JPH0331967B2 - - Google Patents
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- Publication number
- JPH0331967B2 JPH0331967B2 JP62116458A JP11645887A JPH0331967B2 JP H0331967 B2 JPH0331967 B2 JP H0331967B2 JP 62116458 A JP62116458 A JP 62116458A JP 11645887 A JP11645887 A JP 11645887A JP H0331967 B2 JPH0331967 B2 JP H0331967B2
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- Prior art keywords
- air
- container
- combustion
- inner cylinder
- liquid
- Prior art date
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- Fluidized-Bed Combustion And Resonant Combustion (AREA)
Description
【発明の詳細な説明】
[産業上の利用分野]
本発明は、公知の燃焼装置においては使用困難
あるいは不可能な難燃性可燃物を燃焼する技術分
野において利用され、特に水分を多量に含む鉱物
系・生物系の油、及び固体分の多い粗悪可燃物を
安定で効率よく燃焼する燃焼装置に関する。Detailed Description of the Invention [Industrial Field of Application] The present invention is utilized in the technical field of burning flame-retardant combustible materials that are difficult or impossible to use in known combustion devices, and in particular, those that contain a large amount of water. This invention relates to a combustion device that stably and efficiently burns mineral and biological oils and inferior combustible materials with a high solid content.
[従来の技術]
この種の燃焼装置としては、砂、小石等の加熱
媒体を燃焼室に収容し、粗悪可燃物を加熱媒体と
ともに燃焼室内で吹き上げ循環させることによ
り、粗悪可燃物を燃焼させる装置が知られている
(特開昭60−216113号公報、特開昭60−226607号
公報及び特開昭60−256708号公報参照)。[Prior Art] This type of combustion device is a device in which a heating medium such as sand or pebbles is stored in a combustion chamber, and the poor-quality combustible material is blown up and circulated in the combustion chamber together with the heating medium, thereby burning the poor-quality combustible material. is known (see JP-A-60-216113, JP-A-60-226607 and JP-A-60-256708).
[解決すべき問題点]
従来の燃焼装置では、可燃物及び加熱媒体の吹
き上げ及び循環を単一の空気導入管により行つて
いるため、加熱媒体の循環量を、可燃物の供給量
とは別個独立に制御できない。したがつて、粗悪
可燃物の難燃度に応じて加熱媒体の循環量を最適
なものに調節することは困難であつた。[Problems to be solved] In conventional combustion equipment, combustible materials and heating medium are blown up and circulated through a single air introduction pipe, so the amount of circulating heating medium is determined separately from the amount of combustible material supplied. cannot be controlled independently. Therefore, it has been difficult to adjust the circulation amount of the heating medium to an optimum value depending on the flame retardance of the inferior combustible material.
[問題を解決するための手段]
本発明は、従来の燃焼装置のもつていた上述の
問題点を解決し、どんな不均等の液体可燃物でも
安定に安全に燃焼させ、さらには熱効率のよい燃
焼・加熱を行うことができ、しかも、製造コスト
が低廉で経済的な燃焼装置を提供することを目的
とするものである。[Means for Solving the Problems] The present invention solves the above-mentioned problems of conventional combustion devices, enables stable and safe combustion of any uneven liquid combustible material, and also achieves thermally efficient combustion. - The purpose is to provide an economical combustion device that can perform heating and has a low manufacturing cost.
