JPH04214106A - Method of burning foamed liquid fuel and its method - Google Patents

Method of burning foamed liquid fuel and its method

Info

Publication number
JPH04214106A
JPH04214106A JP3037515A JP3751591A JPH04214106A JP H04214106 A JPH04214106 A JP H04214106A JP 3037515 A JP3037515 A JP 3037515A JP 3751591 A JP3751591 A JP 3751591A JP H04214106 A JPH04214106 A JP H04214106A
Authority
JP
Japan
Prior art keywords
combustion
foaming
porous element
liquid fuel
fuel
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
JP3037515A
Other languages
Japanese (ja)
Other versions
JP2688120B2 (en
Inventor
Norio Yasuzawa
安沢 典男
Kouji Adachi
安達 鋼治
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.)
Nippon Steel Corp
Original Assignee
Nippon Steel Corp
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
Priority to KR1019910701141A priority Critical patent/KR950012775B1/en
Application filed by Nippon Steel Corp filed Critical Nippon Steel Corp
Priority to CA002049009A priority patent/CA2049009C/en
Priority to EP19910906260 priority patent/EP0478789A4/en
Priority to PCT/JP1991/000353 priority patent/WO1991014900A1/en
Priority to US07/741,503 priority patent/US5192203A/en
Publication of JPH04214106A publication Critical patent/JPH04214106A/en
Application granted granted Critical
Publication of JP2688120B2 publication Critical patent/JP2688120B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Classifications

    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23DBURNERS
    • F23D5/00Burners in which liquid fuel evaporates in the combustion space, with or without chemical conversion of evaporated fuel

Landscapes

  • Engineering & Computer Science (AREA)
  • Chemical & Material Sciences (AREA)
  • Combustion & Propulsion (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Wick-Type Burners And Burners With Porous Materials (AREA)
  • Evaporation-Type Combustion Burners (AREA)
  • Porous Artificial Stone Or Porous Ceramic Products (AREA)

Abstract

PURPOSE:To make the evaporation of the fuel easy and stabilize further the combustion by supplying air through a porous element to form foamed fuel uniformly, stabilizing the foaming property, and supplying the air required for complete combustion separately. CONSTITUTION:A wind box 7 for supplying the combustion air is provided outside a burner 4 that is positioned above an evaporation pan 3, and the liquid fuel is supplied to the upper section of a porous element 2 that is internally in contact with a foam forming device 1, and the fuel ascends in the state of foam that is a congregation of foams of small diameter by the air from a supply pipe 5 for the gas of foam formation. By the way the average diameter of the air pores in the porous element 2 that is provided below the recess 23 below the bottom face of the evaporation pan 3 is over 1mum and below 200mum. Accordingly the foams become a congregation of small foams by making the resistance of the gas for foaming small and limiting the superficial velocity through the porous element section 2, and it is possible to achieve a stable ignition and continuous combustion.

Description

【発明の詳細な説明】[Detailed description of the invention]

【0001】0001

【産業上の利用分野】本発明は、家庭用石油ストーブか
ら工業窯炉までの幅広い範囲における液体燃料特に、軽
質油燃料(灯油、軽油、等)を泡沫化して燃焼させる方
法およびその燃焼装置に関するものである。
[Industrial Application Field] The present invention relates to a method for foaming and burning liquid fuel, particularly light oil fuel (kerosene, light oil, etc.) for use in a wide range of applications from household kerosene stoves to industrial kilns, and a combustion apparatus for the same. It is something.

【0002】0002

【従来の技術】従来の燃焼は、液体燃料を直接気化させ
て燃焼させるか、または噴霧装置によって一度細かい霧
状に分裂させて燃焼させるかのいずれかの燃焼方法が用
いられている。本出願人は特開平1−95205号公報
で、液体燃料の燃焼量可変範囲の拡大とポット式や噴霧
燃焼方式の欠点を改善した全く新しい液体燃料の泡沫化
燃焼方式を提案した。
BACKGROUND OF THE INVENTION Conventional combustion methods include either directly vaporizing liquid fuel and burning it, or splitting it into fine mist using a spray device and then burning it. In Japanese Patent Application Laid-Open No. 1-95205, the present applicant proposed a completely new liquid fuel foam combustion method that expands the range of variable combustion amount of liquid fuel and improves the drawbacks of the pot type and spray combustion methods.

