JP2006057921A - Combustion method and device for oil-water mixture - Google Patents

Combustion method and device for oil-water mixture Download PDF

Info

Publication number
JP2006057921A
JP2006057921A JP2004240647A JP2004240647A JP2006057921A JP 2006057921 A JP2006057921 A JP 2006057921A JP 2004240647 A JP2004240647 A JP 2004240647A JP 2004240647 A JP2004240647 A JP 2004240647A JP 2006057921 A JP2006057921 A JP 2006057921A
Authority
JP
Japan
Prior art keywords
oil
water
mixed fuel
combustion
tank
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.)
Granted
Application number
JP2004240647A
Other languages
Japanese (ja)
Other versions
JP3928969B2 (en
Inventor
Yukio Hanamoto
本 行 雄 花
Tetsuyuki Hanamoto
本 哲 行 花
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.)
HANAMOTO KENSETSU KK
Kajima Road Co Ltd
Original Assignee
HANAMOTO KENSETSU KK
Kajima Road Co Ltd
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 HANAMOTO KENSETSU KK, Kajima Road Co Ltd filed Critical HANAMOTO KENSETSU KK
Priority to JP2004240647A priority Critical patent/JP3928969B2/en
Publication of JP2006057921A publication Critical patent/JP2006057921A/en
Application granted granted Critical
Publication of JP3928969B2 publication Critical patent/JP3928969B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

Images

Landscapes

  • Spray-Type Burners (AREA)
  • Feeding And Controlling Fuel (AREA)
  • Mixers Of The Rotary Stirring Type (AREA)

Abstract

<P>PROBLEM TO BE SOLVED: To sufficiently mix an oil with water at a prescribed mixture ratio by only a physical stir, and to excellently combust an oil-water mixture thereof regardless of the mixing of the water to reduce an exhaust amount of air pollutant. <P>SOLUTION: In this combustion method for the oil-water mixture for mixing the oil with water and combusting it, the oil and the water are supplied to a stirring tank 1 at a ratio of 8:2 to 4:6 by a high pressure pump 15, and are stirred in the stirring tank by a stirring means 3 to form emulsified mixed fuel, and the mixed fuel is heated to a temperature of 200-400°C and is sent to a nozzle 28 at a pressure of 10-30 MPa, and is combusted together with heated air. <P>COPYRIGHT: (C)2006,JPO&NCIPI

Description

本発明は、油と水とを混合して燃焼させるための油水混合液の燃焼方法及び装置に関する。   The present invention relates to an oil / water mixture combustion method and apparatus for mixing and burning oil and water.

一般に油(本明細書で油とは、重質油を含む鉱油、軽油、灯油、重油、エンジン油、作動油、ギヤオイル、食料油及びこれらに類似の油、並びにこれらの廃油をいう)を燃料として用いて燃焼を行わせる場合、油に水を添加した上で混合燃料を乳化することにより効率的な燃焼結果が得られることが以前から知られており、さらに一般的に重質油の燃焼に際しては、大気汚染物質(窒素酸化物、硫黄酸化物、一酸化炭素、二酸化炭素等)の発生が懸念されるが、水添加燃料であればこれらの物質の発生も抑制されることも知られている(特許文献1)。   Fuel oil (general oil including heavy oil, light oil, kerosene, heavy oil, engine oil, hydraulic oil, gear oil, food oil and similar oils, and waste oil thereof) in general It has long been known that efficient combustion results can be obtained by emulsifying the mixed fuel after adding water to the oil, and more generally burning heavy oil. At that time, there are concerns about the generation of air pollutants (nitrogen oxides, sulfur oxides, carbon monoxide, carbon dioxide, etc.), but it is also known that the generation of these substances can be suppressed with water-added fuel. (Patent Document 1).

しかし、混合燃料を使用するには混合燃料の水・油混合比、混合燃料の中に含まれる油の細分化状態、混合燃料の温度、混合燃料の噴射後の拡散等、複数の要素が良好な状態を保たねばならない。従来は、水・油の混合状態とを保つため界面活性剤等の乳化剤を添加することにより水・油混合燃料を乳化して使用する例が一般的であった(1例として特許文献2)。   However, in order to use a mixed fuel, multiple factors such as the water / oil mixing ratio of the mixed fuel, the subdivision state of the oil contained in the mixed fuel, the temperature of the mixed fuel, and the diffusion after injection of the mixed fuel are good We must keep a good condition. Conventionally, an example of emulsifying a water / oil mixed fuel by adding an emulsifier such as a surfactant in order to maintain a mixed state of water / oil is generally used (Patent Document 2 as an example). .

乳化剤を添加して混合燃料を得るには乳化剤を定量供給しながら撹拌混合しなければならず、製造のための設備が必要となりその設備及び乳化剤の費用が燃料単価へ反映され、その分燃料費が高くなる。
特許第3236249号公報 特許第2655973号公報
In order to obtain a mixed fuel by adding an emulsifier, it is necessary to stir and mix while supplying a certain amount of the emulsifier, and equipment for production is required, and the cost of the equipment and the emulsifier is reflected in the unit price of fuel. Becomes higher.
Japanese Patent No. 3236249 Japanese Patent No. 25595973

上記乳化剤を添加せずに物理的な撹拌のみで乳化させた混合燃料の燃焼装置では、それ自体相応の効果を奏するが、乳化が十分行われ難く、また乳化された混合燃料が時間経過と共に水と油に分離しやすく、安定した燃料供給が困難であった。   A combustion apparatus for mixed fuel emulsified only by physical agitation without adding the above-mentioned emulsifier has a corresponding effect per se, but it is difficult to sufficiently emulsify, and the emulsified mixed fuel becomes water over time. It was easy to separate into oil and stable fuel supply was difficult.