本発明にかかる燃焼装置は、上記目的の達成の
ために、下方に向かつて断面積が小さくなる底部
を有する容器と、該容器内にこれとの間に間〓部
を有するように設けた、上下面開放の内筒と、該
容器の底部に充填される耐熱性固体粒子と、該容
器の底部から容器内へ上方に突出するように設け
られ、吐出端が、該内筒の下端近傍に位置する可
燃性液体送入管と、該容器に設けられ、可燃性液
体を該内筒内で燃焼するための空気を送り入れる
第1空気送入機構であつて、該可燃性液体送入管
を囲み、吐出端が、該可燃性液体送入管の吐出端
とほぼ同じ位置に位置する第1空気送入機構と、
該耐熱性固体粒子を循環させるための空気を送り
込む第2空気送入機構であつて、第1空気送入機
構とは別個に設けられ、該容器内の最下部で、該
第1空気送入機構の根元部の周囲に多孔の空気送
出口を有する第2空気送入機構とからなることを
特徴とする。 In order to achieve the above object, the combustion device according to the present invention includes a container having a bottom portion whose cross-sectional area decreases downwardly, and a space provided within the container with a space between the bottom portion and the bottom portion. An inner cylinder with an open top and bottom, heat-resistant solid particles filled in the bottom of the container, and a discharge end protruding upward from the bottom of the container into the container, with a discharge end near the lower end of the inner cylinder. a flammable liquid inlet pipe located in the inner cylinder, and a first air inlet mechanism provided in the container for feeding air for burning the flammable liquid in the inner cylinder, the flammable liquid inlet pipe a first air supply mechanism surrounding the combustible liquid supply pipe, the discharge end of which is located at approximately the same position as the discharge end of the flammable liquid supply pipe;
A second air supply mechanism for supplying air for circulating the heat-resistant solid particles, the second air supply mechanism being provided separately from the first air supply mechanism, and configured to supply air to the first air supply mechanism at the lowest part of the container. The second air inlet mechanism has a porous air outlet around the base of the mechanism.
本発明の燃焼装置は、不均質な液体可燃物ある
いは固体を含む可燃物を送入すると同時に高温の
固体粗粒子群に接触するように構成され、高温の
固体粗粒子全部が着火源になるために、どんな不
均質の液体可燃物あるいは固体を含む可燃物でも
必ず着火され、安定・安全な燃焼を継続すること
が出来る。 The combustion device of the present invention is configured so that a heterogeneous liquid combustible material or a combustible material containing solids is introduced and simultaneously comes into contact with a group of high-temperature solid coarse particles, and all of the high-temperature solid coarse particles become an ignition source. Therefore, any heterogeneous liquid combustible material or combustible material containing solids will be ignited without fail, and stable and safe combustion can continue.
本発明の燃焼装置は、底部に向つて断面積を小
さくする粗粒子充填部と、耐熱材料で作られる内
筒および液体可燃物を上方に向つて噴出する液体
送入管によつて構成され、粗粒子は、粗粒子充填
部の底部に設置した第2空気送入機構の一部をな
す空気整流板を通じて下方から送入される空気に
よつて流動化され、ほぼ定常的に内筒の内部に循
環される。液体送入管から噴出する液体可燃物の
液滴は、内筒内に送入され、内筒内で高温の固体
粒子群と接触し、急速に加熱・分散・蒸発が行わ
れ、内筒内に同時に送入される燃焼用空気と混合
して直ちに着火する。 The combustion device of the present invention is composed of a coarse particle filling part whose cross-sectional area decreases toward the bottom, an inner cylinder made of a heat-resistant material, and a liquid feed pipe that spouts liquid combustible material upward. The coarse particles are fluidized by air introduced from below through an air baffle plate that is part of the second air supply mechanism installed at the bottom of the coarse particle filling section, and are almost constantly pumped into the interior of the inner cylinder. is circulated. Droplets of liquid combustible material ejected from the liquid inlet pipe are sent into the inner cylinder, where they come into contact with a group of high-temperature solid particles, where they are rapidly heated, dispersed, and evaporated. It mixes with the combustion air that is simultaneously introduced into the air and ignites immediately.
粗粒子群は、上昇する燃焼ガスに伴われて内筒
より上方にとび出るが、重力の作用によつて下降
し、内筒外側、燃焼装置内側の環状部に落下す
る。環状部は高温の固体粗粒子が堆積するが、こ
れらはゆるやかに下降をつづけて粗粒子充填部に
入り、流動化状態になつて内筒内部に循環してゆ
くようになつている。 The group of coarse particles protrudes upward from the inner cylinder with the rising combustion gas, but descends due to the action of gravity and falls on the annular part outside the inner cylinder and inside the combustion device. High-temperature solid coarse particles accumulate in the annular portion, but these continue to slowly descend into the coarse particle filling section, become fluidized, and circulate inside the inner cylinder.
