JPS6296590A - Method and apparatus for burning fuel-water - Google Patents

Method and apparatus for burning fuel-water

Info

Publication number
JPS6296590A
JPS6296590A JP61139877A JP13987786A JPS6296590A JP S6296590 A JPS6296590 A JP S6296590A JP 61139877 A JP61139877 A JP 61139877A JP 13987786 A JP13987786 A JP 13987786A JP S6296590 A JPS6296590 A JP S6296590A
Authority
JP
Japan
Prior art keywords
fuel
water
combustion
reaction chamber
oxygen
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
JP61139877A
Other languages
Japanese (ja)
Other versions
JPH0726107B2 (en
Inventor
Tsumoru Tajima
田島 積
Kiyuugo Nobuhara
延原 九吾
Kazuyoshi Nakamura
中村 和善
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Individual
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Individual
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Publication date
Application filed by Individual filed Critical Individual
Priority to JP61139877A priority Critical patent/JPH0726107B2/en
Publication of JPS6296590A publication Critical patent/JPS6296590A/en
Publication of JPH0726107B2 publication Critical patent/JPH0726107B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

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    • Y02E20/344

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  • Air Supply (AREA)

Abstract

PURPOSE:To prevent an accidental fire, to accelerate the generation of CO and H2, and to improve the combustion efficiency of a fuel, by injecting a fuel and water into a high-temp. reaction chamber together with oxygen to reduce the unevenness of volumes of water, fuel and oxygen and, at the same time, to disperse the vaporized water, thereby burning the fuel. CONSTITUTION:A nozzle 4 for injection of a high-pressure fuel is provided at the top end of a fuel-injection burner 6, and is arranged at the bottom opening portion of a cylindrical high temp. reaction chamber 3 which is packed with a refractory 5 having pores which communicate with each other at a position around the middle thereof. The reaction chamber 3 is a cylindrical hood made of a refractory and opened at its both ends. Fuel-water combustion is carried out, e.g., under the following conditions: a fuel injection pressure of about 300kg/cm<2>; a fuel injection rate of about 40l/hr; a heavy oil A as a fuel; and water content: 10%, 20%, 30%, and 40%. When the fuel is injected, both the fuel 1 and water 2 float in the form of a fume and do not drop down. According to the titled method and apparatus, a water-contg. fuel can be burnt stably at high efficiency without causing accidental fire and can contribute to the energy-saving and the prevention of pollution problems.

Description

【発明の詳細な説明】 「産業上の利用分野」 本発明は燃料・水・添加物等の混合物燃焼法及びその装
置に関するものである。
DETAILED DESCRIPTION OF THE INVENTION "Field of Industrial Application" The present invention relates to a method and apparatus for combustion of a mixture of fuel, water, additives, etc.

「従来の技術」 従来より燃料に水を混入し燃焼の改善をする方法は幾多
の事例があったが、いづれも下記に示すような不具合点
があり改善の余地が残されていた。
``Prior Art'' There have been many examples of methods for improving combustion by mixing water into fuel, but all of them had the following drawbacks and left room for improvement.

m  水混入の目的かNOX値対策の為の炉内温度低減
に使われる”′場合、概ね900°C以下の温度帯で燃
焼が行われる為水の分解反応は極めて少く未燃分も発生
燃焼効率は低下傾向を示していた。
m When used for the purpose of water contamination or to reduce the temperature inside the furnace to reduce NOx levels, combustion occurs at a temperature of approximately 900°C or less, so there is very little water decomposition reaction and unburned matter is also generated. Efficiency showed a decreasing trend.

(21水滴を微細にして炉内に燃料と共に噴射し炭素と
水の反応による水分解燃焼を目的としても炉内に於ける
反応雰囲気が乏しく、尚且つ燃焼ゾーン内は燃焼用空気
、燃料の噴気等のガス体も動きが早く、水の分解反応は
極めて低調、不安定な状況であった。
(21) Even if water droplets are made into fine particles and injected into the furnace together with fuel for water decomposition combustion due to the reaction between carbon and water, the reaction atmosphere inside the furnace is poor, and the combustion zone is filled with combustion air and fuel jets. Gas bodies such as these also moved quickly, and the water decomposition reaction was extremely slow and unstable.