本発明は、上記の点に鑑みてなされたもので、物理的な撹拌のみで油と水を所定の混合比で十分に混合し、その油水混合液の油水分離を防ぎつつ燃焼ノズルに供給し、水の混入に拘わらず良好な燃焼を行い大気汚染物質の排出量を可及的少量とした油水混合液の燃焼方法及び装置を提供することを目的とする。   The present invention has been made in view of the above points. Oil and water are sufficiently mixed at a predetermined mixing ratio only by physical stirring, and supplied to a combustion nozzle while preventing oil-water separation of the oil-water mixture. Another object of the present invention is to provide a method and apparatus for burning an oil / water mixture that achieves good combustion regardless of the mixing of water so that the amount of air pollutants discharged is as small as possible.

上記目的を達成するため本発明の油水混合液の燃焼方法は、油と水とを混合して燃焼させるための油水混合液の燃焼方法において、油と水とをそれぞれ定量ポンプで8:2ないし4:6の割合で撹拌槽に供給し、その撹拌槽において撹拌手段で撹拌して乳化した混合燃料とし、その混合燃料を圧力10ないし30MPaで、温度200ないし400℃に加熱してノズルに送り、加熱した空気と共に燃焼させる。   In order to achieve the above object, the method for combusting an oil / water mixture according to the present invention is an oil / water mixture combusting method for mixing and burning oil and water. The mixture is supplied to the agitation tank at a ratio of 4: 6 and mixed with the emulsification by stirring with the agitation means in the agitation tank. The mixed fuel is heated to a temperature of 200 to 400 ° C. at a pressure of 10 to 30 MPa and sent to the nozzle Burn with heated air.

また本発明の油水混合液の燃焼装置は、撹拌槽と、撹拌槽に油及び水をそれぞれ給送する定量ポンプと、撹拌槽内に回転可能に設けられて油と水の混合燃料を生成する撹拌手段と、撹拌槽内の混合燃料を送出する高圧ポンプと、一端部にノズル及び空気導入筒を有する燃焼室と、一端が高圧ポンプに接続され、中間加熱部が燃焼室の周壁に巻回され、他端がノズルに接続された燃料供給管と、一端がブロアーに接続され、中間加熱部が燃焼室の周壁に巻回され、他端が空気噴出口に接続された給気管とを備え、ノズルから高温高圧の混合燃料を空気導入筒からの高温空気とともに燃焼室内に噴射して燃焼する。   Further, the combustion apparatus for an oil / water mixture of the present invention generates a mixed fuel of oil and water by being provided in a stirring tank, a metering pump for feeding oil and water to the stirring tank, respectively, and rotatably provided in the stirring tank. Stirring means, a high-pressure pump for sending the mixed fuel in the stirring tank, a combustion chamber having a nozzle and an air introduction cylinder at one end, one end connected to the high-pressure pump, and an intermediate heating section wound around the peripheral wall of the combustion chamber A fuel supply pipe whose other end is connected to the nozzle, an air supply pipe whose one end is connected to the blower, the intermediate heating section is wound around the peripheral wall of the combustion chamber, and the other end is connected to the air outlet. The high-temperature and high-pressure mixed fuel is injected from the nozzle together with the high-temperature air from the air introduction cylinder into the combustion chamber and burned.

また前記撹拌槽の下部に貯留槽が付設され、前記撹拌手段は、ディスクとその周縁部から軸方向に延出する多数の羽根を有する3個のタービン型の撹拌翼とこれらの撹拌翼を支持回転する回転軸を有し、上部の2個の撹拌翼は撹拌槽内に配置されるとともに、これら2個の撹拌翼の間に複数の細長プレートが配設され、1個の撹拌翼は貯留槽内に配設され、貯留槽から高圧ポンプにより混合燃料が送出されるようにすることができる。   In addition, a storage tank is attached to the lower part of the stirring tank, and the stirring means supports three turbine-type stirring blades having a disk and a large number of blades extending in the axial direction from the peripheral edge thereof, and supports these stirring blades. The rotating blade has a rotating shaft, and the upper two stirring blades are disposed in the stirring tank, and a plurality of elongated plates are disposed between the two stirring blades, and one stirring blade is stored. It is arrange | positioned in a tank and it can be made to send mixed fuel from a storage tank with a high pressure pump.

本発明の実施に際して混合燃料の温度を200℃以下では燃焼が不安定となり、また400℃以上としても効率の変化はない。
そして圧力が10MPa以下では燃料が充分に霧化せず不安定な燃焼となり、また30MPa以上では機械的な強度上の問題が生ずる。
In the practice of the present invention, combustion becomes unstable when the temperature of the mixed fuel is 200 ° C. or lower, and there is no change in efficiency even when the temperature is 400 ° C. or higher.
When the pressure is 10 MPa or less, the fuel is not atomized sufficiently and unstable combustion occurs. When the pressure is 30 MPa or more, a problem in mechanical strength occurs.

本発明によれば、所定の混合比の水を混合燃料中に混入するので、混合燃料の燃焼後の排気中の大気汚染物質を極めて少量に低減することができる。
また、油と水の混合は物理的な撹拌のみで行い、油水分離を防ぎつつ安定してノズルから噴射燃焼することができ、界面活性剤等の乳化剤を要することなく、比較的低燃費で油水混合燃料を燃焼することができる。
According to the present invention, water having a predetermined mixing ratio is mixed into the mixed fuel, so that air pollutants in the exhaust gas after combustion of the mixed fuel can be reduced to a very small amount.
Oil and water are mixed only by physical agitation, and can be stably injected and burned from the nozzle while preventing separation of oil and water, without requiring an emulsifier such as a surfactant. The mixed fuel can be burned.