【0003】また、特開平2−21106号公報におい
て、泡沫生成器に使用する多孔質フィルター(エレメン
ト)を液体燃料の表面張力より臨界表面張力の低い表面
性状を有する物質とすることで、燃焼の消火時における
燃料の逆流を防止する燃焼装置を提案した。更に本出願
人は、特開平2−259311号公報において、燃焼器
と蒸発皿および泡沫生成器を近接して設け、泡沫生成器
内の多孔質エレメントの外側に液体燃料を供給し、内側
に発泡用の気体を供給して液体燃料を泡沫とし、燃料の
蒸発面積を著しく増加させ、しかる後直ちに燃焼させる
方法およびその装置を提案している。
Furthermore, in Japanese Patent Application Laid-Open No. 2-21106, the porous filter (element) used in the foam generator is made of a material having a surface property with a critical surface tension lower than that of the liquid fuel, thereby reducing combustion. We proposed a combustion device that prevents backflow of fuel when extinguishing a fire. Furthermore, in Japanese Patent Application Laid-open No. 2-259311, the present applicant has provided a combustor, an evaporation plate, and a foam generator in close proximity, supplies liquid fuel to the outside of a porous element in the foam generator, and supplies foam to the inside of the porous element. The present invention proposes a method and an apparatus for turning liquid fuel into foam by supplying a gas for use, significantly increasing the evaporation area of the fuel, and immediately combusting the fuel.

【0004】0004

【発明が解決しようとする課題】このような泡沫化燃焼
において、燃料供給量を一定にして気体供給管6からの
空気量を増加させすぎると、燃料が液滴となり不安定な
燃焼となる場合がある。液体燃料の泡沫化燃焼は、泡沫
生成器を構成する多孔質エレメントの平均気孔径や発泡
用気体の空塔速度(多孔質エレメントがないとして求め
た気体の流速)によって、その点火や継続燃焼の安定性
が大きく影響される。本発明は、泡沫燃料の均一性およ
び発泡性の安定化を達成し、燃料の蒸発を容易にしてよ
り一層の安定燃焼を図る燃焼方法およびその装置を提供
するものである。ここで、泡沫燃料の均一性とは、泡沫
(気泡の集合体)を形成する各々の気泡の直径のばらつ
きが小さいことをいう。また、発泡性の安定化とは、各
々の気泡の直径が小さくて、発泡倍率(泡の体積/液の
体積)が安定して大きいことをいう。
[Problem to be Solved by the Invention] In such foaming combustion, if the amount of air from the gas supply pipe 6 is increased too much while keeping the fuel supply amount constant, the fuel may become droplets, resulting in unstable combustion. There is. The foaming combustion of liquid fuel depends on the average pore diameter of the porous elements that make up the foam generator and the superficial velocity of the foaming gas (the gas flow velocity calculated assuming that there is no porous element). Stability is greatly affected. The present invention provides a combustion method and apparatus that achieves uniformity and stabilization of foaming properties of foamy fuel, facilitates fuel evaporation, and achieves even more stable combustion. Here, the uniformity of foamy fuel means that the variation in the diameter of each bubble forming the foam (aggregation of bubbles) is small. Furthermore, stabilization of foamability means that the diameter of each bubble is small and the foaming ratio (volume of foam/volume of liquid) is stably large.

【0005】[0005]

【課題を解決するための手段】本発明は液体燃料の泡沫
化燃焼において、空気を平均気孔径(目開き)が1μm
以上、200μm以下である多孔質エレメントを通して
液体燃料中に供給し、燃料を直径の小さな気泡の集合体
からなる泡沫とした後、該泡沫燃料を燃焼器で完全燃焼
するのに必要な空気を別に供給して燃焼させる方法およ
びそれを具現化する装置であり、発泡用気体が多孔質エ
レメントを通過する見掛けの速度、すなわち空塔速度が
0.01m/s以上、1m/s以下であることを含むも
のである。
[Means for Solving the Problems] The present invention provides a method for converting air into foam with an average pore size (opening) of 1 μm in the foaming combustion of liquid fuel.
As described above, after supplying liquid fuel through a porous element with a diameter of 200 μm or less and turning the fuel into foam consisting of an aggregate of bubbles with a small diameter, air necessary for complete combustion of the foamed fuel in a combustor is separately removed. It is a method of supplying and combusting it and a device that embodies the same, and the apparent velocity of the foaming gas passing through the porous element, that is, the superficial velocity, is 0.01 m/s or more and 1 m/s or less. It includes.

【0006】すなわち、本発明の要旨とするところは、
(1)液体燃料に平均気孔径(目開き)が1μm以上、
200μm以下の多孔質エレメントを介して空気を供給
し、燃料を直径の小さな気泡の集合体からなる泡沫とし
た後、該泡沫燃料を燃焼器で完全燃焼するのに必要な空
気を別に供給して燃焼させるようにした液体燃料の泡沫
化燃焼方法であり、必要により発泡用気体が多孔質エレ
メントを通過する見掛けの速度、すなわち空塔速度を0
.01m/s以上、1m/s以下とする。
[0006] That is, the gist of the present invention is to
(1) The liquid fuel has an average pore diameter (opening) of 1 μm or more,
After supplying air through a porous element with a diameter of 200 μm or less to turn the fuel into foam consisting of an aggregate of air bubbles with a small diameter, air necessary for complete combustion of the foamed fuel in a combustor is separately supplied. This is a foaming combustion method for liquid fuel that is combusted, and if necessary, the apparent velocity at which the foaming gas passes through the porous element, that is, the superficial velocity, is reduced to 0.
.. 01 m/s or more and 1 m/s or less.