(3)  燃料並びに燃料中の氷粒も噴射バーナーより
噴出された際粒径の大きなものが混入し燃料にあっては
充分内部迄O2の接触ができず未燃となり、氷粒にあっ
ては容積がスチーム化することにより約1244倍に増
大、周辺のO2やC等を飛散させる為、充分な接触がで
き難かった。この為水分解も低調に推移し充分な省エネ
的効果が出なかった。
(3) When the fuel and the ice particles in the fuel are ejected from the injection burner, large particles get mixed in with the fuel, and the fuel is unable to reach enough O2 to reach the inside, resulting in unburned ice particles. The volume increases by approximately 1244 times due to steam formation, which scatters surrounding O2, C, etc., making it difficult to make sufficient contact. For this reason, water splitting remained sluggish and sufficient energy-saving effects were not achieved.

(4)  燃料油中に水を微細粒として混入して噴射す
る方法が一般に使用されているが、油水分離が生じ易く
この為の失火や湿度低下があり、且つ始動の際は油準味
の燃焼が必要な場合も多く、改善の余地が伐ってい念。
(4) A method of mixing fine particles of water into fuel oil and injecting it is generally used, but oil-water separation tends to occur, resulting in misfires and a drop in humidity. There are many cases where combustion is necessary, and there is still room for improvement.

「発明が解決しようとする問題点」 本発明は水の気化膨張による約1244倍の占有容積部
分と燃料及び空気の占有容積部分との均等配分を行って
失火を防止し且つ気化水分の炭素との反応分解によるC
 O% H2の発生を促進し尚且つ安定して燃焼させる
ことにより燃料の燃焼効率を上昇させることを目的とす
るものである。
``Problems to be Solved by the Invention'' The present invention prevents misfires by equally distributing the volume occupied by approximately 1244 times the volume occupied by the vaporized expansion of water and the volume occupied by fuel and air. C due to the reaction decomposition of
The purpose is to increase the combustion efficiency of fuel by promoting the generation of O% H2 and by stably burning it.

「問題点を解決するための手段」 本発明は燃料と水を高温反応室内に酸素と共に」幾噴射
し、水の気化占有部分と燃料、酸素の占有部分との容積
むらを均す工程と、気化水分の分解工程と、燃焼工程と
よりなる燃料・本燃焼法、燃料と水並びに添加物を高温
反応室内に酸素と共に高へ噴射し、水の気化占有部分と
燃料、酸素の占有部分との容積むらを均す工程と、気化
水分の分解工程と、燃焼工程を同時に行うことよりなる
燃料・本燃焼法、 先端開口反応室の基端開口部に燃料高年噴射ノズルを配
設し、同反応室の内部に連通気孔耐火物を配設し、噴射
燃料と燃焼用酸素等が上記耐火物を通過するよう配置し
てなる燃料・本燃焼装置によって構成される。
``Means for Solving the Problems'' The present invention includes a step of injecting fuel and water together with oxygen into a high-temperature reaction chamber to equalize the volume unevenness between the vaporized portion of water and the portion occupied by fuel and oxygen; This fuel/main combustion method consists of a decomposition process of vaporized moisture and a combustion process, in which fuel, water, and additives are injected into a high temperature reaction chamber together with oxygen, and the vaporized portion of water is separated from the portion occupied by fuel and oxygen. The fuel combustion method consists of simultaneously performing the process of leveling volume unevenness, the process of decomposing vaporized water, and the combustion process. It is constituted by a fuel/main combustion device in which a continuous vent refractory is disposed inside the reaction chamber, and the injected fuel, combustion oxygen, etc. are arranged so as to pass through the refractory.