また、混合燃料を高温高圧状態でノズルから噴射すると共に、加熱された空気を噴射燃料の周囲から噴射するので、混合燃料はより細分化され高温状態で点火され
完全燃焼に近い燃焼を行うことができる。
In addition, since the mixed fuel is injected from the nozzle in a high temperature and high pressure state, and heated air is injected from the periphery of the injected fuel, the mixed fuel can be further subdivided and ignited in a high temperature state to perform combustion close to complete combustion. it can.

本発明による油水混合液の燃焼装置の実施形態について、図1〜図6を参照して説明する。   An embodiment of an oil / water mixture combustion apparatus according to the present invention will be described with reference to FIGS.

1は円筒形の撹拌槽で、この撹拌槽1には定量ポンプP1、P2により、それぞれ油及び水が所定の割合で給送される。撹拌槽1の下部に、これより大容量の貯留槽2が必要に応じ設けられる。これらの定量ポンプP1、P2は吐出量の比を一定にするために例えば機械的な連動又は電気的な制御を行っている。   Reference numeral 1 denotes a cylindrical stirring tank, and oil and water are fed to the stirring tank 1 at a predetermined ratio by metering pumps P1 and P2. A storage tank 2 having a larger capacity than this is provided below the stirring tank 1 as necessary. These metering pumps P1, P2 perform, for example, mechanical interlocking or electrical control in order to make the ratio of the discharge amounts constant.

撹拌槽1及び貯留槽2の内部に撹拌手段3が設けられている。撹拌手段3は好ましくは3個の撹拌翼4a、4b、4cを備え、回転軸5により同軸上に支持されている。各撹拌翼4a、4b、4cは、円形のディスク6と多数の羽根7を有してタービン型翼形状をしている。各羽根7はディスク6の周縁部から軸方向に双方向(図示)若しくはいずれか一方に延出され、半径方向からみて略台形、長方形、三角形等の多角形に形成される。   Stirring means 3 is provided inside the stirring tank 1 and the storage tank 2. The stirring means 3 is preferably provided with three stirring blades 4 a, 4 b, 4 c and is supported coaxially by the rotating shaft 5. Each of the stirring blades 4a, 4b, 4c has a circular disk 6 and a large number of blades 7 and has a turbine blade shape. Each blade 7 extends bi-directionally (in the drawing) in the axial direction from the peripheral edge of the disk 6 or one of them, and is formed into a polygonal shape such as a substantially trapezoid, a rectangle, or a triangle as viewed from the radial direction.

上部の2個の撹拌翼4a、4b(全体を示す場合は符号4を用いる)は撹拌槽1内に配設され、これらの撹拌翼4間に細長のプレート8が設けられている。他の1個の撹拌翼4cは貯留槽2内に配設されている。撹拌槽1の上部に軸5を回転駆動する駆動モータ9が設けられ、回転軸5の下端はフートベアリング10により回転自在に支持されている。
一番上の攪拌翼4aは下方に混合燃料を降ろすものであり、そのような作用に適する構造に作られている。
2番目の攪拌翼4bは混合効果を高めるものであり、狭い穴Hに押し込む作用をしている。この狭い穴Hにより混合燃料は比較的に長時間この攪拌翼4bで混合される。一番下の攪拌翼4cは油と水とが分離しないように攪拌するものである。
Two upper stirring blades 4 a and 4 b (reference numeral 4 is used to show the whole) are disposed in the stirring tank 1, and an elongated plate 8 is provided between the stirring blades 4. Another one stirring blade 4 c is arranged in the storage tank 2. A drive motor 9 that rotationally drives the shaft 5 is provided in the upper part of the stirring tank 1, and the lower end of the rotary shaft 5 is rotatably supported by a foot bearing 10.
The uppermost stirring blade 4a is for lowering the mixed fuel downward, and has a structure suitable for such an action.
The second stirring blade 4b enhances the mixing effect and acts to push into the narrow hole H. Due to the narrow hole H, the mixed fuel is mixed with the stirring blade 4b for a relatively long time. The lowermost stirring blade 4c stirs so that oil and water are not separated.

円筒形の撹拌槽1内において油と水は、撹拌翼4により剪断力を受けながら撹拌され物理的に混合され、効率的に乳化されて混合燃料が生成される。そして混合燃料は貯留槽2に移送され、供給量を調整されながら後述の燃焼室へ送給される。撹拌槽1の容積を消費量に合わせることにより、時間と共に起きる浮上油の発生を押さえることができる。なお、この攪拌翼4は図6に示されているように羽根7の枚数が3〜8枚であり、その回転数は約900〜1200回/分で回転するのが好ましい。この羽根による攪拌は、燃料がゲル化するのを防止することもできる。   In the cylindrical stirring tank 1, oil and water are stirred and physically mixed while receiving a shearing force by the stirring blade 4, and are efficiently emulsified to produce a mixed fuel. Then, the mixed fuel is transferred to the storage tank 2 and supplied to a combustion chamber described later while the supply amount is adjusted. By adjusting the volume of the stirring tank 1 to the amount of consumption, generation | occurrence | production of the floating oil which occurs with time can be suppressed. As shown in FIG. 6, the stirring blade 4 has 3 to 8 blades 7 and preferably rotates at about 900 to 1200 times / minute. The stirring by the blades can also prevent the fuel from gelling.

