produces clean, high-temperature hot air that is supplied to heating equipment and other necessary equipment such as culturing, fish farming, and sericulture. In the illustrated case, it is inserted into a heat exchange means 5, where hot water or steam is generated by heat exchange.

しかして、燃焼物が粉体や粒体の場合、火格子
の目が荒いと燃焼物が燃焼されぬまま落下し、目
を細くすると炭化物や灰分が格子に詰りやすく、
これにより通気性が阻害され、不完全燃焼を生じ
させるのが問題であつたが、本発明では所定角度
で斜板17,17を張つた円筒形ロストル3を用
いるため、前後のラツプしあつた斜板17,17
による受け作用により未燃のままストレートに落
下することが効果的に防止される。また資料の水
分含有量や粒度などに応じ適当な時間ごと(たと
えば1分ごとあるいは10分ごとのごとし)手動に
より又はタイマーなどを介して自動的に円筒形ロ
ストル3を回転することができるため、回転によ
り内燃ゾーンCに生成された炭化物や灰分に振動
が与えられ、強制的に斜板17,17の間から除
去させられる。従つて目詰りが完全に防止され、
しかも同時に上層の乾燥ゾーンで水分の除去され
た資料を棚吊りを生じさせることなくガス化ゾー
ンに逐次所定の速度と量で下降させることができ
る。さらに円筒形ロストル3の回転のたびにエア
供給部4と反対側に位置するガス化資料が斜板1
7,17に伴われてエア供給部方向に移動し落下
したオキ燃焼物に代わつてここでオキ燃焼するこ
とになり、資料が長時間にわたり定位置で同じ状
態に置かれない。そのため本発明では燃焼障害原
因となる灰分の残留、圧密化および上層資料の沈
降不全が生じず、一括投入方式でありながら可燃
性有機ガスを均一な条件で円形ロストル内の燃焼
室22に連続供給でき、きわめて良好なガス燃焼
および熱風生成を継続して行うことができる。な
お、円筒形ロストル3の回転は毎分あたり0.25〜
0.5回転というように低速で連続化してもよいし、
間欠的であつてもよい。
However, if the combustion material is powder or granules, if the grate is coarse, the material will fall without being burned, and if the grate is narrow, carbide and ash will easily clog the grate.
This impeded air permeability and caused incomplete combustion, which was a problem, but in the present invention, the cylindrical rostre 3 with the swash plates 17, 17 stretched at a predetermined angle is used, so that the front and rear wraps can be prevented. Swash plate 17, 17
The receiving action effectively prevents the unburned fuel from falling straight down. In addition, the cylindrical rotor 3 can be rotated manually or automatically via a timer or the like at appropriate intervals (for example, every minute or every 10 minutes) depending on the moisture content and particle size of the material. Vibration is applied to the carbide and ash generated in the internal combustion zone C by the rotation, and the charcoal and ash are forcibly removed from between the swash plates 17, 17. Therefore, clogging is completely prevented,
Moreover, at the same time, the materials from which moisture has been removed in the upper drying zone can be sequentially lowered into the gasification zone at a predetermined speed and amount without causing any shelving. Furthermore, each time the cylindrical rooster 3 rotates, the gasification material located on the opposite side of the air supply section 4 is transferred to the swash plate 1.
7 and 17, the material will be burned here in place of the combustible material that has moved toward the air supply section and fallen, and the material will not remain in the same position for a long period of time. Therefore, in the present invention, ash remains, compaction, and failure of sedimentation of the upper material, which cause combustion problems, do not occur, and combustible organic gas is continuously supplied to the combustion chamber 22 in the circular rooster under uniform conditions even though it is a bulk injection method. This allows for extremely good gas combustion and hot air generation to continue. In addition, the rotation of the cylindrical Rostr 3 is 0.25~ per minute.
It may be continuous at a low speed such as 0.5 rotations,
It may be intermittent.