からは酸素(空気)を送入すると上記燃料及び水けS塾
X珈阪細\へ鳳ぺな懺鬼際素と共に連通気孔耐火物内を
通過し、これに点火すると燃料が燃焼して連通気孔耐火
物及び反応室内は高温の状態となり逐次高熱されてくる
。そして上記添加水の微細水滴は高温のなめ気化して容
積か約1244倍に膨張し上記燃料粒子や空気を飛散細
分化させるがそJlに伴い燃料と空気のむらも発生する
。しがしこのような状態は連通気孔耐火物を通過させる
ことによって均等:こ均され気化水分占有部分は寸1)
、分散しその内部に燃料、空気占有部分が介在した状態
となるし、微粒子は上記連通気孔耐火物の無数の気孔面
に衝接して拡散混合微細粒化しかつ同耐火物の保有高温
によって燃料は気化燃焼すると同時に炭素粒子と水蒸気
との反応により水性ガス化しCO,Hzの発生が生じ燃
焼が促進され同耐火物通過後において青色焔による燃焼
状態が安定して生じるようになる。又、燃焼用空気の代
りに0λ、Oz ’Jラッチを吹き込むと格段に上記燃
焼改善が促進され、NOxの値も低減する。この現象は
高床噴射による噴射物の極微粒子比と連通気孔耐火物を
組み合せた為に得られた特技である。上記燃焼の理論は
次のとおりである。
When oxygen (air) is sent from the above, it passes through the refractory through the vent with the above-mentioned fuel and water, and when it is ignited, the fuel burns and the connection is made. The pore refractories and the reaction chamber are in a high temperature state and are gradually heated up. The fine water droplets of the added water vaporize at a high temperature and expand to about 1244 times the volume, scattering and fragmenting the fuel particles and air, but this also causes unevenness between the fuel and air. However, this condition can be evened out by passing through a continuous vent refractory: the area occupied by vaporized water is 1)
The fine particles are dispersed and have fuel and air-occupied parts interposed inside them, and the fine particles collide with the numerous pore surfaces of the above-mentioned continuous-vent refractory and are diffused and mixed into fine particles, and due to the high temperature held by the refractory, the fuel is At the same time as vaporization and combustion, the reaction between carbon particles and water vapor causes water gasification, generating CO and Hz, promoting combustion, and stably producing a blue flame combustion state after passing through the refractory. Furthermore, when 0λ, Oz 'J latch is blown in instead of combustion air, the above-mentioned combustion improvement is greatly promoted and the NOx value is also reduced. This phenomenon is a special skill achieved by combining the ultrafine particle ratio of the ejected material with raised bed injection and the continuous vent refractories. The theory of the above combustion is as follows.

燃料中の炭素が燃える過程でスチームと接触すると特定
温度条件下では下記の反応式の如く可燃性の一酸化炭素
と水素が生じる。この現象が上記反応室内で充分促進さ
れ発熱燃焼が効率よく行われる。尚、炭素と水蒸気の反
応は次のようなものである。
When carbon in fuel comes into contact with steam during the burning process, flammable carbon monoxide and hydrogen are produced under specific temperature conditions as shown in the reaction equation below. This phenomenon is sufficiently promoted in the reaction chamber, and exothermic combustion is efficiently carried out. The reaction between carbon and water vapor is as follows.

C−1−1),O= CO+ l−l2(28,8kc
alAnol )0+ 2 l1zO−C! Oユ+ 
2 H2(18,8kcal/1nol  )又C,C
o、H,の燃焼反応は次のようなものであるO C+ 02= 002  (+ 9 7  kcal/
1nol )C+K 02=CO(+ 29.4  k
cal/1nol  )C+OO,=2CO(38,2
kcal/1nol>2 CO+ O,= 2 COユ
(+ 1 36.4 kcal/1nol )CO+H
,0=CO,+)l、(+10.l   〃  )21
):L−t−0ユ=21).LO(+1 1 5.6 
   、y   )「実施例J 撚れ噴射バーナー6の先端に高圧燃料噴射ノズル4(燃
料の種類にょっでは同項型ノズルを用いる)を設け、筒
状高温反応室3の基端開口部に同ノズル4を配設し、同
反応室3の中程に連通気孔耐火物5を充填する(第1図
、第2図、第4図、第6図〜第9図)。又円環状噴射燃
料では第10図、第1)図のように形成し、螺旋状噴射
燃料では第12図のように連通気孔耐火物5を螺旋状に
配設しても良い。第2図は第1図の試験事例反応室3で
あって全長L=3500+nns内径1 =600mm
温度センサーaz bz CN d及びその距離e1f
sgsh、iが50゛0.800.800.1000.
400rrynで連通気孔耐火物の幅t = 70 t
Tlnである。
C-1-1), O= CO+ l-l2 (28,8kc
alAnol ) 0+ 2 l1zO-C! Oyu+
2 H2 (18,8kcal/1nol) also C,C
The combustion reaction of o, H, is as follows: O C+ 02= 002 (+ 9 7 kcal/
1nol)C+K02=CO(+29.4k
cal/1nol)C+OO,=2CO(38,2
kcal/1nol>2 CO+ O, = 2 COU (+ 1 36.4 kcal/1nol) CO+H
,0=CO,+)l,(+10.l 〃 )21
):L-t-0U=21). LO(+1 1 5.6
, y) "Example J A high-pressure fuel injection nozzle 4 (the same type nozzle is used depending on the type of fuel) is provided at the tip of the twisted injection burner 6, and the same type nozzle is provided at the base end opening of the cylindrical high temperature reaction chamber 3. A nozzle 4 is arranged, and a communicating hole refractory 5 is filled in the middle of the reaction chamber 3 (Fig. 1, Fig. 2, Fig. 4, Fig. 6 to Fig. 9). In this case, the refractory material 5 may be formed as shown in FIG. 10 and FIG. Test case reaction chamber 3, total length L = 3500 + nns inner diameter 1 = 600 mm
Temperature sensor az bz CN d and its distance e1f
sgsh, i is 50゛0.800.800.1000.
Width of continuous vent refractory at 400rryn t = 70t
It is Tln.