貯留槽2の下部に吐出管11が設けられ、この吐出管11に送出管12、点火用油管13、ドレーン管14が連結されている。送出管12に高圧ポンプ15が設けられ、貯留槽2の下部から吐出管11、送出管12を経て送られてくる混合燃料を高圧ポンプ15により送出される。16〜18は各管を開閉するためのバルブレバー、19はフィルターである。   A discharge pipe 11 is provided below the storage tank 2, and a discharge pipe 12, an ignition oil pipe 13, and a drain pipe 14 are connected to the discharge pipe 11. A high pressure pump 15 is provided in the delivery pipe 12, and the mixed fuel sent from the lower part of the storage tank 2 through the discharge pipe 11 and the delivery pipe 12 is delivered by the high pressure pump 15. Reference numerals 16 to 18 are valve levers for opening and closing each pipe, and 19 is a filter.

燃焼室の点火時は、バルブレバー16により関連のバルブを閉じ、バルブレバー17により油管13のバルブを開放して、点火性の良好な油、例えばA重油は点火用油管13から燃料送出管12を介して、高圧ポンプ15により送出される。点火後、燃焼室内が十分な燃焼温度に達すると、バルブレバー17により点火用油管13のバルブを閉じ、バルブレバー16により吐出管11のバルブを開放し、貯留槽2からの混合燃料は管11、12を介して高圧ポンプ15により送出される。   When the combustion chamber is ignited, the associated valve is closed by the valve lever 16 and the valve of the oil pipe 13 is opened by the valve lever 17. Is sent out by the high-pressure pump 15. When the combustion chamber reaches a sufficient combustion temperature after ignition, the valve of the ignition oil pipe 13 is closed by the valve lever 17, the valve of the discharge pipe 11 is opened by the valve lever 16, and the mixed fuel from the storage tank 2 passes through the pipe 11. , 12 through a high-pressure pump 15.

燃焼室20の一端の点火筒部20aには、開口21に空気導入筒22が設けられている。耐熱性の給気管23の一端はブロアー24に接続され、中間加熱部25は燃焼室20の燃焼筒部20bの周壁にコイル状に巻回埋設されており、他端は空気導入筒22に接続されている。具体例として燃焼室の周壁は例えば二重構造の燃焼筒で形成され、中間加熱部25は内壁の周囲にコイル状に巻回され、外壁で被覆される。   An air introduction cylinder 22 is provided in the opening 21 in the ignition cylinder portion 20 a at one end of the combustion chamber 20. One end of the heat-resistant air supply pipe 23 is connected to the blower 24, the intermediate heating part 25 is coiled and embedded in the peripheral wall of the combustion cylinder part 20 b of the combustion chamber 20, and the other end is connected to the air introduction cylinder 22. Has been. As a specific example, the peripheral wall of the combustion chamber is formed of, for example, a double-structured combustion cylinder, and the intermediate heating unit 25 is wound around the inner wall in a coil shape and covered with the outer wall.

ブロアー24から送風される二次空気は、給気管23のコイル状の中間加熱部25において燃焼室20の燃焼筒部20bからの輻射熱等の伝達熱により高温に加熱され、燃焼室内に渦巻き発生器27により渦流となって噴出され、前方に配置されたノズル28から噴射される燃料を巻き込む。二次空気量はブロアー24に付設されたダンパにより調整される。   The secondary air blown from the blower 24 is heated to a high temperature by the transfer heat such as radiant heat from the combustion cylinder portion 20b of the combustion chamber 20 in the coil-shaped intermediate heating portion 25 of the supply pipe 23, and a vortex generator is generated in the combustion chamber. The fuel 27 is ejected as a vortex by the nozzle 27 and is injected from the nozzle 28 disposed in the front. The amount of secondary air is adjusted by a damper attached to the blower 24.

空気導入筒22の先端部中央に燃料を噴射するノズル28が配設されている。燃料供給管29の両端は、ノズル28及び前記高圧ポンプ15にそれぞれ接続され、中間加熱部30は燃焼室20の周壁に、給気管の中間加熱部25と同様にしてコイル状に巻回埋設されている。高圧ポンプ15から送給される混合燃料はコイル状中間加熱部30において燃焼室20の燃焼筒部20bからの伝達熱により加熱され、高温高圧でノズル28から燃焼室内に噴射される。   A nozzle 28 for injecting fuel is disposed at the center of the tip of the air introduction tube 22. Both ends of the fuel supply pipe 29 are connected to the nozzle 28 and the high-pressure pump 15, respectively. The intermediate heating unit 30 is wound around the peripheral wall of the combustion chamber 20 in the same manner as the intermediate heating unit 25 of the air supply pipe. ing. The mixed fuel fed from the high-pressure pump 15 is heated by the heat transferred from the combustion cylinder portion 20b of the combustion chamber 20 in the coiled intermediate heating portion 30, and is injected from the nozzle 28 into the combustion chamber at a high temperature and high pressure.

31は点火用のパイロットバーナである。燃焼室20内において、混合燃料の燃焼に先立って、パイロットバーナ31においてプロパンガス、鉱油等がスパークプラグにより点火され、その火炎が燃焼室内に噴射される。一方バルブレバー17の前記操作により点火用油、例えばA重油が高圧ポンプ15からノズル28へ送給され、ノズル28から噴射されてパイロットバーナ31からの火炎により点火される。   31 is a pilot burner for ignition. In the combustion chamber 20, prior to the combustion of the mixed fuel, propane gas, mineral oil or the like is ignited by the spark plug in the pilot burner 31, and the flame is injected into the combustion chamber. On the other hand, by the operation of the valve lever 17, ignition oil, for example, A heavy oil is supplied from the high pressure pump 15 to the nozzle 28, injected from the nozzle 28, and ignited by the flame from the pilot burner 31.