[作用]
以上のごとく、本発明の燃焼装置によつて不均
質液体可燃物あるいは固体を含む可燃物を燃焼す
るには、先ず空気整流板を通ずる空気送入口を停
止して、固体粗粒子を底部にのみ堆積しておき、
液体送入管に通常の液体燃料を送入し、第1空気
送入機構を通じて可燃性液体送入管の吐出端の周
囲に燃焼用空気を送入して、燃焼室に設けたパイ
ロツトバーナーによつて着火し、通常の燃焼を行
わしめることにより燃焼室の温度を上昇させ、
徐々に空気整流板を通して空気を送入することに
より固体循環を行わしめてこれを加熱し、充分着
火出来る温度に達した時点で所定の不均質難燃性
液体不燃物あるいは固体を含む可燃物を送入し、
定常な燃焼を行う。この際、不均質液体可燃物は
水と燃料油の混合物であつても差支えない。[Operation] As described above, in order to burn a heterogeneous liquid combustible material or a combustible material containing solids using the combustion apparatus of the present invention, first, the air inlet passing through the air baffle plate is stopped, and the solid coarse particles are removed. Let it accumulate only at the bottom,
Normal liquid fuel is fed into the liquid feed pipe, and combustion air is fed around the discharge end of the flammable liquid feed pipe through the first air feed mechanism to a pilot burner provided in the combustion chamber. It then ignites and causes normal combustion, raising the temperature of the combustion chamber.
By gradually introducing air through an air baffle plate, the solid is circulated and heated, and when it reaches a temperature sufficient to ignite, a specified heterogeneous flame-retardant liquid incombustible material or combustible material containing solids is delivered. Enter,
Perform steady combustion. In this case, the heterogeneous liquid combustible material may be a mixture of water and fuel oil.
通常のバーナーでは燃焼のできない難燃性液体
可燃性でも、高温粗粒子の循環と接触によつて極
めて安定した安全な定常燃焼操作が出来る。 Even with combustible flame-retardant liquids that cannot be burned in a normal burner, extremely stable and safe constant combustion operations can be achieved through the circulation and contact of high-temperature coarse particles.
燃焼操作は、必ずしも連続に行うばかりでな
く、例えば、朝に着火して夕方に停止する、いわ
ゆる断続操作も、特に小規模な事業所においては
よく行われるものである。このような操作の場合
には、停止時に高温であつた固体粗粒子はその熱
容量が大きいために翌朝までの温度低下が小さ
く、上記のような着火操作を行う必要がなく、直
ちに着火運転が出来るので熱エネルギーおよび労
力の損失が無い。 Combustion operations are not necessarily carried out continuously; for example, so-called intermittent operations, in which the combustion is started in the morning and stopped in the evening, are often carried out, especially in small-scale business establishments. In such an operation, the solid coarse particles that were at a high temperature at the time of shutdown have a large heat capacity, so the temperature drop until the next morning is small, so there is no need to perform the ignition operation as described above, and ignition operation can be started immediately. Therefore, there is no loss of heat energy and labor.
固体粗粒子の流動化および飛び出しの運動エネ
ルギーは大きいので、分散の出来にくい不均質液
体あるいは固体を含む可燃物も内筒内で充分に分
散され、確実に燃焼することが出来る。 Since the kinetic energy of fluidizing and ejecting solid coarse particles is large, combustible materials containing heterogeneous liquids or solids that are difficult to disperse can be sufficiently dispersed within the inner cylinder and can be reliably combusted.
燃焼装置によつて発生する灰分は通常、粒子層
に凝着し易いものであるが、粗粒の場合には、上
記のように運動エネルギーが大きいので凝着を起
さず、円滑に流動、循環し、着火源として充分な
作用を果すことが出来る、このため操作は高温下
で可能であるので、燃焼装置の体積を小さくする
ことが出来る。 The ash generated by combustion equipment usually tends to stick to the particle layer, but in the case of coarse particles, it has a large kinetic energy as mentioned above, so it does not stick and flows smoothly. It circulates and can serve as a sufficient ignition source, so operation can be done at high temperatures and the volume of the combustion device can be reduced.
[実施例]
以下添付図面に基づいて、本発明の好ましい実
施例を説明する。[Embodiments] Preferred embodiments of the present invention will be described below based on the accompanying drawings.