燃料噴射圧力  300 K9/Cm”燃料噴射量  
  401/II 燃料銘柄    A重油 水混入率  10%、20%、30%、40%、反応室
3は耐火材を使用した筒状両端開口フードである。又燃
料噴射時には燃料lと水2¥i共に煙霧状(0,1μ位
い)となり浮遊し落下するものはない。
Fuel injection pressure 300 K9/Cm” Fuel injection amount
401/II Fuel brand A Heavy oil Water mixing rate 10%, 20%, 30%, 40% The reaction chamber 3 is a cylindrical hood with openings at both ends made of fireproof material. Furthermore, during fuel injection, both fuel 1 and water 2\i become atomized (approximately 0.1 μm in size) and float, with nothing falling.

(実験結果) へ重油401/I−1と水とを混合して用いその比率は
水30%八重油70%であった。
(Experimental Results) Heavy oil 401/I-1 and water were mixed and the ratio was 30% water and 70% double oil.

(1)  燃料着火筒内温度上昇しAよりa附近が10
00°C位に達すると燃焼室の白赤色火焔が青味を帯び
けじめその長さも短くなる(150〜200mn)。
(1) The temperature in the fuel ignition cylinder increases and the temperature near a is 10% compared to A.
When the temperature reaches around 00°C, the white-red flame in the combustion chamber takes on a bluish tinge and its length becomes short (150 to 200 m).

(2)a点1200°C位になると青色畑がうすくなり
バーナー先端デフユーザー附近に若干みられる程度、他
は煙色がない状態に近くなり筒内温度は上昇、 (3)火焔の温度は油単味の時は焔の色があるので測定
した。約1680°C前後の漬水混入時は焔の色かうす
い為測定はできづらいが筒内温度は上昇、 (4)内部温度は下記の値で火焔も安定し燃焼も継続安
定的に推移した。
(2) When point a reaches around 1,200°C, the blue field becomes thinner and can be seen slightly near the burner tip near the differential user, and the rest becomes almost no smoke color, and the temperature inside the cylinder increases. (3) The temperature of the flame increases. When using only oil, there is a color of flame, so I measured it. When soaking water at around 1680°C was mixed in, the flame color was so faint that it was difficult to measure, but the temperature inside the cylinder rose. (4) The internal temperature was as follows, the flame was stable, and the combustion continued to be stable .

8点  1255°C b点  1260℃ 0点  1265°C 4点  1200”C (5)黒煙皆無、空気過剰係数m値=0.95(6)燃
焼時煙色が油単味時と大幅に異り青色や無色に近くなる
のはH2とCOが発生しての燃焼と思われる。
8 points 1255°C Point b 1260°C 0 points 1265°C 4 points 1200”C (5) No black smoke, excess air coefficient m value = 0.95 (6) Smoke color during combustion is significantly different from when using only oil. The reason why it becomes blue and almost colorless is thought to be due to combustion due to the generation of H2 and CO.

(力 水の混入率は下記の如き内容迄実施、いづれも上
記同様の似かよった現象を示した。
(Power) Water mixing rates were tested as shown below, and all showed similar phenomena as above.

バーナー噴射量 401/I−1 油%  水%  空気過剰率(m値) 90  10   1.05 80  20   1.02 70     30       0.9560  4
0   0.8 以上が試験結果であるが前記のスチームに関する燃焼反
応の項で述べた水の分解と水が燃焼を促進する働きがあ
ることを実証している。
Burner injection amount 401/I-1 Oil% Water% Air excess ratio (m value) 90 10 1.05 80 20 1.02 70 30 0.9560 4
0 0.8 The test results above demonstrate that water decomposes and promotes combustion as described in the section on combustion reactions related to steam.

