JP3530286B2 - Concentrated emulsion fuel material and emulsion fuel - Google Patents
Concentrated emulsion fuel material and emulsion fuelInfo
- Publication number
- JP3530286B2 JP3530286B2 JP27311095A JP27311095A JP3530286B2 JP 3530286 B2 JP3530286 B2 JP 3530286B2 JP 27311095 A JP27311095 A JP 27311095A JP 27311095 A JP27311095 A JP 27311095A JP 3530286 B2 JP3530286 B2 JP 3530286B2
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- Prior art keywords
- emulsion fuel
- water
- fuel material
- combustion
- concentrated
- 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.)
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Description
【0001】[0001]
【発明の属する技術分野】本発明は石油系液体燃料に水
を混入してなるエマルジョン燃料に関するものである。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to an emulsion fuel prepared by mixing petroleum liquid fuel with water.
【0002】[0002]
【従来の技術】従来、石油系液体燃料の燃焼排気ガス中
の煤塵と窒素酸化物の減少を図る手段として水添加エマ
ルジョン燃料を用いる方法が知られている。2. Description of the Related Art Conventionally, a method of using a water-added emulsion fuel has been known as a means for reducing soot and nitrogen oxides in combustion exhaust gas of petroleum liquid fuel.
【0003】このエマルジョン燃焼は、例えば、石油な
どの疎水性の液体化石燃料に水と少量の界面活性剤を混
入攪拌して乳化させたものであり、その原理は燃料の燃
焼において、エマルジョン燃料の油滴中の水分が急激に
水蒸気になるときの体膨張(約1700倍)の力を利用
してバーナーから出た油滴(径約300〜400μm)
を再微粒化して燃焼用空気との混合を良くし、燃焼を促
進させることで煤煙を減少させると共に、その蒸発潜熱
によって火炎温度を低くして燃焼時の窒素酸化物の発生
率を低減するようにしたものである。In this emulsion combustion, for example, hydrophobic liquid fossil fuel such as petroleum is mixed with water and a small amount of a surface-active agent and stirred to emulsify. Oil droplets (diameter about 300-400 μm) that came out of the burner by utilizing the force of body expansion (about 1700 times) when the water in the oil droplets suddenly becomes steam
To improve the mixing with combustion air and promote combustion, thereby reducing soot and smoke, and lowering the flame temperature by the latent heat of vaporization to reduce the generation rate of nitrogen oxides during combustion. It is the one.
【0004】[0004]
【発明が解決しようとする課題】ところで、このような
従来のエマルジョン燃料を構成する水と液体燃料は比重
が異なっていることから、これを貯蔵タンク等で貯蔵す
ると2〜3週間で水と油の層に分離してしまい、BC重
油を除き、長期間の保存は不可能であった。By the way, since the specific gravity of water and liquid fuel which constitute such a conventional emulsion fuel is different, if they are stored in a storage tank or the like, water and oil will be formed within 2-3 weeks. It was separated into two layers, and it was impossible to store it for a long period of time except BC heavy oil.
【0005】また、従来のエマルジョン燃料では水混入
率1%に対して熱損失が0.08%あるため、例えば、
20%の水を混入しただけでも、約1.6%の熱損失を
招いてしまい、高い熱効率が求められるボイラーには使
用することができないといった問題点があった。Further, in the conventional emulsion fuel, the heat loss is 0.08% with respect to the water mixing ratio of 1%.
Even if only 20% of water is mixed, it causes a heat loss of about 1.6%, and there is a problem that it cannot be used for a boiler that requires high thermal efficiency.
【0006】そこで、本発明は上述した欠点を有効に解
決するために案出されたものであり、その目的は、煤塵
と窒素酸化物の低減は勿論、長期の保存でも分離せず安
定性に優れ、かつ、高熱効率のボイラーにも問題なく使
用することができる新規な濃縮エマルジョン燃料材及び
これに、使用前に水を同量以上混入したエマルジョン燃
料を提供することにある。Therefore, the present invention has been devised in order to effectively solve the above-mentioned drawbacks, and its purpose is not only to reduce soot and nitrogen oxides, but also to maintain stability without separation even during long-term storage. It is an object of the present invention to provide a novel concentrated emulsion fuel material which is excellent and can be used without problem in a boiler having a high thermal efficiency, and an emulsion fuel containing water in the same amount or more before use.
【0007】[0007]
【課題を解決するための手段】上記目的を達成するため
に本発明は、アニオン系界面活性剤のアルキルエーテル
硫酸エステルナトリウムとアルキルベンゼン酸ナトリウ
ムとを混合均一化した合成アニオン系界面活性溶液剤に
蒸留水を投入攪拌し、気泡性を均一に含有するムース状
乳化剤に任意量の石油系液体燃料材を混入攪拌してなる
ものである。In order to achieve the above object, the present invention is directed to a synthetic anionic surfactant solution which is prepared by mixing and homogenizing sodium alkyl ether sulfate of anionic surfactant and sodium alkylbenzene. Water is charged and stirred, and an arbitrary amount of petroleum-based liquid fuel material is mixed and stirred in a mousse-like emulsifier that uniformly contains foamability.