また、第6図および第7図の実施例のように貯
槽2に気送パイプ28を挿設しておくときには、
操業中において該気送パイプ28から円筒形ロス
トル内の燃焼室22へ燃焼用2次エアを効果的に
供給できるだけでなく、内燃乾留方式により乾燥
ゾーンAで除去され蒸気となつた資料中の水分が
蒸気吸引孔30を通して気送パイプ28に連続的
に集気され、さらに、この気送パイプ28がガス
化ゾーンBに到つていることからこのゾーンを通
る間に加熱されて高温蒸気となり、気送パイプ2
8の下端開孔29から斜板17,17を通り円筒
形ロストル内の燃焼室22に送入され、乾留可燃
性ガスと混合する。これにより円筒形ロストル3
の高温雰囲気内で水性ガス反応が生ずるため燃焼
効率が著しく助長され、良質の熱風を生成供給す
ることが可能になる。
Furthermore, when the pneumatic pipe 28 is inserted into the storage tank 2 as in the embodiments shown in FIGS. 6 and 7,
During operation, not only can secondary air for combustion be effectively supplied from the pneumatic pipe 28 to the combustion chamber 22 in the cylindrical rooster, but also moisture in the material that has been removed in the drying zone A and turned into steam by the internal combustion carbonization method can be effectively supplied. is continuously collected into the pneumatic pipe 28 through the steam suction hole 30, and furthermore, since this pneumatic pipe 28 reaches the gasification zone B, it is heated and becomes high-temperature steam while passing through this zone. Feed pipe 2
8 through the swash plates 17, 17 and into the combustion chamber 22 in the cylindrical rooster, where it is mixed with the carbonized combustible gas. This allows the cylindrical Rostr 3
Because the water gas reaction occurs in the high-temperature atmosphere, combustion efficiency is significantly improved, making it possible to generate and supply high-quality hot air.

さらに、貯槽2に投入された資料が下層から順
次熱風に変換され槽内の資料量が減少した場合に
は一時的に多量の未燃ガスが生じ、これが貯槽に
留つたり外部に黒煙として放散されるおそれがあ
るが、本発明では貯槽内に円筒形ロストル3を指
向する気送パイプ28が中空状に縦設されている
ため、ダウンドラフト方式による吸引作用で発生
未燃ガスを効果的に集気しかつこれを円筒形ロス
トル内の燃焼室22に送り込んで完全燃焼させる
ことができ、従つて貯槽内の資料全部を無公害
で、効率よく熱風化することができる。
Furthermore, when the material put into storage tank 2 is converted into hot air from the lower layer and the amount of material in the tank decreases, a large amount of unburned gas is temporarily generated, which may remain in the storage tank or as black smoke outside. However, in the present invention, since the pneumatic pipe 28 that directs the cylindrical rostol 3 is installed vertically in the storage tank in a hollow shape, the generated unburned gas can be effectively removed by the suction effect using the downdraft system. It is possible to collect air and send it into the combustion chamber 22 in the cylindrical rooster for complete combustion, and therefore all the materials in the storage tank can be hot-aired efficiently without any pollution.

なお、本発明を燃焼器として使用し、熱風を取
出さずに燃焼ガスをそのまま放出させることも可
能であり、また、ペレツト化された資料の使用が
不可というものでないことはもとよりである。さ
らに、本発明は木質系粉粒状物に好適であるが、
厳密に粉又は粒である必要はなくやさいくずやチ
ツプなどの片状のものも使用可能であり、また石
炭粉などが含まれていても十分使用できる。
It should be noted that it is possible to use the present invention as a combustor and release combustion gas as it is without extracting hot air, and it is of course possible to use pelletized materials. Furthermore, although the present invention is suitable for wood-based powder and granular materials,
It is not strictly necessary to use powder or granules; flake-like materials such as vegetable scraps and chips can also be used, and even if they contain coal powder, etc., they can be used satisfactorily.