【0007】更に本発明は平均気孔径が1μm以上、2
00μm以下である多孔質エレメントと、該多孔質エレ
メントに気体供給管を接続して発泡域を形成する泡沫生
成器と、該泡沫生成器の上部に近接して設けられ、泡沫
燃料に燃焼用空気を供給して燃焼域を形成する燃焼器と
からなる液体燃料の泡沫化燃焼装置であり、必要により
多孔質エレメントを密度4.0〜6.0gr/cm3 
、空隙率35〜45%の焼結金属により構成し、多孔質
エレメントを密度2.0〜5.0gr/cm3 、見掛
けの気孔率15〜45%のセラミックス体により構成し
、多孔質エレメントの目開き方向を横向きとして、煤や
スケールによる発泡機能の障害を防止せしめ、多孔質エ
レメントの目開き方向を下向きとして、煤やスケールに
よる発泡機能の障害を防止せしめ、多孔質エレメントが
リング状の形状をなしていることにある。
[0007] Furthermore, the present invention has an average pore diameter of 1 μm or more, 2 μm or more.
00 μm or less; a foam generator that connects a gas supply pipe to the porous element to form a foaming region; This is a liquid fuel foaming combustion device consisting of a combustor that supplies fuel to form a combustion zone, and if necessary, a porous element with a density of 4.0 to 6.0 gr/cm3.
The porous element is made of a ceramic body with a density of 2.0 to 5.0 gr/cm3 and an apparent porosity of 15 to 45%. The opening direction of the porous element is set horizontally to prevent obstruction of the foaming function due to soot and scale, and the opening direction of the porous element is set downward to prevent obstruction of the foaming function due to soot and scale, and the porous element has a ring-shaped shape. It's in what you're doing.

【0008】図1は本発明の実施態様を示す要部縦断面
図、図2は図1のA−A断面図である。図3(a)(b
)は本発明における多孔質エレメントの平均気孔径と通
気抵抗の関係および着火の安定度の関係を示す図表であ
る。図5は本発明における空塔速度と発泡倍率の関係を
示す図表である。図6および図7は本発明に関わる泡沫
生成器の他の構成例を示す要部縦断面図であり、図6(
b)は図6(a)のB−B断面図である。
FIG. 1 is a longitudinal sectional view of a main part showing an embodiment of the present invention, and FIG. 2 is a sectional view taken along line AA in FIG. Figure 3(a)(b)
) is a chart showing the relationship between the average pore diameter of the porous element and the ventilation resistance and the relationship between the ignition stability in the present invention. FIG. 5 is a chart showing the relationship between superficial velocity and expansion ratio in the present invention. 6 and 7 are longitudinal cross-sectional views of main parts showing other configuration examples of the foam generator related to the present invention, and FIG.
b) is a BB sectional view of FIG. 6(a).

【0009】[0009]

【作用】以下本発明を図面にもとづいて説明する。図1
は本発明の実施態様例を示すもので、その要部を縦断面
で示す説明図、図2は図1のA−A断面図である。1は
泡沫生成器で、2は燃料を発泡させる機能を有する多孔
質エレメント、3は蒸発皿を示す。4は燃焼器で、該燃
焼器4の下部には、蒸発皿3と更にその下方に泡沫を生
成させるための泡沫生成器1が連続して近接配置されて
いる。
[Operation] The present invention will be explained below based on the drawings. Figure 1
2 shows an embodiment of the present invention, and is an explanatory diagram showing a main part thereof in a longitudinal section, and FIG. 2 is a sectional view taken along the line AA in FIG. 1. FIG. 1 is a foam generator, 2 is a porous element having a function of foaming fuel, and 3 is an evaporating dish. Reference numeral 4 denotes a combustor, and below the combustor 4, an evaporating dish 3 and a foam generator 1 for generating foam are disposed in series and close to each other below the evaporating dish 3.

【0010】蒸発皿3の上方にある燃焼器4は、その外
側に燃焼用空気を供給するための風箱7が設置されてい
る。液体燃料は泡沫生成器1に内接した多孔質エレメン
ト2の上部に供給されるが、下部に設けた発泡用気体供
給管5から空気で代表される気体があらかじめ吹き込ま
れているので、燃料(灯油、軽油等)は直ちに発泡し直
径の小さな気泡の集合体からなる泡沫の状態で上昇する
[0010] The combustor 4 located above the evaporating dish 3 is provided with a wind box 7 on the outside thereof for supplying combustion air. The liquid fuel is supplied to the upper part of the porous element 2 which is inscribed in the foam generator 1, but since a gas represented by air is blown in advance from the foaming gas supply pipe 5 provided at the lower part, the fuel ( (kerosene, diesel oil, etc.) immediately foams and rises in a foamy state consisting of a collection of small-diameter air bubbles.

