JPH02106603A - combustion device - Google Patents
combustion deviceInfo
- Publication number
- JPH02106603A JPH02106603A JP25823688A JP25823688A JPH02106603A JP H02106603 A JPH02106603 A JP H02106603A JP 25823688 A JP25823688 A JP 25823688A JP 25823688 A JP25823688 A JP 25823688A JP H02106603 A JPH02106603 A JP H02106603A
- Authority
- JP
- Japan
- Prior art keywords
- heat
- liquid fuel
- combustion
- fuel
- vaporizing material
- 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.)
- Pending
Links
Landscapes
- Wick-Type Burners And Burners With Porous Materials (AREA)
Abstract
Description
【発明の詳細な説明】
〔産業上の利用分野〕
本発明は、液体燃料を多孔質の気化体に含浸させて燃焼
する比較的小型の燃焼装置、例えばl」\型のボイラや
燃料加熱装置等に関する。[Detailed Description of the Invention] [Field of Industrial Application] The present invention is applicable to relatively small-sized combustion devices that impregnate liquid fuel into a porous vaporized body and burn it, such as an l'' type boiler or a fuel heating device. Regarding etc.
液体燃料の燃焼はまず蒸発という過程を経て気化し”C
なる燃料蒸気が酸素と反応して行なわれる。When liquid fuel is burned, it first undergoes a process called evaporation and becomes vaporized.
This is done by reacting fuel vapor with oxygen.
この際、液体IBMを気化するものとして多孔質のセラ
ミックスや金属等からなる気化体が用いられ、液体燃料
はこの気化体に含浸され、その細孔部分を液体の表面張
力、N力または液体燃料を送液するポンプの吐出圧力等
によりて気化体の表面に達し、燃焼により生じた火炎の
かく射や対流による熱を受け、蒸発して燃焼する。この
ような気化体を有する燃焼装f1として従来W、4図に
示すものが知られている。図に2いて多孔質のセラミッ
ク等からなる気化体2は炉容器3の−1の周面に燃焼突
気の複数の空気分配孔4を備えたカバー5に取付けられ
ている。なお気化体2には炉容器3内の燃焼室6側に気
化体カバー7が取付けられている。燃焼室6内には炉容
器3と内壁8とにより環状のガスの流路が形成される熱
交換器9が設けられている。なお、11 、12は熱交
換器9に流入するガスの入口、出口であり、13は燃焼
排ガスが排出される排出口である。At this time, a vaporizer made of porous ceramics, metal, etc. is used to vaporize the liquid IBM, and the liquid fuel is impregnated with this vaporizer, and the pores are controlled by the surface tension of the liquid, the N force, or the liquid fuel. The liquid reaches the surface of the vaporized body due to the discharge pressure of the pump that delivers the liquid, receives heat from the flame radiation and convection generated by combustion, and evaporates and burns. As a combustion device f1 having such a vaporized body, the one shown in FIG. 4 is conventionally known. As shown in FIG. 2, a vaporizer 2 made of porous ceramic or the like is attached to a cover 5 provided with a plurality of combustion air distribution holes 4 on the -1 peripheral surface of a furnace vessel 3. A vaporizer cover 7 is attached to the vaporizer 2 on the combustion chamber 6 side within the furnace vessel 3. A heat exchanger 9 is provided in the combustion chamber 6 in which the furnace vessel 3 and the inner wall 8 form an annular gas flow path. Note that 11 and 12 are an inlet and an outlet for gas flowing into the heat exchanger 9, and 13 is an outlet from which combustion exhaust gas is discharged.
ファン15はカバー5を囲むケーシング16の中に設け
られ、ケーシング16の外側に突気取入口17を備えた
ファン駆動用のモータ18が取付けられている。The fan 15 is provided in a casing 16 surrounding the cover 5, and a fan driving motor 18 having a sudden air intake port 17 is attached to the outside of the casing 16.
l9は燃料供給管であり、ケーシング16.カバー5を
貫通して気化体21こ設けられた燃料供給口かに挿入さ
れている。なお図示しないが点火装置が備えられている
。19 is a fuel supply pipe, and casing 16. The vaporizer 21 is inserted into a fuel supply port provided through the cover 5. Although not shown, an ignition device is provided.