以上説明した本発明によるときには、灰取出口
9を有する下槽1に投入口13を有する貯槽2を
立設し、この貯槽2と下槽1とのほぼ境界域にエ
ア供給部4を設けると共に、これの軸線方向に多
数の斜板17を間隔的に張設した円筒形ロストル
3を回転可能に内装し、貯槽に投入された木質系
粉粒状物を円筒形ロストル3と底として堆積させ
つつ円筒形ロストルからの輻射熱で順次乾燥ガス
化させ、乾留ガスを斜板17を通して円筒形ロス
トル内で燃焼させ、かつ円筒形ロストル3の回転
により残灰に振動を与え、下槽にふるい落すよう
にしたので、静止時の円筒形ロストル3による資
料落下防止作用、乾燥ガス化のための輻射熱分散
供給作用、高温蓄熱燃焼作用および回転時の円筒
形ロストル3による残灰除去作用とにより木質系
粉粒状物類を円滑に燃焼させ熱風生成を行うこと
ができる。
According to the present invention as described above, the storage tank 2 having the input port 13 is installed upright in the lower tank 1 having the ash take-out port 9, and the air supply part 4 is provided almost in the boundary area between the storage tank 2 and the lower tank 1. A cylindrical rostol 3 with a large number of swash plates 17 stretched at intervals in the axial direction is rotatably installed inside the tank, and the wood-based powder and granules put into the storage tank are deposited on the cylindrical rostol 3 and the bottom. The ash is sequentially dried and gasified using radiant heat from the cylindrical rostre, and the carbonized gas is combusted in the cylindrical rostre through the swash plate 17, and the remaining ash is vibrated by the rotation of the cylindrical rostol 3, so that it is sieved into the lower tank. Therefore, the cylindrical rostol 3 prevents material from falling when it is stationary, the radiant heat dispersion and supply function for dry gasification, the high temperature heat storage combustion effect, and the ash removal effect of the cylindrical rostol 3 when it rotates. It can burn things smoothly and generate hot air.

また、本発明は貯槽2内に気送パイプ28を設
け、これの上半部に蒸気吸引孔30を形成すると
共にパイプ下端を円筒形ロストル3に臨ませ、こ
の気送パイプ28により円筒形ロストル内の燃焼
室への2次燃焼エア供給と資料から蒸発した水分
の高温化および前記燃焼室への供給を行うように
したので、資料中に吸湿されている水分を効果的
に利用して燃焼効率を著しく助長することができ
ると共に、貯槽内の資料減少時にも未燃ガスをう
まく完全燃焼させることができる。
Further, the present invention provides a pneumatic pipe 28 in the storage tank 2, forms a steam suction hole 30 in the upper half of the pipe, and makes the lower end of the pipe face the cylindrical roistle 3. By supplying secondary combustion air to the combustion chamber inside the document, raising the temperature of moisture evaporated from the materials, and supplying the moisture to the combustion chamber, the moisture absorbed in the materials can be effectively utilized for combustion. Not only can the efficiency be significantly improved, but also the unburned gas can be successfully and completely combusted even when the amount of material in the storage tank is decreasing.

そのため本発明によればいちいちペレツト化な
どの前処理をせず湿分を多く含むままの各種木質
系粉粒状物類をうまく燃料化し、連続安定的に熱
風として供給することができ、しかも構造が簡単
でコンパクトかつ安価な装置とすることができる
などのすぐれた効果が得られる。
Therefore, according to the present invention, it is possible to successfully convert various wood-based powders and granules that still contain a large amount of moisture into fuel without pre-treatment such as pelletization, and continuously and stably supply the fuel as hot air. Excellent effects such as a simple, compact, and inexpensive device can be obtained.