尚図中1は燃料、2は水、7はフィルター、8はスタテ
ィックミキサー、9は燃料油タンク、10は水タンク、
第1図中1)は燃焼用空気旋回羽根、1)1−を着火電
極、13け高圧燃料噴射ポンプ、14は攪拌槽、第6図
中15は0ユ又け0ユリツチ或は0Jの貯留槽、4′は
水環用噴射ノズル13’は水専用高圧噴射ポンプ、第7
図中16はスチーム供給管、第8因中17は界面活性剤
アルコール等の添加物注入槽である。連通気孔耐火物5
は第3火に拡大して示すようにアルミナ系窒化珪素、炭
化珪素、カーボランダム、セラミック材、発泡セラミッ
ク、網状セラミック等を燃F1の種類と条件により気孔
率を適宜形成することができる。燃料は液体、粉体等の
燃料であれば良く石炭、コークス荀の粉体ll1200
メツシユ以下のものを用いる。
In the figure, 1 is fuel, 2 is water, 7 is a filter, 8 is a static mixer, 9 is a fuel oil tank, 10 is a water tank,
1) in Figure 1 is a combustion air swirl vane, 1) 1- is an ignition electrode, 13-piece high-pressure fuel injection pump, 14 is a stirring tank, and 15 in Figure 6 is a 0-unit, 0-unit or 0-J storage. tank, 4' is a water ring injection nozzle 13' is a high-pressure injection pump exclusively for water, No. 7
In the figure, 16 is a steam supply pipe, and 17 in the eighth factor is a tank for injecting additives such as surfactant alcohol. Connecting vent refractory 5
As shown in the enlarged view of the third flame, alumina-based silicon nitride, silicon carbide, carborundum, ceramic material, foamed ceramic, reticulated ceramic, etc. can be used to form an appropriate porosity depending on the type and conditions of the flame F1. The fuel may be liquid, powder, etc. Coal, coke powder ll1200
Use something below mesh.

上記実験は次の条件の下に行った。The above experiment was conducted under the following conditions.

(1)高圧噴射の圧力は100〜1000 K9/cJ
(2)  噴射される噴霧粒子は10μ以下(3)  
連通気孔耐火物温度け1000−1600’C(4) 
 添加物は水、界面活性剤、アルコール類他、酸素、酸
素リッチ、オゾン等、混焼用燃料(石炭、石油フークス
、その他低質油8)「効果」 本発明は上述の方法及び装置によったので水添加燃料を
失火のおそれがなくきわめて効率良く安定して燃焼し得
て省エネ及び公害対策に適用し得る効果がある。
(1) High pressure injection pressure is 100 to 1000 K9/cJ
(2) Sprayed particles are 10μ or less (3)
Connecting vent refractory temperature 1000-1600'C (4)
Additives include water, surfactants, alcohols, etc., oxygen, oxygen rich, ozone, etc., fuel for co-combustion (coal, petroleum Fuchs, and other low quality oils8). Water-added fuel can be burnt very efficiently and stably without fear of misfire, and has the effect of being applicable to energy saving and pollution control.

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

第1図は本発明の燃料・水燃焼装置を示す図、第2図は
反応室の(till +1n図、第3図は連通気孔耐火
物の一部拡大図、@4図は第2図の他の実施例の側面図
、第5図は粒子の連通気孔耐火物への接触状態の説明図
、第6図は第1図の他の実施例の説明図、第7図はスチ
ー′ム添加による本発明の説明図、第8図は第1図の池
の実施例の説明図、第9図〜第12図はそれぞれ反応室
の実施例の縦断面図である。 l・・燃料、2・・水、3・・高温反応室、4・・燃料
蘂平噴射ノズル、5・・連通気孔耐火物。
Figure 1 is a diagram showing the fuel/water combustion device of the present invention, Figure 2 is a (till +1n diagram) of the reaction chamber, Figure 3 is a partially enlarged view of the continuous vent refractory, and Figure @4 is a diagram of the reaction chamber. A side view of another embodiment, FIG. 5 is an explanatory diagram of the state of contact of particles with the continuous vent refractory, FIG. 6 is an explanatory diagram of another embodiment of FIG. 1, and FIG. 7 is an illustration of the addition of steam. FIG. 8 is an explanatory diagram of the embodiment of the pond in FIG. 1, and FIGS. 9 to 12 are longitudinal cross-sectional views of the embodiment of the reaction chamber. ... Water, 3. High temperature reaction chamber, 4. Fuel injection nozzle, 5. Continuous vent refractory.