第1図は、本発明の第1実施例を示す縦断面図
である。符号1は、筒状容器からなる燃焼装置本
体を示すものであり、その下部に、下方に向かつ
て断面積を小さくする固体粗粒子充囓部2を備え
る。この固体粗粒子充填部には、燃焼装置本体の
底部のほぼ中央より液体送入管4が、装置本体内
に上方に向つて突出する。液体送入管の上方に
は、装置本体の内壁面との間に環状の間隙を有し
て、上下面が開放した耐熱材料製の円筒状の内筒
3が設けられる。液体送入管4の吐出端は、この
内筒内に突出させてもよい。筒状容器の底部に
は、液体送入管4を囲むように環状の第1空気送
入機構7を設ける。この第1空気送入機構7の吐
出端は、第1図に示すように、液体送入管4の吐
出端とほぼ同じ位置に設けるとよい。さらに、第
1空気送入機構7の根元部の周囲を囲むように第
2空気送入機構の一部をなす空気整流板5を装置
本体、すなわち燃焼室の底部に設ける。この空気
整流板は、例えば、多孔板あるいは多孔質材料板
構造をしていて、固体粗粒子層を支える。燃焼装
置本体1の内壁面と内筒3の外表面間の環状間隙
部には、固体粗粒子が充填される。固体粗粒子
は、平均粒径0.5mm〜6mmのもので耐熱製のもの
であれば、その種類は任意であり、例えば、アル
ミナ、シリカ、シリカ・アルミナ系のように磨耗
に強くて安価なものが好適で、形状には制限はな
いが、球状のものが好ましい。この外、燃焼室に
は、液体送入管を通じて送入する通常の液体燃料
を着火するたの公知の初期着火用パイロツトバー
ナー21を設ける。 FIG. 1 is a longitudinal sectional view showing a first embodiment of the present invention. Reference numeral 1 indicates a combustion device main body made of a cylindrical container, and a solid coarse particle-filled portion 2 whose cross-sectional area decreases downwardly is provided at the bottom thereof. In this solid coarse particle filling section, a liquid feed pipe 4 projects upward into the combustion apparatus main body from approximately the center of the bottom of the combustion apparatus main body. A cylindrical inner tube 3 made of a heat-resistant material and having an annular gap with the inner wall surface of the device main body and having open upper and lower surfaces is provided above the liquid feed pipe. The discharge end of the liquid feed pipe 4 may protrude into this inner cylinder. An annular first air feeding mechanism 7 is provided at the bottom of the cylindrical container so as to surround the liquid feeding tube 4 . The discharge end of the first air supply mechanism 7 is preferably provided at approximately the same position as the discharge end of the liquid supply pipe 4, as shown in FIG. Furthermore, an air baffle plate 5 forming a part of the second air feeding mechanism is provided on the apparatus main body, that is, at the bottom of the combustion chamber, so as to surround the base of the first air feeding mechanism 7. This air baffle plate has, for example, a porous plate or porous material plate structure and supports a layer of solid coarse particles. The annular gap between the inner wall surface of the combustion device main body 1 and the outer surface of the inner cylinder 3 is filled with solid coarse particles. The solid coarse particles can be of any type as long as they have an average particle size of 0.5 mm to 6 mm and are made of heat-resistant material.For example, they may be made of abrasion-resistant and inexpensive materials such as alumina, silica, or silica/alumina. is preferable, and there are no restrictions on the shape, but spherical ones are preferable. In addition, the combustion chamber is provided with a known pilot burner 21 for initial ignition for igniting ordinary liquid fuel fed through a liquid feed pipe.
燃焼用空気は、第1空気送入機構7の空気送入
口6より導入され、液体送入管4のまわりの環状
部を通つて、吐出端から吹き出されることによ
り、液体送入管4の吐出端から液体の滴を激しい
乱流状態で上昇させ、内筒3の内部に循環してく
る高温の固体粗粒子をまき込んでこれらと液滴と
を接触させるとともに着火させ、安定な燃焼を行
わせる。この際、この環状部のまわりには耐熱材
料製の断熱管8を設け、液体送入管の過熱を防止
することが出来る。 Combustion air is introduced from the air inlet 6 of the first air inlet mechanism 7 , passes through the annular portion around the liquid inlet pipe 4 , and is blown out from the discharge end of the liquid inlet pipe 4 . Droplets of liquid rise from the discharge end in a state of intense turbulence, and high-temperature solid coarse particles circulating inside the inner cylinder 3 are mixed in, making contact with these droplets and igniting them, resulting in stable combustion. Let it happen. At this time, a heat insulating tube 8 made of a heat-resistant material is provided around this annular portion to prevent overheating of the liquid feed tube.