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

第1図は本発明に係る木質系粉粒状物を燃料と
する熱風発生装置の一実施例を示す一部切欠側面
図、第2図は同じくその背面図、第3図は同じく
その平面図、第4図は本発明における円筒形ロス
トルの横断面図、第5図は同じくその縦断面図、
第6図は本発明の他の実施例を示す一部切欠側面
図、第7図は同じくその平面図、第8図は本発明
装置の作用を示す説明図である。 1……下槽、2……貯槽、3……円筒形ロスト
ル、4……エア供給部、5……熱交換手段、9…
…灰取出口、17……斜板、18……支軸、28
……気送パイプ、30……蒸気吸収孔、33……
噴孔。
FIG. 1 is a partially cutaway side view showing an embodiment of a hot air generator using wood-based powder as fuel according to the present invention, FIG. 2 is a rear view thereof, and FIG. 3 is a plan view thereof. FIG. 4 is a cross-sectional view of the cylindrical rostre according to the present invention, and FIG. 5 is a longitudinal cross-sectional view thereof.
FIG. 6 is a partially cutaway side view showing another embodiment of the present invention, FIG. 7 is a plan view thereof, and FIG. 8 is an explanatory view showing the operation of the device of the present invention. DESCRIPTION OF SYMBOLS 1... Lower tank, 2... Storage tank, 3... Cylindrical roost, 4... Air supply section, 5... Heat exchange means, 9...
...Ash outlet, 17...Swash plate, 18...Spindle, 28
...Pneumatic pipe, 30...Steam absorption hole, 33...
Nozzle hole.

Claims (1)