Claims (3)

【特許請求の範囲】[Claims] (1)燃料と水を高温反応室内に酸素と共に噴射し、水
の気化占有部分と燃料、酸素の占有部分との容積むらを
均す工程と、気化水分の分解工程と、燃焼工程とよりな
る燃料・水燃焼法。
(1) Consists of a step in which fuel and water are injected together with oxygen into a high-temperature reaction chamber to equalize the volume unevenness between the vaporized portion of water and the portion occupied by fuel and oxygen, a step of decomposing vaporized water, and a combustion step. Fuel/water combustion method.
(2)燃料と水並びに添加物を高温反応室内に酸素と共
に噴射し、水の気化占有部分と燃 料、酸素の占有部分との容積むらを均す工程と、気化水
分の分解工程と、燃焼工程を同時に行うことよりなる燃
料・水燃焼法。
(2) A step in which fuel, water, and additives are injected together with oxygen into a high-temperature reaction chamber to equalize the volume unevenness between the vaporized portion of water and the portion occupied by fuel and oxygen, a step of decomposing vaporized water, and a combustion step. A fuel/water combustion method that involves performing the following at the same time.
(3)先端開口反応室の基端開口部に燃料噴射ノズルを
配設し、同反応室の内部に連通気孔耐火物を配設し、噴
射燃料と燃焼用酸素等が上記耐火物を通過するよう配置
してなる燃料・水燃焼装置。
(3) A fuel injection nozzle is provided at the base end opening of the tip-opening reaction chamber, and a continuous vent refractory is provided inside the reaction chamber, so that the injected fuel and combustion oxygen, etc. pass through the refractory. A fuel/water combustion device arranged as follows.
JP61139877A 1986-06-16 1986-06-16 Fuel / water combustion method Expired - Lifetime JPH0726107B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP61139877A JPH0726107B2 (en) 1986-06-16 1986-06-16 Fuel / water combustion method

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP61139877A JPH0726107B2 (en) 1986-06-16 1986-06-16 Fuel / water combustion method

Related Parent Applications (1)

Application Number Title Priority Date Filing Date
JP5286885A Division JPS61211396A (en) 1985-03-16 1985-03-16 Method of burning fuel-water and apparatus therefor

Publications (2)

Publication Number Publication Date
JPS6296590A true JPS6296590A (en) 1987-05-06
JPH0726107B2 JPH0726107B2 (en) 1995-03-22

Family

ID=15255647

Family Applications (1)

Application Number Title Priority Date Filing Date
JP61139877A Expired - Lifetime JPH0726107B2 (en) 1986-06-16 1986-06-16 Fuel / water combustion method

Country Status (1)

Country Link
JP (1) JPH0726107B2 (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPWO2005033582A1 (en) * 2003-10-01 2006-12-14 阿部 俊廣 Combustion device
JP2010203721A (en) * 2009-03-05 2010-09-16 Nihon Kankyo System Co Ltd Hot bulb-free hydrated fuel combustion device
WO2012077172A1 (en) * 2010-12-06 2012-06-14 株式会社ニレコ Chamber for water-mixed fuel combustion device

Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS4958101A (en) * 1972-06-26 1974-06-05
JPS54117504A (en) * 1978-03-03 1979-09-12 Agency Of Ind Science & Technol Gasification of coal
JPS5734192A (en) * 1980-08-09 1982-02-24 Babcock Hitachi Kk Water gas unit

Patent Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS4958101A (en) * 1972-06-26 1974-06-05
JPS54117504A (en) * 1978-03-03 1979-09-12 Agency Of Ind Science & Technol Gasification of coal
JPS5734192A (en) * 1980-08-09 1982-02-24 Babcock Hitachi Kk Water gas unit

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPWO2005033582A1 (en) * 2003-10-01 2006-12-14 阿部 俊廣 Combustion device
JP2010203721A (en) * 2009-03-05 2010-09-16 Nihon Kankyo System Co Ltd Hot bulb-free hydrated fuel combustion device
WO2012077172A1 (en) * 2010-12-06 2012-06-14 株式会社ニレコ Chamber for water-mixed fuel combustion device

Also Published As

Publication number Publication date
JPH0726107B2 (en) 1995-03-22

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