一方、粒子循環用の空気は、空気送入口9より
導入され、空気整流板5を通つて固体粗粒子充填
部2の中にある高温の粗粒子層を流動化し、ほぼ
定常的に高温の粗粒子を内筒の内部に循環送入さ
せる。この際燃焼装置本体1の内壁面と内筒3の
外表面間の環状部には、高温の粗粒子層10が堆
積され、緩やかな速度で下降してゆき、固体粗粒
子充填部2の中に入つて流動化循環される。この
場合の固体粗粒子の温度は500〜1100℃の範囲が
好ましい。 On the other hand, air for particle circulation is introduced from the air inlet 9, passes through the air baffle plate 5, fluidizes the high temperature coarse particle layer in the solid coarse particle filling section 2, and almost constantly maintains the high temperature coarse particle layer. The particles are circulated into the inner cylinder. At this time, a high-temperature coarse particle layer 10 is deposited on the annular portion between the inner wall surface of the combustion device main body 1 and the outer surface of the inner cylinder 3, and descends at a slow speed into the solid coarse particle filling section 2. It is then fluidized and circulated. In this case, the temperature of the solid coarse particles is preferably in the range of 500 to 1100°C.
内筒3の内部空間11において燃焼が行われ、
高温となつた燃焼ガスは高速度で上方に向つて流
れるが、その際高温の固体粗粒群を伴い、内筒3
の上方の空間部12に運び上げる。極めて不均質
で難燃性の液体可燃物あるいは固体を含む可燃物
の場合には、内筒3の内部11において高温の固
体粗粒炭素分を含有する固体を付着するが、空間
部12の温度は充分に高く且つ固体粗粒の空間部
12における滞留時間が長いのでそれらの固体分
は燃焼しつくす。空間部12の中で固体粗粒は重
力により上昇速度を減じて反転し、主として燃焼
装置1の内壁面に近接した領域を落下して、燃焼
装置1の内壁面に近接した領域を落下して、燃焼
装置1の内壁面と内筒外表面の間の環状部に形成
される高温の粗粒子層10の上表面に堆積するこ
とにより、高温の固体粗粒子は、粗粒子層10よ
り固体粒子充填部2、内筒内部11、内部空間1
2、高温の粗粒子層10という循環をほぼ定常的
に行う。 Combustion is performed in the internal space 11 of the inner cylinder 3,
The high-temperature combustion gas flows upward at high speed, but at the same time, it is accompanied by high-temperature solid coarse particles and flows into the inner cylinder 3.
It is carried up to the space 12 above. In the case of extremely heterogeneous and flame-retardant liquid combustibles or combustibles containing solids, solids containing high-temperature solid coarse carbon are deposited in the interior 11 of the inner cylinder 3, but the temperature of the space 12 is sufficiently high and the residence time of the solid coarse particles in the space 12 is long, so that the solid components are completely burned. In the space 12, the solid coarse particles reduce their rising speed due to gravity and turn around, mainly falling in the area close to the inner wall surface of the combustion device 1; , the high-temperature solid coarse particles are deposited on the upper surface of the high-temperature coarse particle layer 10 formed in the annular portion between the inner wall surface and the outer surface of the inner cylinder of the combustion device 1, so that the high-temperature solid coarse particles become more solid particles than the coarse particle layer 10. Filling part 2, inner cylinder interior 11, internal space 1