このような燃焼装置の構造により液体燃料は外部からポ
ンプ等により燃料供給管19を通り燃料出口部21から
気化体2の燃料供給口(9)に供給される。With such a structure of the combustion device, liquid fuel is supplied from the outside to the fuel supply port (9) of the vaporized body 2 through the fuel supply pipe 19 from the fuel outlet portion 21 by a pump or the like.
供給された液体燃料は気化体2の細孔を通って気化体2
の周囲に達し、燃料の燃焼によるふく射熱や対流によっ
て気化して燃焼する。この時燃焼に必要な空気は空気塊
人口17からファン15によりて吸引され、エネルギを
与えられてファン15とカバー5との間の空気予熱室器
を経て空気分配孔4を通って気化体2の周囲から中心部
に向りて吹きつけられ、気化した燃料ガスと混合されて
燃焼する。The supplied liquid fuel passes through the pores of the vaporized body 2
The fuel reaches the surrounding area, vaporizes and burns due to radiant heat and convection from the combustion of the fuel. At this time, the air necessary for combustion is sucked from the air mass 17 by the fan 15, is energized, passes through the air preheating chamber between the fan 15 and the cover 5, and passes through the air distribution hole 4 to the vaporized body 2. It is blown from the periphery toward the center, mixed with vaporized fuel gas, and combusted.
燃焼ガスは燃焼室6の周囲の熱交換器内jA8から熱交
換器9を流れる加熱流体Uに熱を伝え、排気口13から
外部へ排出される。加熱流体Uは入口11から供給され
出口12を経て外部へ送り出される。The combustion gas transfers heat from the inside of the heat exchanger jA8 around the combustion chamber 6 to the heating fluid U flowing through the heat exchanger 9, and is discharged to the outside from the exhaust port 13. The heating fluid U is supplied from the inlet 11 and sent out to the outside via the outlet 12.
このようにして液体燃料は気化体2にて燃焼による熱に
より気化して燃焼が行なわれるが、この方式の燃焼装置
によれば液体燃料の気化液面を水平に保持する必要がな
いので取付方向としてバーナを下向きにすることもでき
るなど火炎方向を自由に選択できるし、振動などにより
失火する恐れもないという利点がある。また、特にこの
方式では燃料噴き式のような一般的に高級な燃料ポンプ
や燃料噴射弁を必要としないので小型の燃焼装置が安価
に提供できるという利点もある。In this way, the liquid fuel is vaporized and combusted by the heat generated by combustion in the vaporizer 2. However, with this type of combustion device, there is no need to maintain the vaporized level of the liquid fuel horizontally, so the mounting direction is The advantage is that the flame direction can be freely selected, such as by being able to point the burner downward, and there is no risk of misfires caused by vibrations. In addition, this method has the advantage that a compact combustion device can be provided at a low cost since it does not require a generally high-grade fuel pump or fuel injection valve such as a fuel injection type.