【0011】点火はこの泡沫に直接点火ヒータ13で点
火し、燃焼を継続する。燃焼に供される液体燃料は、通
常灯油が多用されるが軽油も使用可能である。これらの
液体燃料は燃料タンク10からポンプ11、燃料供給管
6を通して供給される。9は保炎器で燃焼リング14と
対をなして継続燃焼を安定化させるもので、燃焼器4の
内部に設けられる。12は火炎を示す。泡沫生成器1は
蒸発皿3の中央部の下方に設けられる。泡沫生成器1の
中には、多孔質エレメント2が蒸発皿の底面以下に設け
た凹み23よりも下方に設けられる。多孔質エレメント
2には、図示の例では下方から発泡用の気体供給管5が
接続されて発泡域aを形成する。このようにして設けら
れる多孔質エレメント2は、泡沫燃料の均一化や発泡性
の安定化に極めて重要な役割を持つものであり、本発明
では、この多孔質エレメントの平均気孔径(目開き)を
1μm以上、200μm以下としている点に特徴がある
。図3(a)に点火、消火試験における圧力損失を示し
た。また、図3(b)に点火時の失火頻度を表した。 いずれも本発明者等の実験に基づくものである。これら
の試験によれば、多孔質エレメントの平均気孔径が1μ
m未満になると、発泡用空気の通気抵抗が多きくなるほ
か、しまいには目詰まりを生じることがわかった。また
、200μm超であると、泡沫を形成する気泡の直径が
全体に大きくなり供給空気の吹き抜けが発生し、安定し
た泡沫の形成ができなくなることがわかった。
[0011] This foam is directly ignited by the ignition heater 13 to continue combustion. The liquid fuel used for combustion is usually kerosene, but light oil can also be used. These liquid fuels are supplied from a fuel tank 10 through a pump 11 and a fuel supply pipe 6. A flame stabilizer 9 pairs with the combustion ring 14 to stabilize continuous combustion, and is provided inside the combustor 4. 12 indicates a flame. The foam generator 1 is provided below the center of the evaporating dish 3. Inside the foam generator 1, a porous element 2 is provided below a recess 23 provided below the bottom surface of the evaporating dish. In the illustrated example, a gas supply pipe 5 for foaming is connected to the porous element 2 from below to form a foaming region a. The porous element 2 provided in this way plays an extremely important role in making the foamed fuel uniform and stabilizing the foamability. It is characterized in that it is 1 μm or more and 200 μm or less. Figure 3(a) shows the pressure loss in the ignition and extinguishing tests. Further, FIG. 3(b) shows the misfire frequency during ignition. All of these are based on experiments by the inventors. According to these tests, the average pore diameter of the porous element was 1μ.
It has been found that when it is less than m, the ventilation resistance of the foaming air increases and eventually clogging occurs. Furthermore, it has been found that if the diameter exceeds 200 μm, the diameter of the bubbles forming the foam becomes large as a whole, causing supply air to blow through, making it impossible to form stable foam.

【0012】さらに本発明者等の実験によれば、燃料と
発泡用空気との接触面積を増加させ、燃料の蒸発量を点
火や燃焼に必要な加熱範囲にするには、泡の状態を示す
発泡倍率で5倍以上の泡沫とすることが必要であること
を見いだした。しかし、発泡倍率は、多孔質エレメント
の平均気孔径を適正にしても、図4に示すように、燃料
の種類や温度によって変化することから、多孔質エレメ
ントを通過する気体の空塔速度を0.01m/s以上、
1m/s以下の範囲が適正域として選択される。
Furthermore, according to experiments conducted by the present inventors, in order to increase the contact area between the fuel and the foaming air and bring the amount of fuel evaporation to the heating range necessary for ignition and combustion, it is necessary to It has been found that it is necessary to create foam with a foaming ratio of 5 times or more. However, even if the average pore diameter of the porous element is set appropriately, the expansion ratio changes depending on the type of fuel and temperature, as shown in Figure 4. .01m/s or more,
A range of 1 m/s or less is selected as an appropriate range.