点火用油により燃焼室内が高温に達すると、バルブレバー16、17の操作により、高圧ポンプ15からの点火用油の送給は混合燃料の送給に切り替えられ、混合燃料はノズル28から燃焼室20内に噴射され、燃焼室20内において燃焼され始める。その際高圧ポンプ15及び中間加熱部により高圧高温とされた混合燃料は、ノズル28から瞬時に大気に放出されるため激しい噴流となり、空気との混合が助長され、良好な燃焼を可能とする。燃焼室20の内部が十分に高温となり、混合燃料の燃焼が定常的になり、パイロットバーナ31が不要になると停止される。燃料の噴出量は、高圧ポンプ15の回転数を変えるより、ノズルの口径サイズの異なるものと交換することが好ましい。   When the combustion chamber reaches a high temperature due to the ignition oil, the operation of the valve levers 16 and 17 switches the supply of the ignition oil from the high pressure pump 15 to the supply of the mixed fuel, and the mixed fuel is supplied from the nozzle 28 to the combustion chamber. 20 is injected into the combustion chamber 20 and begins to burn in the combustion chamber 20. At that time, the mixed fuel that has been brought to a high pressure and high temperature by the high pressure pump 15 and the intermediate heating section is instantaneously discharged from the nozzle 28 to the atmosphere, so that it becomes a vigorous jet, which facilitates mixing with the air and enables good combustion. When the inside of the combustion chamber 20 becomes sufficiently high in temperature, combustion of the mixed fuel becomes steady, and the pilot burner 31 is no longer needed. It is preferable to replace the fuel ejection amount with a nozzle having a different nozzle size rather than changing the rotational speed of the high-pressure pump 15.

32は燃焼室20の端部に適宜付設された熱負荷で、例えばボイラとして給湯器としたり、蒸気発生器とすることができる。燃焼室からの排気は熱負荷32を通過した後、図示しない排気筒を通って外部へ排出される。熱負荷32は図示のように燃焼室端部に代えて、燃焼室の周壁に付設してもよい。   Reference numeral 32 denotes a heat load appropriately attached to the end portion of the combustion chamber 20. For example, the boiler 32 can be a hot water heater or a steam generator. Exhaust gas from the combustion chamber passes through the heat load 32 and is then discharged to the outside through an exhaust pipe (not shown). The heat load 32 may be attached to the peripheral wall of the combustion chamber instead of the end portion of the combustion chamber as shown.

次に、本発明による油水混合液の燃焼方法の実施形態について説明する。
油と水は定量ポンプ1、2により8:2ないし4:6の割合で、撹拌槽1に供給される。撹拌槽1内において撹拌手段3により油と水は物理的ないし機械的に撹拌され、乳化されて混合燃料が生成される。混合燃料は、貯留槽2に移送され撹拌翼4により乳化状態が維持されながら、高圧ポンプ15へ送出される。
Next, an embodiment of an oil-water mixture combustion method according to the present invention will be described.
Oil and water are supplied to the stirring tank 1 at a ratio of 8: 2 to 4: 6 by the metering pumps 1 and 2. In the agitation tank 1, the oil and water are physically or mechanically agitated by the agitation means 3 and emulsified to produce a mixed fuel. The mixed fuel is transferred to the storage tank 2 and delivered to the high-pressure pump 15 while the emulsified state is maintained by the stirring blade 4.

次に混合燃料は高圧ポンプ15により、送出圧を10ないし30MPaとして、燃料供給管29を介してノズル28に供給される。また、混合燃料は燃焼室20の周壁に巻回された燃料供給管29の中間加熱部30において、燃焼室20からの伝達熱により200ないし400℃に加熱される。実験では350ないし380℃の温度範囲で良好な結果が得られた。   Next, the mixed fuel is supplied to the nozzle 28 through the fuel supply pipe 29 by the high pressure pump 15 at a delivery pressure of 10 to 30 MPa. Further, the mixed fuel is heated to 200 to 400 ° C. by the heat transferred from the combustion chamber 20 in the intermediate heating portion 30 of the fuel supply pipe 29 wound around the peripheral wall of the combustion chamber 20. In the experiment, good results were obtained in the temperature range of 350 to 380 ° C.

一方、ブロアー24から送給される空気は、給気管23を通り、その中間加熱部25において燃焼室20からの伝達熱により混合燃料と同様の温度に加熱されて、空気導入筒22へ導入される。空気導入筒22へ導入された空気は、渦巻き発生器27により渦流とされてノズル28から噴出され、混合燃料を巻き込みながら燃焼室内へ噴出され、混合燃料の燃焼が助長される。   On the other hand, the air fed from the blower 24 passes through the air supply pipe 23, is heated to the same temperature as the mixed fuel by the heat transferred from the combustion chamber 20 in the intermediate heating section 25, and is introduced into the air introduction cylinder 22. The The air introduced into the air introduction cylinder 22 is swirled by the swirl generator 27 and ejected from the nozzle 28 and is ejected into the combustion chamber while entraining the mixed fuel, thereby promoting the combustion of the mixed fuel.