2. The high temperature coarse particle layer 10 is circulated almost constantly.
第1図は燃焼ガス出口13を内筒上面の位置付
近に設けた場合であり、内筒内の空間11から高
流速で上昇した燃焼ガスが反転して下方に向きを
かえ、空間部12内で燃焼装置1の内壁面に近い
領域を下方に流れることにより、随伴する高温固
体粗粒が燃焼装置1の頂部に衝突することを抑止
する作用を行わせる。この際燃焼ガス出口13の
数および形状、および内筒の上面に対する位置関
係は任意であり、例えば第1図にように対称軸の
まわりに13′などの複数個の出口をつけること
が好ましい。 FIG. 1 shows a case where the combustion gas outlet 13 is provided near the top surface of the inner cylinder, and the combustion gas rising from the space 11 in the inner cylinder at a high flow rate is reversed and directed downward, and inside the space 12. By flowing downward in a region close to the inner wall surface of the combustion device 1, the accompanying high-temperature solid coarse particles are prevented from colliding with the top of the combustion device 1. At this time, the number and shape of the combustion gas outlets 13 and their positional relationship with respect to the upper surface of the inner cylinder are arbitrary. For example, it is preferable to provide a plurality of outlets 13' around the axis of symmetry as shown in FIG.
本発明の燃焼装置には液体導入管4による液体
可燃物を送入するだけではなく、その上に例えば
空間部12の中の適当な位置に送入口14を設
け、例えば、固体を含む可燃物のようにポンプに
よる送入が困難な可燃物を内筒3の内部空間11
に送入することができる。 In the combustion apparatus of the present invention, not only the liquid combustible material is introduced through the liquid introduction pipe 4, but also an inlet port 14 is provided at an appropriate position in the space 12, so that, for example, combustible materials including solids are introduced. The internal space 11 of the inner cylinder 3 contains combustible materials that are difficult to pump.
can be sent to.
また、例えば、有臭ガスのように高温度にして
処理することが要求される場合はそのガスを燃焼
装置1の頂部に開口する送入口15より下方に向
つて送入し、あわせて上昇してくる高温の固体粗
粒子群が頂部に衝突することを抑止することがで
きる。 For example, if the gas needs to be treated at a high temperature, such as with odorous gas, the gas is fed downward through the inlet 15 opened at the top of the combustion device 1, and the gas rises as well. It is possible to prevent the high-temperature solid coarse particles coming from colliding with the top.
液体送入管4を通じて送入する液体が、例え
ば、廃油、魚油などのように大きな発熱量を有す
る場合には、燃焼によつて発生する熱エネルギー
を回収することが必要である。第2図(簡明化の
ため、燃焼装置の上半部のみを示し、下半部は、
第一実施例と同様なので省略する。)はこの場合
に対する実施例であり、燃焼装置の空間12のま
わりの壁面を水冷ジヤケツト16を用いて構成
し、給水口17からジヤケツト16に送入される
水を加熱し、温水として温水口18から流出させ
ることもできる。 When the liquid fed through the liquid feed pipe 4 has a large calorific value, such as waste oil or fish oil, it is necessary to recover the thermal energy generated by combustion. Figure 2 (For simplicity, only the upper half of the combustion device is shown; the lower half is
Since it is the same as the first embodiment, the explanation will be omitted. ) is an embodiment for this case, in which the wall surface around the space 12 of the combustion device is constructed using a water cooling jacket 16, and the water fed into the jacket 16 from the water inlet 17 is heated, and the water is supplied as hot water to the hot water inlet 18. It can also be drained from.
また熱エネルギーを水蒸気にて回収する場合に
は、第3図(簡明化のため、燃焼装置の上半部の
みを示し、下半部は、第一実施例と同様なので省
略する。)における符号19で示すような水管を
もつて空間12を囲み、燃焼ガスおよび高温固体
粗粒子群からの強烈な放射熱エネルギーによつて
効率のよい水蒸気発生を行うことができる。 In addition, when thermal energy is recovered by steam, the reference numerals in FIG. By surrounding the space 12 with water pipes such as those shown at 19, efficient steam generation can be achieved using intense radiant heat energy from the combustion gas and the high-temperature solid coarse particles.