【0013】すなわち、空塔速度が0.01m/s未満
になると、液体燃料の温度で異なるものの気泡の大部分
は、液体燃料中に留まって分離している状態、すなわち
、図4に示す気泡分離域での泡の状態となり、通常使わ
れる燃料の種類や温度において、点火や継続燃焼に必要
な燃料蒸気が不足する状態となる。また、この空塔速度
が1m/s超になると気体の塊が液体燃料中を吹き抜け
る状態となり、もはや安定した泡沫が形成されなくなり
、点火や継続燃焼が不安定になる。
That is, when the superficial velocity becomes less than 0.01 m/s, most of the bubbles remain in the liquid fuel and are separated, although the temperature of the liquid fuel varies, that is, the bubbles shown in FIG. Bubbles form in the separation zone, resulting in a lack of fuel vapor necessary for ignition and continued combustion at the type and temperature of fuel normally used. Furthermore, when the superficial velocity exceeds 1 m/s, a mass of gas blows through the liquid fuel, and stable bubbles are no longer formed, making ignition and continued combustion unstable.

【0014】次に、本発明を具現化する多孔質エレメン
トの具体的構成について述べる。平均気孔径が1μm以
上、200μm以下の多孔質エレメントとして実用可能
なものは例えば、多孔質の焼結金属やセラミックスがあ
げられる。多孔質エレメントに焼結金属を用いるときは
、焼結体の密度が4.0〜6.0gr/cm3 、空隙
率が35〜45%のものを、またセラミックス体を用い
るときは、セラミックス体の密度が2.0〜5.0gr
/cm3、見掛け気孔率が15〜45%のものを選択す
るとよい。
Next, the specific structure of the porous element embodying the present invention will be described. Practical porous elements having an average pore diameter of 1 μm or more and 200 μm or less include, for example, porous sintered metals and ceramics. When using sintered metal for the porous element, the sintered body should have a density of 4.0 to 6.0 gr/cm3 and a porosity of 35 to 45%, and when using a ceramic body, the ceramic body should have a porosity of 35 to 45%. Density is 2.0~5.0gr
/cm3, and the apparent porosity is preferably 15 to 45%.

【0015】なお本発明者等の他の実験によると、長時
間燃焼による煤の生成、あるいは保炎器などからのスケ
ールの落下があることから、このような場合には、多孔
質エレメント2の目開きを図6に示すように横向きとす
るか、あるいは図7に示すように下向きとして泡沫生成
器を構成すると良い。すなわち図6に示す例では、多孔
質エレメント2をリング状に形成し、発泡用気体供給管
5から接線方向に発泡用気体を供給するように示してい
る。これらの例によると、燃料の煤やスケールがエレメ
ント上に堆積することがないので安定した点火や燃焼を
継続することができる。
[0015] According to other experiments conducted by the present inventors, soot is produced due to long-term combustion or scale falls from a flame stabilizer, etc. In such cases, the porous element 2 is It is preferable to configure the foam generator with the openings facing sideways as shown in FIG. 6 or facing downwards as shown in FIG. 7. That is, in the example shown in FIG. 6, the porous element 2 is formed into a ring shape, and the foaming gas is supplied from the foaming gas supply pipe 5 in the tangential direction. According to these examples, since fuel soot and scale do not accumulate on the element, stable ignition and combustion can be continued.

【0016】なお、本発明における泡沫生成器、蒸発皿
、燃焼器は図2に示すように、その平面が円形に限定さ
れるものではなく、正方形や長方形等の変型も包含され
る。いずれの場合にも本発明の構成によれば、燃料供給
管6から供給する燃料と、発泡用気体供給管5から供給
する空気量を多くして泡沫生成量を増加させると共に、
燃焼用空気管8からの空気量を増やすことにより、燃焼
量を容易に増加させることができ、その可変範囲も十分
広いものである。
As shown in FIG. 2, the foam generator, evaporating dish, and combustor according to the present invention are not limited to circular planes, and may include modifications such as square or rectangular planes. In either case, according to the configuration of the present invention, the amount of fuel supplied from the fuel supply pipe 6 and the amount of air supplied from the foaming gas supply pipe 5 are increased to increase the amount of foam produced,
By increasing the amount of air from the combustion air pipe 8, the amount of combustion can be easily increased, and its variable range is sufficiently wide.

【0017】[0017]