廃油と水とを撹拌槽1において撹拌混合して混合燃料を生成し、高圧ポンプ15により高圧で吐出し、ノズル28により高温高圧の混合燃料を燃焼室20内で燃焼した。廃油と水の比は廃油3:水7、廃油5:水5、廃油7:水3、廃油10:水0と混合比を変えて混合燃料を生成し、燃焼させた。その結果は、表1に示される。
表1

Figure 2006057921
Waste oil and water were agitated and mixed in the agitation tank 1 to produce a mixed fuel, discharged at high pressure by the high-pressure pump 15, and the high-temperature and high-pressure mixed fuel was combusted in the combustion chamber 20 by the nozzle 28. The ratio of waste oil to water was changed to waste oil 3: water 7, waste oil 5: water 5, waste oil 7: water 3, waste oil 10: water 0, and mixed fuel was produced and burned. The results are shown in Table 1.
Table 1
Figure 2006057921

この表1に示されるように、廃油3:水7、廃油5:水5、廃油7:水3では窒素酸化物、二酸化硫黄は大気汚染防止法の基準値以下に収まっている。これらの値は図7のようにプロットされ、廃油と水の比は、8:2〜4:6の範囲が良好な結果が得られると考えられる。即ち、廃油の量が80%を越えると、窒素酸化物、二酸化硫黄の量が増加して大気汚染物質の発生を抑制することが困難である。また、混合比が3:7の場合、即ち廃油の量が30%の場合は、火炎の状態が不安定となり、A重油では火炎の問題はなく、油の種類により燃焼状態が異なる。これらの事情を考慮すると、油の下限は40%以上として、混合比を4:6にすることで良好な燃焼を行うことができる。また廃油が、70%を越えると窒素酸化物や二酸化硫黄の量が増える傾向にあるので、廃油は70%以下にすることが好ましく、廃油以外の油は廃油よりも大気汚染物質を比較的少量含有するので、油と水との混合比は7:3〜4:6とすることが好ましい。   As shown in Table 1, in waste oil 3: water 7, waste oil 5: water 5, waste oil 7: water 3, nitrogen oxides and sulfur dioxide are within the standard values of the Air Pollution Control Law. These values are plotted as shown in FIG. 7, and the ratio of waste oil to water is considered to be good when the range of 8: 2 to 4: 6 is obtained. That is, when the amount of waste oil exceeds 80%, the amount of nitrogen oxides and sulfur dioxide increases and it is difficult to suppress the generation of air pollutants. In addition, when the mixing ratio is 3: 7, that is, when the amount of waste oil is 30%, the flame state becomes unstable, and there is no flame problem with heavy fuel oil A, and the combustion state varies depending on the type of oil. Considering these circumstances, the lower limit of the oil is set to 40% or more, and a favorable combustion can be performed by setting the mixing ratio to 4: 6. Also, if the amount of waste oil exceeds 70%, the amount of nitrogen oxides or sulfur dioxide tends to increase. Therefore, it is preferable to reduce the amount of waste oil to 70% or less, and oil other than waste oil contains a relatively small amount of air pollutants than waste oil. Since it contains, it is preferable that the mixing ratio of oil and water shall be 7: 3-4: 6.

また、一酸化炭素及び二酸化炭素は廃油の混合比が30〜70%においても、100%の場合と殆ど異ならず、略完全燃焼が行われている。
なお、燃料供給管29の管内圧力は、20MPaの場合が良好であったが10ないし30MPaに変化させても略同様の結果が得られた。
Further, carbon monoxide and carbon dioxide are almost completely different from each other even when the mixing ratio of waste oil is 30 to 70%, which is almost 100%.
The internal pressure of the fuel supply pipe 29 was good when it was 20 MPa, but substantially the same result was obtained even when it was changed from 10 to 30 MPa.

表1から分かるように温度はノズルから1m離れた位置で約1000〜1400℃であることが確認される。炎温度は水を混合することにより物理的に廃油100%時よりも降下するが、1000℃を越えており、使用用途を見極めれば十分といえる。燃焼室運転中に周囲において燃焼ガスの臭いを感覚的に確認したが、異臭は全く知覚されなかった。この結果は燃料供給管内において油水混合燃料の水の部分が高温(200〜400℃)、高圧(10〜30MPa)において超臨界水として挙動するものと推定される。   As can be seen from Table 1, it is confirmed that the temperature is about 1000 to 1400 ° C. at a position 1 m away from the nozzle. The flame temperature is physically lowered by mixing water with that of the waste oil at 100%, but exceeds 1000 ° C., and it can be said that it is sufficient to determine the intended use. While the combustion chamber was operating, the smell of combustion gas was sensibly confirmed in the surroundings, but no off-flavor was perceived. This result is presumed that the water portion of the oil / water mixed fuel in the fuel supply pipe behaves as supercritical water at high temperature (200 to 400 ° C.) and high pressure (10 to 30 MPa).

本発明の燃焼装置の一実施形態を示す模式図。The schematic diagram which shows one Embodiment of the combustion apparatus of this invention. 図1の燃焼室部を示す詳細正面図。The detailed front view which shows the combustion chamber part of FIG. 図1の撹拌槽部を示す詳細正面図。The detailed front view which shows the stirring tank part of FIG. 図3のB−B線に沿う図。The figure which follows the BB line of FIG. 図3の撹拌手段を示す図。The figure which shows the stirring means of FIG. 図5の撹拌翼の拡大斜視図。The expansion perspective view of the stirring blade of FIG. 本発明の燃焼方法による燃焼結果を示すグラフThe graph which shows the combustion result by the combustion method of this invention