【特許請求の範囲】 1 灰取出口9を有する下槽1の上に投入口13
を有する貯槽2を連設し、この貯槽2と下槽1の
ほぼ境界付近にエア供給部4を挿設すると共に、
エア供給部4の軸線方向には、外周に多数の斜板
17を間隔的に張設した円筒形ロストル3を回転
可能に取付け、投入された木質系粉粒状物を円筒
形ロストル3の斜板17を介して堆積させつつこ
れからの熱で順次乾燥、ガス化させ、ガス化部で
生じた乾留ガスを斜板間のすき間を通して円筒形
ロストル内の燃焼室22で燃焼させるようにし、
さらに高度ロストル周囲の内燃部で生成された残
灰を円筒形ロストル3の回転により斜板17間か
ら下槽1に落下せしめるようにしたことを特徴と
する木質系粉粒状物類を燃料とする熱風供給装
置。 2 灰取出口9を有する下槽1の上に、投入口1
3を有する貯槽2を連設し、この貯槽2を下槽1
のほぼ境界付近にエア供給部4を挿設すると共
に、エア供給部4の軸線方向には、外周に多数の
斜板17を間隔的に張設した円筒形ロストル3を
回転可能に取付け、しかも前記貯槽内には、上半
部分に蒸気吸引孔30を有し下端開孔29が円筒
形ロストル3に指向した気送パイプ28を設け、
投入された木質系粉粒状物類を円筒形ロストル3
の斜板17を介して堆積させつつこれからの熱で
順次乾燥、ガス化させ、ガス化部で生じた乾留ガ
スを斜板17,17間のすき間通して円筒形ロス
トル内に供給すると共に、乾燥過程の木質系粉粒
状物類から生じた水蒸気を気送パイプ28を通し
て円筒形ロストル内に供給し、それらをエア供給
部4からのエアと共に混合燃焼させるようにし、
ロストル周囲の内燃部で生成された残灰を円筒形
ロストル3の回転により斜板17間から下槽1に
落下せしめるようにしたことを特徴とする木質系
粉粒状物類を燃料とする熱風供給装置。 3 斜板17,17がロストル内の中心線に対し
30〜50゜の傾きをもつている特許請求の範囲第1
項又は第2項に記載の木質系粉粒状物類を燃料と
する熱風供給装置。 4 円筒形ロストル3が中心に支軸18を有し、
この支軸18を介して円筒形ロストル3が回転さ
れるようになつている特許請求の範囲第1項又は
第2項に記載の木質系粉粒状物類を燃料とする熱
風発生装置。 5 支軸18が中空状をなすと共に円筒形ロスト
ル内部に位置するゾーンに噴出孔33を有し、支
軸18の外端から導入したエア類を燃焼室22に
供給するようになつている特許請求の範囲第1項
又は第2項記載の木質系粉粒状物類を燃料とする
熱風発生装置。
[Claims] 1. An inlet 13 on the lower tank 1 having an ash outlet 9
A storage tank 2 having a storage tank 2 and a lower tank 1 are arranged in series, and an air supply section 4 is inserted near the boundary between the storage tank 2 and the lower tank 1, and
In the axial direction of the air supply section 4, a cylindrical rostol 3 having a number of swash plates 17 stretched at intervals around the outer periphery is rotatably attached, and the wood powder and granules introduced are transferred to the swash plate of the cylindrical rostol 3. The carbonized gas produced in the gasification section is passed through the gap between the swash plates and combusted in the combustion chamber 22 in the cylindrical roost.
Further, the residual ash generated in the internal combustion section around the altitude rostle is caused to fall from between the swash plates 17 into the lower tank 1 by the rotation of the cylindrical rostle 3. Wood-based powder and granular materials are used as fuel. Hot air supply device. 2 Above the lower tank 1 having the ash outlet 9, there is an inlet 1
A storage tank 2 having a storage tank 3 is installed in series, and this storage tank 2 is connected to a lower tank 1.
An air supply section 4 is inserted near the boundary of the air supply section 4, and a cylindrical rostol 3 having a large number of swash plates 17 stretched at intervals around the outer periphery is rotatably attached in the axial direction of the air supply section 4. In the storage tank, a pneumatic pipe 28 having a steam suction hole 30 in the upper half portion and a lower end opening 29 facing the cylindrical roistle 3 is provided,
The wood-based powder and granules that have been introduced are transferred to a cylindrical roaster 3.
The carbonization gas generated in the gasification section is supplied into the cylindrical roost through the gap between the swash plates 17, and the drying The water vapor generated from the wood-based powder and granules in the process is supplied into the cylindrical rostre through the pneumatic pipe 28, and is mixed and combusted together with the air from the air supply section 4,
Hot air supply using wood-based powder and granular materials as fuel, characterized in that residual ash generated in the internal combustion section around the rostol is caused to fall from between the swash plates 17 into the lower tank 1 by the rotation of the cylindrical rostol 3. Device. 3 The swash plates 17, 17 are aligned with the center line inside the rostre.
Claim 1 having an inclination of 30 to 50 degrees
A hot air supply device using the wood-based powder and granules as described in item 1 or 2 as fuel. 4 The cylindrical rotor 3 has a support shaft 18 in the center,
A hot air generator using wood powder and granules as fuel according to claim 1 or 2, wherein the cylindrical roistle 3 is rotated via the support shaft 18. 5. A patent in which the support shaft 18 is hollow and has an ejection hole 33 in a zone located inside the cylindrical rooster, so that air introduced from the outer end of the support shaft 18 is supplied to the combustion chamber 22. A hot air generator using the wood-based powder and granular material according to claim 1 or 2 as fuel.
JP2326482A 1982-02-16 1982-02-16 Hot air supplier using woody pulverized substance as fuel Granted JPS58140502A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP2326482A JPS58140502A (en) 1982-02-16 1982-02-16 Hot air supplier using woody pulverized substance as fuel

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP2326482A JPS58140502A (en) 1982-02-16 1982-02-16 Hot air supplier using woody pulverized substance as fuel

Publications (2)

Publication Number Publication Date
JPS58140502A JPS58140502A (en) 1983-08-20
JPH0145522B2 true JPH0145522B2 (en) 1989-10-04

Family

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Family Applications (1)

Application Number Title Priority Date Filing Date
JP2326482A Granted JPS58140502A (en) 1982-02-16 1982-02-16 Hot air supplier using woody pulverized substance as fuel

Country Status (1)

Country Link
JP (1) JPS58140502A (en)

Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE10349365A1 (en) * 2003-10-16 2005-05-19 Herlt, Christian, Dipl.-Ing. Carburetted boilers for solid fuels, in particular for straw bales, with optimized exhaust gas values
JP6621028B2 (en) * 2016-09-14 2019-12-18 株式会社ソラール Rice husk combustion hot water boiler and combustion method

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Publication number Publication date
JPS58140502A (en) 1983-08-20

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