上記の燃焼装置は小型軽量であること、つまり装置の単
位容積(または重量)当りの燃焼量の多いこと、または
単位容積(′f:たはWit)当りの燃料の発熱量の多
いこと、そしてどんな液体燃料でも燃焼可能であること
が望まれている。しかし上記の燃焼装置では燃料量を増
しても無制限に燃焼できるわけでなく、ある量販上では
気化体21ごて気化できなくなる。すなわち、ふく射や
対流Eこよって気化体が受ける熱量以上には液体燃料を
気化できなくなるので、気化しきれない液体燃料は液滴
として気化体2の下面からしたたり落ちて来て気化体針
午方(水平設置の場合)lこ落下する。この際、伝熱等
によりである程度の液体燃料も気化できるが、気化しき
れない液体燃料は気化体2の下側の空気分配孔4から空
気予熱室器へ流れ出しやがてはモータ18のフランジ面
がなどから生の液体燃料が流れ出したり、また燃焼室6
tこ吹き飛ばされて留った液体燃料が気化する熱でもっ
て熱交換器内壁8の温度を下げたり、燃焼室で気化した
ガスが正常位置にて燃焼しない(燃焼室の出口付近や排
気管中などで燃焼する)ため、効率の低下を来たしたり
危険な状態を生み出す。The above combustion device is small and lightweight, that is, it has a large amount of combustion per unit volume (or weight) of the device, or a large calorific value of the fuel per unit volume ('f: or Wit), and It is desired to be able to burn any liquid fuel. However, in the above-mentioned combustion device, even if the amount of fuel is increased, it is not possible to burn the fuel indefinitely, and the vaporized material 21 cannot be vaporized at certain mass sales. In other words, since the liquid fuel cannot be vaporized more than the amount of heat received by the vaporized body due to radiation and convection E, the liquid fuel that cannot be vaporized falls down from the bottom surface of the vaporized body 2 as droplets, If installed horizontally, it will fall down. At this time, a certain amount of liquid fuel can be vaporized due to heat transfer, etc., but the liquid fuel that is not completely vaporized flows into the air preheating chamber from the air distribution hole 4 on the lower side of the vaporizer 2, and eventually the flange surface of the motor 18 Raw liquid fuel may flow out from the combustion chamber 6, etc.
The liquid fuel that remains after being blown away may lower the temperature of the heat exchanger inner wall 8 with the heat of vaporization, or the gas vaporized in the combustion chamber may not burn in the normal position (near the exit of the combustion chamber or in the exhaust pipe). etc.), resulting in a decrease in efficiency and creating a dangerous situation.
また、燃料の選択において、例えば灯油、軽油。In addition, when selecting fuel, for example, kerosene or diesel oil.
航空用燃料ガソリン等と最近工業的に盛んに利用され始
めたメタノールとを比較してみると、発熱量は灯油、軽
油、航空燃料等が約10000〜10500Ca4/g
rであるのに対し、メタノールのそれは4760c嵯へ
rであり、同じ発熱量を得るためにはメタノールは軽油
などの2倍以上の量を燃焼させねばならない。さらに両
者の蒸発熱を比較してみると軽油を例にとるならば色々
と種類はあるが、平均では約90 cd7grであるの
lこ対し、メタノールのそれは263cdygr必要で
ある。このことはメタノールを燃焼させて、軽油と同じ
発熱量を得るためには気化体が必要とする蒸発熱は
x−=6.13となる。つまりメタノール燃焼の場合
は6倍の熱量を気化体は液体燃料に与えてやらなければ
液体燃料の一部が気化せずに前述したようにモータフラ
ンジ面からの液だれや正常な位置での燃焼が行なわれず
、性能の低下等の状態が生じるという問題がある。Comparing aviation fuel gasoline, etc. with methanol, which has recently begun to be widely used industrially, the calorific value of kerosene, diesel oil, aviation fuel, etc. is approximately 10,000 to 10,500 Ca4/g.
r, whereas that of methanol is 4760cr, and in order to obtain the same calorific value, methanol must be burned in more than twice the amount as light oil. Furthermore, when comparing the heat of vaporization of the two, taking light oil as an example, although there are various types, the average is about 90 cd7gr, whereas methanol requires 263 cdygr. This means that in order to burn methanol and obtain the same calorific value as light oil, the vaporization heat required by the vaporized substance is
x-=6.13. In other words, in the case of methanol combustion, the vaporized substance must give 6 times the amount of heat to the liquid fuel, otherwise a part of the liquid fuel will not vaporize, and as mentioned above, the liquid may drip from the motor flange surface or burn at the normal position. There is a problem in that this is not carried out and a situation such as performance deterioration occurs.