【実施例】図1に示す実施態様と同様の構成により下記
の燃焼器で燃焼させた時の実施例および比較例について
説明する。ここで使用した燃焼器および泡沫生成器の仕
様は以下の通りである。   ・燃焼器の直径×高さ             
   :内径    150mmφ×150mm  ・
泡沫生成器の直径×高さ            :内
径      40mmφ×  20mm・多孔質エレ
メントの直径×厚さ      :有効直径  40m
mφ×    2mm(焼結金属およびセラミックス体
) ・蒸発皿逆円錐形上縁部直径×底部直径:内径    
150mmφ×  40mmφ・保炎器       
                     :燃焼リ
ング付保炎器燃焼試験は、点火後そのまま燃焼を48時
間継続して消火する長時間繰り返し連続試験と、点火後
30分間の燃焼、その後消火し15分間停止させて再び
試験を繰り返す点火、消火試験に分けて実施した。
[Example] Examples and comparative examples in which combustion is performed in the following combustor with the same configuration as the embodiment shown in FIG. 1 will be described. The specifications of the combustor and foam generator used here are as follows.・Diameter x height of combustor
:Inner diameter 150mmφ×150mm ・
Diameter x height of foam generator: Inner diameter 40mmφ x 20mm・Diameter x thickness of porous element: Effective diameter 40m
mφ x 2mm (sintered metal and ceramic body) ・Evaporation dish inverted conical upper edge diameter x bottom diameter: Inner diameter
150mmφ×40mmφ・Flame holder
:The flame holder combustion test with a combustion ring consists of a long-term repeated continuous test in which the combustion is continued for 48 hours after ignition and extinguished, and the ignition test is repeated for 30 minutes after ignition, then extinguished, stopped for 15 minutes, and the test is repeated again. The fire extinguishing test was conducted separately.

【0018】長時間連続試験は、燃焼器4の燃焼用空気
管8から所定の空気量を供給し、次に直径40mmの多
孔質エレメント2に接続した発泡用気体供給管5から所
定の発泡用空気を供給しながら、灯油の所定量をポンプ
11を介して泡沫生成器1に内接して設けてある多孔質
エレメント2の上部に供給した。ここで灯油は直ちに泡
沫となって点火ヒータ13で着火され約2分後に所定の
空気比、燃焼量に調整されて燃焼を継続する。その後、
燃焼が定常状態となってから、4時間毎に燃焼排ガス中
のCO,NOx,BR(煤),アルデヒドを測定した。 それらの結果を表1に比較例とともに示した。
In the long-term continuous test, a predetermined amount of air is supplied from the combustion air pipe 8 of the combustor 4, and then a predetermined amount of air is supplied from the foaming gas supply pipe 5 connected to the porous element 2 having a diameter of 40 mm. While supplying air, a predetermined amount of kerosene was supplied via the pump 11 to the upper part of the porous element 2 provided internally in the foam generator 1. Here, the kerosene immediately becomes foam and is ignited by the ignition heater 13, and after about 2 minutes, the air ratio and combustion amount are adjusted to a predetermined air ratio and combustion amount continues. after that,
After the combustion reached a steady state, CO, NOx, BR (soot), and aldehyde in the combustion exhaust gas were measured every 4 hours. The results are shown in Table 1 along with comparative examples.

【0019】[0019]

【表1】[Table 1]

【0020】本発明は表1に示すように、燃焼特性値の
いずれにおいても良好であった。これらの結果は、液体
燃料の泡沫化燃焼が単に燃料の蒸発促進のみでなく、蒸
発燃料と燃焼用空気との均一混合性も大きく改善できる
ことを意味している。
As shown in Table 1, the present invention was good in all combustion characteristic values. These results mean that the foaming combustion of liquid fuel not only promotes evaporation of the fuel, but also greatly improves the uniformity of mixing the evaporated fuel and the combustion air.

【0021】また、表2には多孔質エレメントの平均気
孔径(目開き)と空塔速度により、燃焼特性値を整理し
て示した。この結果からも、本発明で示す多孔質エレメ
ントの平均気孔径の範囲および空塔速度の範囲が有効で
あることがわかる。なお表1の比較例に示すように、多
孔質エレメントの平均気孔径(目開き)が本発明の範囲
にあっても、空塔速度が本発明の範囲を逸脱する場合に
は、最良の燃焼状態が得られないものであった。
[0021] Table 2 also shows the combustion characteristic values organized according to the average pore diameter (mesh opening) and superficial velocity of the porous element. This result also shows that the range of average pore diameter and superficial velocity range of the porous element shown in the present invention is effective. As shown in the comparative example in Table 1, even if the average pore diameter (opening) of the porous element is within the range of the present invention, if the superficial velocity deviates from the range of the present invention, the best combustion The condition was unobtainable.

【0022】[0022]

【表2】[Table 2]

【0023】また多孔質エレメント部の空塔速度は、目
開きの限界近傍で点火の安定性に大きく影響するほか、
長時間連続試験でも表2に示すように、燃焼排ガス中の
CO,NOx,BR(煤)に影響するほか、図5に示す
消火時間にも影響する。この多孔質エレメント部の空塔
速度は、これらのいずれの燃焼試験結果にあっても、そ
の適正範囲は0.01〜1m/sであった。
[0023] In addition, the superficial velocity of the porous element has a large effect on the stability of ignition near the limit of opening, and
Even in long-term continuous tests, as shown in Table 2, it not only affects CO, NOx, and BR (soot) in the combustion exhaust gas, but also affects the extinguishing time shown in Figure 5. In all of these combustion test results, the superficial velocity of this porous element portion was within the appropriate range of 0.01 to 1 m/s.