【0008】すなわち、合成アニオン系界面活性剤に蒸
溜水を加えて製造されたムース状の乳化剤と石油系液体
燃料を混入攪拌して製造された濃縮エマルジョン燃料
は、油中水滴特性のため、親水基性があり、攪拌による
気泡による体積が大きくなって水分との接触面積が大き
くなるため、多量の水分を混入できる。そして、この混
入した水分の粒子は気泡によって比重が軽くなり、石油
系液体燃料の比重とほぼ同じ比重となることにより、長
期間(2〜3ヶ月間)油成分とに分離しない化学的安定
性の高いエマルジョン状態が保持される。That is, a concentrated emulsion fuel prepared by mixing a mousse-like emulsifier prepared by adding distilled water to a synthetic anionic surfactant and a petroleum-based liquid fuel and stirring it is hydrophilic because of its water-in-oil characteristic. Since it is basic and has a large volume due to bubbles due to stirring and a large contact area with water, a large amount of water can be mixed. The particles of the mixed water have a low specific gravity due to bubbles, and have a specific gravity almost the same as the specific gravity of the petroleum-based liquid fuel, so that the chemical stability is not separated into the oil component for a long period (2 to 3 months). High emulsion state is maintained.
【0009】また、このように高い化学的安定性を有す
る濃縮エマルジョン燃料材に、容量比で1〜1.5倍の
水を加えることにより、水の水素と酸素を分離活用する
ために、燃焼用の空気の必要量が少なくてすむので、燃
焼による排気ガス中の煤塵と窒素酸化物が低減されると
共に、燃焼中の火炎温度を上昇して高熱効率の燃焼を行
うことができる。但し、水を同量以上加えるので、着火
温度は400℃以上の雰囲気中を必要とするが、着火後
は連続燃焼が可能となる。Further, by adding 1 to 1.5 times by volume of water to the concentrated emulsion fuel material having such high chemical stability, combustion is performed in order to separate and utilize hydrogen and oxygen of the water. Since the required amount of air for use is small, soot and nitrogen oxides in the exhaust gas due to combustion can be reduced, and the flame temperature during combustion can be increased to perform combustion with high thermal efficiency. However, since the same amount or more of water is added, an ignition temperature of 400 ° C. or more is required in the atmosphere, but continuous combustion is possible after ignition.
【0010】すなわち、従来では、燃焼排ガス中の窒素
酸化物の発生を抑えるためには、水分の含水率を多くし
て火炎温度を低くする必要があるが、そうすると、水分
の蒸発潜熱により、熱効率が低下してしまい、高熱効率
のボイラーではエマルジョン燃料を使用することが困難
であった。しかしながら、本発明のエマルジョン燃料
は、少ない燃焼空気で未燃焼油を完全燃焼させることか
ら、不完全燃焼に起因する煤塵は勿論、燃焼温度を高く
しても窒素酸化物の発生を大幅に低減することができ
る。That is, conventionally, in order to suppress the generation of nitrogen oxides in the combustion exhaust gas, it is necessary to increase the water content of water to lower the flame temperature. Then, the latent heat of vaporization of water causes thermal efficiency. It was difficult to use emulsion fuel in a high thermal efficiency boiler. However, the emulsion fuel of the present invention completely burns unburned oil with a small amount of combustion air, so that not only soot and dust caused by incomplete combustion but also generation of nitrogen oxides is significantly reduced even when the combustion temperature is raised. be able to.
【0011】[0011]
【発明の実施の形態】以下、本発明の実施の形態を添付
図面に基づいて詳述する。BEST MODE FOR CARRYING OUT THE INVENTION Embodiments of the present invention will be described in detail below with reference to the accompanying drawings.
【0012】上述したように、本発明の濃縮エマルジョ
ン燃料材は、アニオン系界面活性剤のアルキルエーテル
硫酸エステルナトリウムとアルキルベンゼン酸ナトリウ
ムとを混合均一化した合成アニオン系界面活性溶液剤に
蒸留水を投入攪拌し、気泡性を均一に含有するムース状
乳化剤に任意量の石油系液体燃料材を混入攪拌してなる
ものである。As described above, in the concentrated emulsion fuel material of the present invention, distilled water is added to a synthetic anionic surfactant solution agent in which sodium alkyl ether sulfate as anionic surfactant and sodium alkylbenzene are mixed and homogenized. It is prepared by stirring and mixing an arbitrary amount of a petroleum-based liquid fuel material with a mousse-like emulsifier that uniformly contains foamability.