また、燃焼装置の定格仕様は燃焼量と燃料の両面から決
められるが、その定格仕様は安全性を見込んで決められ
るため必要以上の大きさとなる。Furthermore, the rated specifications of a combustion device are determined from both the amount of combustion and the fuel, but the rated specifications are determined with safety in mind, so the size is larger than necessary.
したがってメタノールを燃焼する燃焼装置では軽油等の
約6倍より大きい気化能力をもつ装置となり、当方式の
%徴である小型で安価な装置とすることができないとい
う問題がある。Therefore, a combustion device that burns methanol has a vaporization capacity that is about six times greater than that of light oil, etc., and there is a problem that it cannot be made into a small and inexpensive device, which is the characteristic of this method.
本発明の目的は液体燃料の気化を促進することにより燃
焼能力、燃焼効率が高く小型化できる液体燃料の燃焼装
置を提供することである。An object of the present invention is to provide a liquid fuel combustion device that has high combustion capacity and combustion efficiency and can be downsized by promoting vaporization of liquid fuel.
上記課題を解決するために、本発明によれば多孔質から
なる気化体に液体燃料を含浸し、燃焼室で燃焼針こより
生じる熱媒体により気化して燃焼空気により燃焼する燃
焼装置lこおいて、気化体に気化体の少なくとも一部を
覆う伝熱部材と、この伝熱部材に接続し、気化体から燃
焼室に延びる伝熱部材とを設けるものとする。In order to solve the above problems, the present invention provides a combustion apparatus in which a porous vaporized body is impregnated with liquid fuel, vaporized in a combustion chamber by a heat medium generated from a combustion needle, and then combusted by combustion air. The vaporized body is provided with a heat transfer member that covers at least a portion of the vaporized body, and a heat transfer member that is connected to the heat transfer member and extends from the vaporized body to the combustion chamber.
気化体の少なくとも一部を覆う伝熱部材と、これに接続
し気化体から燃焼室に延びる伝熱部材を設けたことによ
り、気化体から延びる伝熱部材は燃焼室で燃焼により生
じた高温の熱媒体から熱を受け、この熱はこの伝熱部材
を伝熱して気化体に導かれ、さらに気化体を覆う伝熱部
材に伝熱して気化体に供給されるので、気化体には液体
燃料が気化するのに十分な熱が供給され、このため気化
体に含浸され細孔を通る液体燃料は完全に気化して燃焼
が行なわれる。By providing a heat transfer member that covers at least a portion of the vaporized body and a heat transfer member connected to the heat transfer member that extends from the vaporized body to the combustion chamber, the heat transfer member extending from the vaporized body can absorb the high temperature generated by combustion in the combustion chamber. Heat is received from the heating medium, and this heat is transferred through this heat transfer member and led to the vaporized body, and further transferred to the heat transfer member that covers the vaporized body and supplied to the vaporized body, so that the vaporized body contains liquid fuel. Sufficient heat is supplied to vaporize the fuel, so that the liquid fuel impregnated with the vapor and passing through the pores is completely vaporized and combusted.
以下図面正こ基づいて本発明の実施例について説明する
。第1図は本発明の実施例による燃焼装置の断面図、$
2図は第1図のA−A断面図である。Embodiments of the present invention will be described below with reference to the accompanying drawings. FIG. 1 is a sectional view of a combustion device according to an embodiment of the present invention, $
FIG. 2 is a sectional view taken along line AA in FIG. 1.