【0024】[0024]

【発明の効果】本発明は泡生成器の多孔質エレメントの
平均気孔径(目開き)を最適に選択したので、発泡用気
体の通気抵抗を小さくでき、また、多孔質エレメント部
の空塔速度を限定することにより、生成される泡沫も直
径が0.5〜5mmの小さな気泡の集合体となり、安定
した点火や継続燃焼を達成させるものであり、産業上多
大な効果を奏するものである。
Effects of the Invention In the present invention, the average pore diameter (opening) of the porous element of the foam generator is optimally selected, so the ventilation resistance of the foaming gas can be reduced, and the superficial velocity of the porous element can be reduced. By limiting the amount, the generated foam becomes an aggregate of small bubbles with a diameter of 0.5 to 5 mm, achieving stable ignition and continuous combustion, which has great industrial effects.

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

【図1】本発明の実施態様を示す要部の縦断面図である
FIG. 1 is a longitudinal cross-sectional view of essential parts showing an embodiment of the present invention.

【図2】図1のA−A断面図である。FIG. 2 is a sectional view taken along the line AA in FIG. 1;

【図3】(a)(b)は本発明における多孔質エレメン
トの平均気孔径と通気抵抗の関係および着火の安定度の
関係を示す図表である。
FIGS. 3(a) and 3(b) are charts showing the relationship between the average pore diameter of the porous element and the ventilation resistance and the relationship between the ignition stability in the present invention.

【図4】本発明における空塔速度と発泡倍率の関係を示
す図表である。
FIG. 4 is a chart showing the relationship between superficial velocity and expansion ratio in the present invention.

【図5】本発明の実施例における空塔速度と消火時間の
関係を示す図表である。
FIG. 5 is a chart showing the relationship between superficial velocity and extinguishing time in an example of the present invention.

【図6】 (a)は本発明に関わる泡沫生成器の他の構成例を示す
要部の縦断面図であり 、(b)は(a)のB−B縦断面図である。
FIG. 6(a) is a vertical cross-sectional view of essential parts showing another configuration example of the foam generator according to the present invention, and FIG. 6(b) is a vertical cross-sectional view taken along line BB in (a).

【図7】本発明に関わる泡沫生成器の他の構成例を示す
要部の縦断面図である。
FIG. 7 is a vertical cross-sectional view of essential parts showing another configuration example of the foam generator according to the present invention.

【符号の説明】[Explanation of symbols]

1    泡沫生成器 2    多孔質エレメント 3    蒸発皿 4    燃焼器 5    発泡用気体供給管 6    燃料供給管 7    風箱 8    燃焼用空気供給管 9    保炎器 10  燃料タンク 11  ポンプ 12  火炎 13  点火ヒータ 14  燃焼リング 1 Foam generator 2 Porous element 3 Evaporating dish 4 Combustor 5 Gas supply pipe for foaming 6 Fuel supply pipe 7 Wind box 8 Combustion air supply pipe 9 Flame holder 10 Fuel tank 11 Pump 12 Flame 13 Ignition heater 14 Combustion ring

Claims (8)