符号の説明Explanation of symbols

1・・・撹拌槽
2・・・貯留槽
3・・・撹拌手段
4a、4b、4c・・・撹拌翼
5・・・回転軸
6・・・ディスク
7・・・羽根
8・・・プレート
11・・・吐出管
12・・・送出管
13・・・点火用油管
14・・・ドレーン管
15・・・高圧ポンプ
16、17、18・・・バルブレバー
20・・・燃焼室
21・・・開口部
22・・・空気導入筒
23・・・給気管
24・・・ブロアー
25、30・・・中間加熱部
27・・・渦巻き発生器
28・・・ノズル
29・・・燃料供給管
DESCRIPTION OF SYMBOLS 1 ... Stirring tank 2 ... Storage tank 3 ... Stirring means 4a, 4b, 4c ... Stirring blade 5 ... Rotating shaft 6 ... Disk 7 ... Blade 8 ... Plate 11 ... discharge pipe 12 ... delivery pipe 13 ... ignition oil pipe 14 ... drain pipe 15 ... high pressure pumps 16, 17, 18 ... valve lever 20 ... combustion chamber 21 ... Opening 22 ... Air introduction tube 23 ... Air supply pipe 24 ... Blower 25, 30 ... Intermediate heating part 27 ... Swirl generator 28 ... Nozzle 29 ... Fuel supply pipe

Claims (3)

油と水とを混合して燃焼させるための油水混合液の燃焼方法において、油と水とをそれぞれ定量ポンプで8:2ないし4:6の割合で撹拌槽に供給し、その撹拌槽において撹拌手段で撹拌して乳化した混合燃料とし、その混合燃料を圧力10ないし30MPaで、温度200ないし400℃に加熱してノズルに送り、加熱した空気と共に燃焼させることを特徴とする油水混合液の燃焼方法。 In the combustion method of an oil / water mixture for mixing oil and water for combustion, oil and water are respectively supplied to a stirring tank at a ratio of 8: 2 to 4: 6 by a metering pump and stirred in the stirring tank. Combustion of an oil-water mixture characterized in that the mixed fuel is agitated and emulsified by means, and the mixed fuel is heated to a temperature of 200 to 400 ° C. at a pressure of 10 to 30 MPa, sent to a nozzle, and combusted with the heated air. Method. 撹拌槽と、撹拌槽に油及び水をそれぞれ給送する定量ポンプと、撹拌槽内に回転可能に設けられて油と水の混合燃料を生成する撹拌手段と、撹拌槽内の混合燃料を送出する高圧ポンプと、一端部にノズル及び空気導入筒を有する燃焼室と、一端が高圧ポンプに接続され、中間加熱部が燃焼室の周壁に巻回され、他端がノズルに接続された燃料供給管と、一端がブロアーに接続され、中間加熱部が燃焼室の周壁に巻回され、他端が空気噴出口に接続された給気管とを備え、ノズルから高温高圧の混合燃料を空気導入筒からの高温空気とともに燃焼室内に噴射して燃焼することを特徴とする油水混合液の燃焼装置。 An agitation tank, a metering pump that supplies oil and water to the agitation tank, an agitation means that is rotatably provided in the agitation tank and generates a mixed fuel of oil and water, and a mixed fuel in the agitation tank is sent out A high-pressure pump, a combustion chamber having a nozzle and an air introduction cylinder at one end, a fuel supply in which one end is connected to the high-pressure pump, an intermediate heating unit is wound around the peripheral wall of the combustion chamber, and the other end is connected to the nozzle A pipe, one end connected to the blower, an intermediate heating unit wound around the peripheral wall of the combustion chamber, and the other end connected to the air outlet, and a high-temperature high-pressure mixed fuel from the nozzle to the air introduction cylinder An oil / water mixture combustion apparatus for injecting and combusting together with high-temperature air from a combustion chamber. 前記撹拌槽の下部に貯留槽が付設され、前記撹拌手段は、ディスクとその周縁部から軸方向に延出する多数の羽根を有する3個のタービン型の撹拌翼とこれらの撹拌翼を支持回転する回転軸を有し、上部の2個の撹拌翼は撹拌槽内に配置されるとともに、これら2個の撹拌翼の間に複数の細長プレートが配設され、1個の撹拌翼は貯留槽内に配設され、貯留槽から高圧ポンプにより混合燃料が送出されるようにしたことを特徴とする請求項2の油水混合液の燃焼装置。 A storage tank is attached to the lower part of the agitation tank, and the agitation means supports and rotates three turbine-type agitation blades having a disk and a large number of blades extending in the axial direction from the periphery thereof. The upper two stirring blades are disposed in the stirring tank, and a plurality of elongated plates are disposed between the two stirring blades. One stirring blade is a storage tank. The oil / water mixture combustion apparatus according to claim 2, wherein the mixed fuel is sent out from the storage tank by a high-pressure pump.
JP2004240647A 2004-08-20 2004-08-20 Oil-water mixture combustion equipment Expired - Fee Related JP3928969B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP2004240647A JP3928969B2 (en) 2004-08-20 2004-08-20 Oil-water mixture combustion equipment

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP2004240647A JP3928969B2 (en) 2004-08-20 2004-08-20 Oil-water mixture combustion equipment

Publications (2)

Publication Number Publication Date
JP2006057921A true JP2006057921A (en) 2006-03-02
JP3928969B2 JP3928969B2 (en) 2007-06-13

Family

ID=36105532

Family Applications (1)

Application Number Title Priority Date Filing Date
JP2004240647A Expired - Fee Related JP3928969B2 (en) 2004-08-20 2004-08-20 Oil-water mixture combustion equipment

Country Status (1)

Country Link
JP (1) JP3928969B2 (en)