なお、第1図、第2図および後述する第3図において第
4図の従来例と同一部品には同じ符号を付し、その説明
を省略する。第1図、第2図において従来例と異なるの
は気化体2の燃焼室側面を覆う伝熱板Iと、これに接続
し燃焼室6の中間位置迄に届く十分の長さをもった伝熱
棒31が複数本設けられたことである。ここで伝熱板I
と伝熱棒31とは溶接とかネジ接手などによって強固に
接、読して接続部にて熱抵抗を発生しないようlこする
。伝熱棒31は燃焼による火炎を十分に受けるので、単
純な丸棒のような断面形状にて必要な熱は十二分に集め
られるけれど、もし何らかの理由でさらに熱量が必要の
場合には燃焼を阻害しない範囲で表面積を増すことも可
能である。なお、伝熱板間。In FIG. 1, FIG. 2, and FIG. 3 which will be described later, the same parts as in the conventional example shown in FIG. 4 are given the same reference numerals, and their explanations will be omitted. What is different from the conventional example in FIGS. 1 and 2 is the heat transfer plate I that covers the side surface of the combustion chamber of the vaporized body 2, and the heat transfer plate I that is connected to this and has a sufficient length to reach the middle position of the combustion chamber 6. This is because a plurality of heating rods 31 are provided. Here, heat exchanger plate I
The heat transfer rod 31 and the heat transfer rod 31 are firmly connected by welding or threaded joints, and the joints are rubbed so as not to generate thermal resistance. Since the heat transfer rod 31 receives sufficient flame from combustion, it can collect enough heat with its simple round rod-like cross-sectional shape, but if for some reason more heat is needed It is also possible to increase the surface area within a range that does not inhibit the In addition, between the heat exchanger plates.
伝熱棒31は熱伝導性の良い銅、アルミニウム等から製
造されている。The heat transfer rod 31 is made of copper, aluminum, or the like, which has good thermal conductivity.
このような構成により伝熱棒31は燃焼室6内の火炎や
燃焼ガスから熱を受領し、この集めた熱を伝熱板間に伝
える。一方、燃料供給管19から送られた液体燃料は気
化体2の燃料供給日田から気化体2に入り気化体の細孔
を通りて気化体2の表面に達する。この際一部の液体燃
料は伝熱板(9)に接する面lこて熱の授受を行なう。With this configuration, the heat transfer rod 31 receives heat from the flame and combustion gas in the combustion chamber 6, and transfers the collected heat between the heat transfer plates. On the other hand, the liquid fuel sent from the fuel supply pipe 19 enters the vaporizer 2 from the fuel supply hole of the vaporizer 2, passes through the pores of the vaporizer, and reaches the surface of the vaporizer 2. At this time, part of the liquid fuel transfers heat to and from the surface of the heat exchanger plate (9).
そして伝熱板IかイAト
ら伝えられた熱はさらに燃料自身の伝熱、気化器本体の
伝熱lこよって気化体の内部迄達して液体燃料を加熱す
ると同時に液体燃料の気化熱によって冷却される液体燃
料及び気化体に熱を供給して液体燃料の蒸発を促進する
。このため気化体2に送られた液体燃料はすべて気化さ
れ、これにより液体燃料は未燃焼料を生じることなく良
好に燃焼する。The heat transferred to the heat transfer plate I or A further reaches the inside of the vaporized body through heat transfer of the fuel itself and heat transfer of the vaporizer body, and heats the liquid fuel. Heat is supplied to the liquid fuel and the vaporized body to be cooled to promote evaporation of the liquid fuel. Therefore, all of the liquid fuel sent to the vaporized body 2 is vaporized, and as a result, the liquid fuel is burnt well without producing any unburned fuel.
第3図は本発明の異なる実施例による燃焼装置の断面図
である。図Iこおいては気化体2のファン15側の面1
こも伝熱板℃を取付け、伝熱棒おを伝熱板刃と気化体2
とを貫通して伝熱板33に接続している。また伝熱1e
34は伝熱板(9)に接続するとともにその一部は気化
体2の内部に挿入されている。FIG. 3 is a sectional view of a combustion device according to a different embodiment of the invention. In Figure I, the fan 15 side surface 1 of the vaporized body 2
Attach the heat transfer plate ℃, and connect the heat transfer rod to the heat transfer plate blade and vaporizer 2.