【特許請求の範囲】[Claims] 【請求項1】  液体燃料に平均気孔径(目開き)が1
μm以上、200μm以下の多孔質エレメントを介して
空気を供給し、燃料を直径の小さな気泡の集合体からな
る泡沫とした後、該泡沫燃料を燃焼器で完全燃焼するの
に必要な空気を別に供給して燃焼させるようにした液体
燃料の泡沫化燃焼方法。
[Claim 1] The liquid fuel has an average pore diameter (opening) of 1.
After supplying air through a porous element with a size of µm or more and 200 µm or less and converting the fuel into foam consisting of an aggregate of air bubbles with a small diameter, air necessary for complete combustion of the foamed fuel in a combustor is separately supplied. A method for combusting liquid fuel into foam by supplying and combusting it.
【請求項2】  発泡用気体が多孔質エレメントを通過
する見掛けの速度、すなわち空塔速度が0.01m/s
以上、1m/s以下である請求項1記載の液体燃料の泡
沫化燃焼方法。
[Claim 2] The apparent velocity at which the foaming gas passes through the porous element, that is, the superficial velocity is 0.01 m/s.
The method for foaming and combustion of liquid fuel according to claim 1, wherein the combustion rate is 1 m/s or less.
【請求項3】  平均気孔径が1μm以上、200μm
以下である多孔質エレメントと、該多孔質エレメントに
気体供給管を接続して発泡域を形成する泡沫生成器と、
該泡沫生成器の上部に近接して設けられ、泡沫燃料に燃
焼用空気を供給して燃焼域を形成する燃焼器とからなる
液体燃料の泡沫化燃焼装置。
[Claim 3] Average pore diameter is 1 μm or more, 200 μm
a porous element as follows; a foam generator connecting a gas supply pipe to the porous element to form a foaming region;
A combustor for foaming and combusting liquid fuel, which comprises a combustor that is disposed close to the upper part of the foam generator and that supplies combustion air to the foamed fuel to form a combustion zone.
【請求項4】  多孔質エレメントを密度4.0〜6.
0gr/cm3、空隙率35〜45%の焼結金属により
構成した請求項3記載の液体燃料の泡沫化燃焼装置。
4. The porous element has a density of 4.0 to 6.0.
4. The liquid fuel foaming combustion apparatus according to claim 3, wherein the liquid fuel foaming combustion apparatus is made of sintered metal having a porosity of 0 gr/cm3 and a porosity of 35 to 45%.
【請求項5】  多孔質エレメントを密度2.0〜5.
0gr/cm3、見掛けの気孔率15〜45%のセラミ
ックス体により構成した請求項3記載の液体燃料の泡沫
化燃焼装置。
5. The porous element has a density of 2.0 to 5.
4. The liquid fuel foaming combustion apparatus according to claim 3, which is constructed of a ceramic body having an apparent porosity of 0 gr/cm3 and an apparent porosity of 15 to 45%.
【請求項6】  多孔質エレメントの目開き方向を横向
きとして、煤やスケールによる発泡機能の障害を防止し
た請求項3記載の液体燃料の泡沫化燃焼装置。
6. The liquid fuel foaming combustion device according to claim 3, wherein the opening direction of the porous element is oriented horizontally to prevent the foaming function from being impaired by soot or scale.
【請求項7】  多孔質エレメントの目開き方向を下向
きとして、煤やスケールによる発泡機能の障害を防止し
た請求項3記載の液体燃料の泡沫化燃焼装置。
7. The liquid fuel foaming combustion device according to claim 3, wherein the opening direction of the porous element is directed downward to prevent obstruction of the foaming function due to soot and scale.
【請求項8】  多孔質エレメントがリング状の形状を
なしている請求項6記載の液体燃料の泡沫化燃焼装置。
8. The liquid fuel foaming combustion device according to claim 6, wherein the porous element has a ring shape.
JP3037515A 1990-03-20 1991-03-04 Method and apparatus for foaming combustion of liquid fuel Expired - Lifetime JP2688120B2 (en)

Priority Applications (5)

Application Number Priority Date Filing Date Title
KR1019910701141A KR950012775B1 (en) 1990-03-20 1990-03-15 Method and apparatus for burning foamed liquid fuel
CA002049009A CA2049009C (en) 1990-03-20 1991-03-15 Method and apparatus for burning foamed liquid fuel
EP19910906260 EP0478789A4 (en) 1990-03-20 1991-03-15 Method of and device for burning liquid fuel after turning thereof into bubbles
PCT/JP1991/000353 WO1991014900A1 (en) 1990-03-20 1991-03-15 Method of and device for burning liquid fuel after turning thereof into bubbles
US07/741,503 US5192203A (en) 1990-03-20 1991-03-15 Method and apparatus for burning foamed liquid fuel

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
JP7155790 1990-03-20
JP2-71557 1990-03-20

Publications (2)

Publication Number Publication Date
JPH04214106A true JPH04214106A (en) 1992-08-05
JP2688120B2 JP2688120B2 (en) 1997-12-08

Family

ID=13464147

Family Applications (1)

Application Number Title Priority Date Filing Date
JP3037515A Expired - Lifetime JP2688120B2 (en) 1990-03-20 1991-03-04 Method and apparatus for foaming combustion of liquid fuel

Country Status (2)

Country Link
JP (1) JP2688120B2 (en)
KR (1) KR950012775B1 (en)

Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5697708A (en) * 1980-01-08 1981-08-06 Matsushita Electric Ind Co Ltd Liquid fuel combustor
JPS5821715U (en) * 1981-08-03 1983-02-10 ティーディーケイ株式会社 combustion device
JPS643946U (en) * 1987-06-29 1989-01-11
JPH0195205A (en) * 1987-10-05 1989-04-13 Nippon Steel Corp Method of burning liquid fuel

Patent Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5697708A (en) * 1980-01-08 1981-08-06 Matsushita Electric Ind Co Ltd Liquid fuel combustor
JPS5821715U (en) * 1981-08-03 1983-02-10 ティーディーケイ株式会社 combustion device
JPS643946U (en) * 1987-06-29 1989-01-11
JPH0195205A (en) * 1987-10-05 1989-04-13 Nippon Steel Corp Method of burning liquid fuel

Also Published As

Publication number Publication date
KR950012775B1 (en) 1995-10-21
JP2688120B2 (en) 1997-12-08
KR920701752A (en) 1992-08-12

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