第1図〜第3図は燃焼ガスの出口を燃焼装置空
間部12の下部に設置した例であるが、その位置
は必ずしもそれに制限されず、例えば第4図(簡
明化のため、燃焼装置の上半部のみを示し、下半
部は、第一実施例と同様なので省略する。)のよ
うに燃焼装置1の頂部に燃焼ガス出口20を設置
しても差支えない。 1 to 3 are examples in which the combustion gas outlet is installed at the lower part of the combustion device space 12, but its position is not necessarily limited thereto. For example, in FIG. Only the upper half is shown, and the lower half is omitted because it is similar to the first embodiment.) The combustion gas outlet 20 may be installed at the top of the combustion device 1.
[発明の効果]
以上のごとくの本発明によるならば、次のよう
な効果を得る。[Effects of the Invention] According to the present invention as described above, the following effects can be obtained.
公知のバーナーでは燃焼不可能な不均質難燃
性の可燃液体あるいは固体を含む液体を安定に
燃焼することができる。 It is possible to stably burn heterogeneous flame-retardant combustible liquids or liquids containing solids that cannot be burned using known burners.
効率が高く失火の危険性がなく安全である。 It is highly efficient and safe with no risk of misfire.
固体粗粒の熱容量が大きいため、断続操作の
場合でもすぐ着火と定常運転ができるので熱効
率が大きい。 Due to the large heat capacity of solid coarse particles, immediate ignition and steady operation are possible even in intermittent operation, resulting in high thermal efficiency.
停止時にも固体粒の閉塞が無い。 There is no blockage of solid particles even when the machine is stopped.
流動状況・燃焼状況の観察が容易であり、操
作がやり易い。 It is easy to observe the flow and combustion conditions and is easy to operate.
粗粒子循環用の空気は、難燃性不燃物を循環
させる燃焼用空気とは別の送入口を通じて送り
込まれるので、第2空気送入機構を通じて送り
込む空気量を制御することにより、難燃性不燃
物の供給量とは独立して粗粒子の循環量を最適
状態に調節出来る。 The air for coarse particle circulation is sent through a separate inlet from the combustion air that circulates flame-retardant and noncombustible materials, so by controlling the amount of air sent through the second air supply mechanism, it is possible to The circulation amount of coarse particles can be adjusted to the optimum state independently of the amount of material supplied.
第1空気送入機構は、可燃性液体送入管の吐
出端とほぼ同じ位置まで、可燃性液体送入管を
囲んでいるので、可燃性液体送入管自体が、直
接加熱されなくて済む。このため、燃料のカー
ボン化による可燃性液体送入管の吐出端の閉塞
を回避できる。また、循環する固体粒子が、可
熱性液体送入管に直接当たるのを最小限に抑え
られる。 Since the first air supply mechanism surrounds the flammable liquid supply pipe to almost the same position as the discharge end of the flammable liquid supply pipe, the flammable liquid supply pipe itself does not need to be directly heated. . Therefore, clogging of the discharge end of the flammable liquid feed pipe due to carbonization of the fuel can be avoided. Also, direct contact of circulating solid particles with the heatable liquid inlet tube is minimized.
可燃性液体送入管を囲む第1空気送入機構
は、可燃性液体送入管の吐出端とほぼ同じ位置
に吐出端を有するので、可燃性液体の吹き飛ば
し効果が大である。 The first air supply mechanism surrounding the flammable liquid supply pipe has a discharge end at approximately the same position as the discharge end of the flammable liquid supply pipe, and therefore has a great effect of blowing off the combustible liquid.
可燃性液体送入管の吐出端が、該内筒の下端
近傍に位置するので、液体可燃物の蒸発や燃焼
が、内筒内側で確実に行われる。 Since the discharge end of the flammable liquid feed pipe is located near the lower end of the inner cylinder, evaporation and combustion of the liquid combustible material is reliably performed inside the inner cylinder.
第1図は本発明の第一実施例の構成概要を示す
縦断面図、第2図、第3図、第4図は燃焼装置上
部形状についての変形を示す、各々第二、第三、
第四実施例装置を示す部分縦断面図である。
1……燃焼装置本体、2……固体粗粒子充填
部、3……内筒、4……液体送入管、5……空気
整流板、6,9……空気送入口、7……空気送入
部、8……断熱管、10……粗粒子層、11……
内筒内部空間、12……燃焼装置空間部、13,
13′……燃焼ガス出口、14……可燃物送入口、
15……気体送入口、16……水冷ジヤケツト、
17……給水口、18……温水口、19……水
管、20……燃焼ガス排出口、21……パイロツ
トバーナー。
FIG. 1 is a longitudinal cross-sectional view showing the outline of the configuration of the first embodiment of the present invention, and FIGS. 2, 3, and 4 show modifications of the upper shape of the combustion device, respectively.