It is connected to the heat exchanger plate 33 by passing through it. Also heat transfer 1e
34 is connected to the heat exchanger plate (9) and a part thereof is inserted inside the vaporizer 2.
このような構造により伝熱棒おが燃焼室6で燃焼した火
炎や燃焼ガスから受領した熱は伝熱棒間を経て伝熱板間
と31とに熱を伝え、気化体2(こ熱を供給する。また
伝熱棒あが受領した熱も伝熱板間に伝えられ、伝熱板I
から気化体2に熱を供給するとともに気化体2の内部に
ある伝熱偉部34aからも供給する。したがって気化体
内の液体燃料に熱を供給する伝熱面が増加して液体燃料
の蒸発を促進させるので燃焼装置としての燃焼能力が向
上する。特に蒸発潜熱の大きな液体燃料、例えばメタノ
ールを燃焼させる場合とか、さらにはメタノールに水を
6加して燃焼させる場合、またはメタノールを改質する
改質装置など(こ有効である。With this structure, the heat received from the flame and combustion gas burned in the combustion chamber 6 by the heat transfer rods is transferred between the heat transfer plates and 31 through the heat transfer rods, and the heat is transferred to the vaporized body 2 (this heat is Also, the heat received by the heat transfer rod A is transferred between the heat transfer plates, and the heat transfer plate I
Heat is supplied to the vaporized body 2 from the vaporized body 2, and is also supplied from the heat transfer portion 34a inside the vaporized body 2. Therefore, the heat transfer surface that supplies heat to the liquid fuel in the vaporized body increases and evaporation of the liquid fuel is promoted, so that the combustion performance of the combustion device is improved. This is particularly effective when burning liquid fuel with a large latent heat of vaporization, such as methanol, when adding water to methanol and burning it, or when using a reformer to reform methanol.
なお、本実施例において伝熱棒あを伝熱板324こも接
続してもよい。In this embodiment, the heat transfer rods may also be connected to the heat transfer plates 324.
また、本実施例において伝熱板32を取除いて伝熱板ア
、34が伝熱板Iを貫通してその一部が気化体2の内部
にあるようにしても十分な効果が得られる。Further, in this embodiment, sufficient effects can be obtained even if the heat exchanger plates 32 are removed so that the heat exchanger plates A and 34 penetrate through the heat exchanger plates I and a portion thereof is inside the vaporizer 2. .
上記実施例では伝熱板を気化体2の燃焼室側の一面、ま
たは燃焼室側とファン側の二面に取付けているが、伝熱
板を気化体2のファン側に取付けた伝熱板32だけにし
ても十分な効果がある。これは気化体2を貫通して内部
にある伝熱棒部により直接気化体内の液体燃料を加熱し
ながら熱を伝熱板32に伝えられるためである。In the above embodiment, the heat transfer plate is attached to one side of the vaporizer 2 on the combustion chamber side, or on two sides of the combustion chamber side and the fan side, but the heat transfer plate is attached to the fan side of the vaporizer 2. Even if it is only 32, it has a sufficient effect. This is because the heat transfer rod section penetrating the vaporized body 2 and located inside the vaporized body 2 directly heats the liquid fuel in the vaporized body and transmits heat to the heat transfer plate 32 .
上記の実施例において伝熱棒31 、33 、34は良
熱伝導性の材料を使用しているが、ヒートパイプを使用
してもよい。ヒートパイプの熱伝達は鋼材のそれの10
〜100倍の能力を有し、またこの場合にはステンレス
等を管材として使用できるので、高温燃焼する燃焼装置
に有効である。In the above embodiment, the heat transfer rods 31, 33, and 34 are made of a material with good thermal conductivity, but heat pipes may also be used. The heat transfer of heat pipes is 10 times higher than that of steel materials.
It has up to 100 times the capacity, and in this case, stainless steel or the like can be used as the tube material, so it is effective for combustion equipment that burns at high temperatures.