Cited By (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR100836835B1 (en) * 2007-03-29 2008-06-12 김일룡 A burning system for emulsified fuel
KR100859220B1 (en) 2007-10-10 2008-09-18 주식회사 아이씨엘뉴텍 Combustion system for mixed fuel and water
JP2010133682A (en) * 2008-12-08 2010-06-17 Niigata Power Systems Co Ltd Combustion treatment device for liquid voc (volatile organic compound)
KR100980377B1 (en) * 2009-10-30 2010-09-07 박형호 The apparatus burn after mix oil and water
JP2011191053A (en) * 2011-05-31 2011-09-29 Miike Iron Works Co Ltd Burner unit
KR101103037B1 (en) 2009-02-26 2012-01-05 최이교 Combustion device for mixed fuel ana water
CN102449397A (en) * 2009-06-23 2012-05-09 朱圣镐 Burner using plasma
CN103225813A (en) * 2013-04-26 2013-07-31 如皋市双马化工有限公司 Combustion method for refined glycerin black foot
CN113041873A (en) * 2021-03-19 2021-06-29 重庆国际复合材料股份有限公司 Emulsion constant temperature circulation shearing mechanism

Cited By (11)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR100836835B1 (en) * 2007-03-29 2008-06-12 김일룡 A burning system for emulsified fuel
KR100859220B1 (en) 2007-10-10 2008-09-18 주식회사 아이씨엘뉴텍 Combustion system for mixed fuel and water
WO2009048200A1 (en) * 2007-10-10 2009-04-16 Iclnewtec Co., Ltd Combustion system for mixed fuel and water
JP2010133682A (en) * 2008-12-08 2010-06-17 Niigata Power Systems Co Ltd Combustion treatment device for liquid voc (volatile organic compound)
KR101103037B1 (en) 2009-02-26 2012-01-05 최이교 Combustion device for mixed fuel ana water
CN102449397A (en) * 2009-06-23 2012-05-09 朱圣镐 Burner using plasma
JP2012531572A (en) * 2009-06-23 2012-12-10 チュ,スンホ Burner using plasma
KR100980377B1 (en) * 2009-10-30 2010-09-07 박형호 The apparatus burn after mix oil and water
JP2011191053A (en) * 2011-05-31 2011-09-29 Miike Iron Works Co Ltd Burner unit
CN103225813A (en) * 2013-04-26 2013-07-31 如皋市双马化工有限公司 Combustion method for refined glycerin black foot
CN113041873A (en) * 2021-03-19 2021-06-29 重庆国际复合材料股份有限公司 Emulsion constant temperature circulation shearing mechanism

Also Published As

Publication number Publication date
JP3928969B2 (en) 2007-06-13

Similar Documents

Publication Publication Date Title
EP2370681B1 (en) Method of operating a fuel oxidizer in multiple operating modes and fuel oxidizer system
EP2278223A1 (en) Combustion method and apparatus
JP2010159957A (en) Method and apparatus for injecting fuel in turbine engine
JP3928969B2 (en) Oil-water mixture combustion equipment
JP2004263572A (en) Cogeneration system
JP5368063B2 (en) Oily substance combustion apparatus and oily substance combustion method
JP5153918B2 (en) Burner unit
JP2009174723A (en) Combustion burner and burner unit
KR100264417B1 (en) Emulsion fuel production supply apparatus
JP3142680U (en) Horizontal combustion furnace
JP2006112666A (en) Combustion device provided with emulsified fuel supply system
AU2004293014A1 (en) A method and device for combusting liquid fuels using hydrogen
KR101049715B1 (en) A hot air fan
JP2011021803A (en) Water oil combustion device
JP5403546B2 (en) Method and apparatus for supplying fuel to combustor
KR102531566B1 (en) Gas emulsion combustion device
KR200417952Y1 (en) Combustion apparatus
JP5403552B2 (en) Boiler fuel supply system with water added to fuel oil
KR200417812Y1 (en) Combustion apparatus
JP7150291B2 (en) Combustion device
JP3737435B2 (en) Vaporized gas mixed combustion apparatus and method
KR20120063096A (en) Producing and feeding equipment for emulsion fuel oil and producing and feeding methode using the same
JP2006112664A (en) Emulsion fuel combustion device
JP2011080448A (en) Plenum air preheat for cold startup of liquid-fueled pulse detonation engine
KR20030095555A (en) waste oil burner system

Legal Events

Date Code Title Description
A977 Report on retrieval

Free format text: JAPANESE INTERMEDIATE CODE: A971007

Effective date: 20060727

A131 Notification of reasons for refusal

Free format text: JAPANESE INTERMEDIATE CODE: A131

Effective date: 20060801

A521 Written amendment

Free format text: JAPANESE INTERMEDIATE CODE: A523

Effective date: 20060921

TRDD Decision of grant or rejection written
A01 Written decision to grant a patent or to grant a registration (utility model)

Free format text: JAPANESE INTERMEDIATE CODE: A01

Effective date: 20070302

A61 First payment of annual fees (during grant procedure)

Free format text: JAPANESE INTERMEDIATE CODE: A61

Effective date: 20070302

R150 Certificate of patent or registration of utility model

Free format text: JAPANESE INTERMEDIATE CODE: R150

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20100316

Year of fee payment: 3

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20110316

Year of fee payment: 4

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20110316

Year of fee payment: 4

R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

S111 Request for change of ownership or part of ownership

Free format text: JAPANESE INTERMEDIATE CODE: R313117

R350 Written notification of registration of transfer

Free format text: JAPANESE INTERMEDIATE CODE: R350

LAPS Cancellation because of no payment of annual fees