FIG. 7 is a partial vertical cross-sectional view showing the device of the fourth embodiment. 1...Combustion device main body, 2...Solid coarse particle filling section, 3...Inner cylinder, 4...Liquid feed pipe, 5...Air straightening plate, 6, 9...Air inlet, 7...Air Inlet section, 8...Insulated pipe, 10...Coarse particle layer, 11...
Inner cylinder internal space, 12... Combustion device space, 13,
13'... Combustion gas outlet, 14... Combustible material inlet,
15... Gas inlet, 16... Water cooling jacket,
17...Water inlet, 18...Hot water inlet, 19...Water pipe, 20...Combustion gas discharge port, 21...Pilot burner.
Claims (1)
する容器と、 該容器内にこれとの間に間〓部を有するように
設けた、上下面開放の内筒と、 該容器の底部に充填される耐熱性固体粒子と、 該容器の底部から容器内へ上方に突出するよう
に設けられ、吐出端が、該内筒の下端近傍に位置
する可熱性液体送入管と、 該容器に設けられ、可燃性液体を該内筒内で燃
焼するための空気を送り入れる第1空気送入機構
であつて、該可燃性液体送入管を囲み、吐出端
が、該可燃性液体送入管の吐出端とほぼ同じ位置
に位置する第1空気送入機構と、 該耐熱性固体粒子を循環させるための空気を送
り込む第2空気送入機構であつて、該第1空気送
入機構とは別個に設けられ、該容器内の最下部
で、該第1空気送入機構の根元部の周囲に多孔の
空気送出口を有する第2空気送入機構とからなる
ことを特徴とする、粗粒を媒体とする燃焼装置。[Scope of Claims] 1. A container having a bottom whose cross-sectional area decreases downward; an inner cylinder with an open upper and lower surface provided within the container with a space between the bottom; heat-resistant solid particles filled in the bottom of the container; a heat-resistant liquid feed pipe provided to protrude upward from the bottom of the container into the container and having a discharge end located near the lower end of the inner cylinder; , a first air supply mechanism provided in the container for supplying air for combustion of the flammable liquid in the inner cylinder, the first air supply mechanism surrounding the flammable liquid supply pipe and having a discharge end disposed in the combustible liquid a first air supply mechanism located at approximately the same position as the discharge end of the liquid supply pipe; and a second air supply mechanism for supplying air for circulating the heat-resistant solid particles, the first air supply mechanism comprising: A second air inlet mechanism is provided separately from the inlet mechanism and has a porous air outlet around the base of the first air inlet mechanism at the lowest part of the container. A combustion device that uses coarse particles as a medium.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP11645887A JPS63282417A (en) | 1987-05-13 | 1987-05-13 | Burner using rough particle as medium |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP11645887A JPS63282417A (en) | 1987-05-13 | 1987-05-13 | Burner using rough particle as medium |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS63282417A JPS63282417A (en) | 1988-11-18 |
| JPH0331967B2 true JPH0331967B2 (en) | 1991-05-09 |
Family
ID=14687615
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP11645887A Granted JPS63282417A (en) | 1987-05-13 | 1987-05-13 | Burner using rough particle as medium |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS63282417A (en) |
Family Cites Families (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| GB1577717A (en) * | 1976-03-12 | 1980-10-29 | Mitchell D A | Thermal reactors incorporating fluidised beds |
| JPS55165416A (en) * | 1979-06-13 | 1980-12-23 | Ebara Corp | Fluidized bed incinerator |
| JPS5620455A (en) * | 1979-07-31 | 1981-02-26 | Matsushita Electric Works Ltd | Air massager |
-
1987
- 1987-05-13 JP JP11645887A patent/JPS63282417A/en active Granted
Also Published As
| Publication number | Publication date |
|---|---|
| JPS63282417A (en) | 1988-11-18 |
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