以上の説明から明らかなようIこ、本発明によればセラ
ミック等の多孔質の気化体の少なくとも一部を伝熱部材
で覆い、さらにこの伝熱部材に接続し、気化体から燃焼
室に延びる伝熱部材を設けること(こより、燃焼室で燃
焼により生じた熱媒体の熱を燃焼室に延びる伝熱部材を
経て気化体を覆う伝熱部材から気化体内の液体燃料に供
給して蒸発を促進するので、未燃焼料がなくなり燃焼能
力が向上するとともtこ燃焼を正常、安定化できるので
燃焼効率が同上する。したがって燃焼装置を小型。As is clear from the above description, according to the present invention, at least a portion of a porous vaporized body made of ceramic or the like is covered with a heat transfer member, which is further connected to the heat transfer member, and extends from the vaporized body to the combustion chamber. Providing a heat transfer member (Thus, the heat of the heat medium generated by combustion in the combustion chamber is supplied to the liquid fuel in the vaporizer through the heat transfer member extending into the combustion chamber and covering the vaporizer to promote evaporation. As a result, there is no unburned fuel and the combustion capacity is improved, and combustion can be made normal and stable, resulting in higher combustion efficiency.Therefore, the combustion device can be made smaller.
軽量化するとともに安価にすることができる。また気化
体における燃焼時未燃焼料がな(なるので、生の液体燃
料の流出や排気口からの火炎の噴出もな(なるので、安
全性が向上するという効果もある。It can be made lighter and less expensive. Furthermore, since there is no unburned material during combustion in the vaporized substance, there is no leakage of raw liquid fuel or flame ejection from the exhaust port, which has the effect of improving safety.
81図は本発明の実施例による燃焼装置の断面図、第2
図は第1図のA−A断面図、第3図は本発明の異なる実
施例による燃焼装置の断面図、第4図は従来の燃焼装置
の断面図である。
1:燃焼装置、2:気化体、6:燃焼室、第
目
第
図
系
図FIG. 81 is a sectional view of a combustion device according to an embodiment of the present invention, the second
The figures are a sectional view taken along the line AA in FIG. 1, FIG. 3 is a sectional view of a combustion device according to a different embodiment of the present invention, and FIG. 4 is a sectional view of a conventional combustion device. 1: Combustion device, 2: Vaporizer, 6: Combustion chamber, 1st order diagram
Claims (1)
で燃焼により生じる熱媒体により気化して燃焼空気によ
り燃焼する燃焼装置において、気化体にこの気化体の少
なくとも一部を覆う伝熱部材と、この伝熱部材に接続し
気化体から燃焼室に延びる伝熱部材とを設けたことを特
徴とする燃焼装置。1) In a combustion device in which a porous vaporized body is impregnated with liquid fuel, vaporized by a heat medium generated by combustion in a combustion chamber, and combusted by combustion air, heat transfer that covers at least a part of the vaporized body A combustion device comprising: a member; and a heat transfer member connected to the heat transfer member and extending from the vaporized body to the combustion chamber.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP25823688A JPH02106603A (en) | 1988-10-13 | 1988-10-13 | combustion device |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP25823688A JPH02106603A (en) | 1988-10-13 | 1988-10-13 | combustion device |
Publications (1)
Publication Number | Publication Date |
---|---|
JPH02106603A true JPH02106603A (en) | 1990-04-18 |
Family
ID=17317415
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP25823688A Pending JPH02106603A (en) | 1988-10-13 | 1988-10-13 | combustion device |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH02106603A (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US10941935B2 (en) | 2016-12-01 | 2021-03-09 | Sango Co., Ltd. | Evaporation type burner |
-
1988
- 1988-10-13 JP JP25823688A patent/JPH02106603A/en active Pending
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US10941935B2 (en) | 2016-12-01 | 2021-03-09 | Sango Co., Ltd. | Evaporation type burner |
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