【0013】次に、この濃縮エマルジョン燃料材の製造
方法の一例について説明すると、図1に示すように、先
ず常温(室温)、常圧(大気圧)下で、ビーカー1にア
ニオン系界面活性剤10のアルキルエーテル硫酸エステ
ルナトリウムと、アルキルベンゼンスルホン酸ナトリウ
ムをそれぞれ容量比3(例えば300cc)と容量比1
(100cc)ずつ混合し、均一に攪拌してアニオン系
界面活性剤溶液を生成し、このアニオン系界面活性剤溶
液に容量比6(600cc)の蒸溜水11を徐々に混入
攪拌し泡立たせた後、さらに、プロペラ攪拌機2で泡が
細かくムース状なるまでにゆっくり攪拌して気泡の入っ
たムース状の乳化剤3を生成する。次に、このムース状
の乳化剤3をさらに大きな容器4に移し替えて、その中
に容量比で150(15L)〜200(20L)倍の石
油、灯油、重油、軽油等の液体化石炭化水素分留分中の
オレフィン系不飽和炭化水素5をホイップ状態を維持し
つつ攪拌しながら、最初は徐々に滴下して乳化剤を連続
相、オレフィン系不飽和炭化水素5を分散相としたO/
W型(水中油滴型)エマルジョン燃料を生成する。そし
て、投入されるオレフィン系不飽和炭化水素の量が乳化
剤3の量を上回ると連続相と分散相が逆転して、W/O
型(油中水滴型)エマルジョン燃料が生成される。さら
に投入されるオレフィン系不飽和炭化水素の量が増える
とゲル状態を経た後、凝固して半透明のゲル状態とな
り、含水率0.3〜0.4%程度の濃縮エマルジョン燃
料6が生成される。そして、この濃縮エマルジョン燃料
材6をさらに大きい容器7に移し変えた後、この濃縮エ
マルジョン燃料材6に、これに対して容量比1.0〜
1.5倍の水8を混入して攪拌してエマルジョン燃料9
を生成することになる。Next, an example of the method for producing this concentrated emulsion fuel material will be described. As shown in FIG. 1, first, an anionic surfactant is added to the beaker 1 at room temperature (room temperature) and atmospheric pressure (atmospheric pressure). 10 sodium alkyl ether sulphate and sodium alkylbenzene sulphonate in a volume ratio of 3 (eg 300 cc) and a volume ratio of 1 respectively.
(100 cc) each, and stirred uniformly to form an anionic surfactant solution. Distilled water 11 with a volume ratio of 6 (600 cc) was gradually mixed into this anionic surfactant solution, and the mixture was stirred and bubbled. Further, the propeller stirrer 2 is gently stirred until the bubbles become finely mousse-like to generate the mousse-like emulsifier 3 containing bubbles. Next, the mousse-like emulsifier 3 is transferred to a larger container 4, and 150 (15 L) to 200 (20 L) times by volume of liquefied coal hydrogenated petroleum, kerosene, heavy oil, light oil, etc. While stirring the olefinic unsaturated hydrocarbon 5 in the distillate while maintaining the whipping state, first, the emulsifier was gradually added dropwise to form a continuous phase of the emulsifier and a dispersed phase of the olefinic unsaturated hydrocarbon 5 O /
It produces a W-type (oil-in-water type) emulsion fuel. When the amount of the olefinic unsaturated hydrocarbon added exceeds the amount of the emulsifier 3, the continuous phase and the dispersed phase are reversed and W / O
A type (water-in-oil type) emulsion fuel is produced. When the amount of the olefinic unsaturated hydrocarbon added further goes through a gel state, it solidifies and becomes a semitransparent gel state, and a concentrated emulsion fuel 6 having a water content of about 0.3 to 0.4% is produced. It Then, after transferring the concentrated emulsion fuel material 6 to a larger container 7, the concentrated emulsion fuel material 6 has a volume ratio of 1.0 to
Emulsion fuel 9 by mixing 1.5 times water 8 and stirring
Will be generated.
【0014】このようにして得られた濃縮エマルジョン
燃料材はゲル状となっているため、その組成は安定して
おり、長期間(2〜3ケ月以上)の保存が可能となる。Since the concentrated emulsion fuel material thus obtained is in the form of gel, its composition is stable and can be stored for a long period (2 to 3 months or more).
【0015】また、この濃縮エマルジョン燃料材に使用
前に容量比で1〜1.5倍の水を混入したエマルジョン
燃料を燃焼させると、少ない燃焼空気で未燃焼油を完全
燃焼させることができることから、不完全燃焼に起因す
る煤塵の発生量は勿論、必要とする燃焼空気量が少なく
なるため、火炎温度を高くしても窒素酸化物の発生を大
幅に低減することができる。When the concentrated emulsion fuel material is burned with an emulsion fuel containing 1 to 1.5 times the volume ratio of water before use, unburned oil can be completely burned with a small amount of combustion air. Of course, the amount of soot and dust generated due to incomplete combustion is reduced, and the required amount of combustion air is reduced. Therefore, even if the flame temperature is raised, the generation of nitrogen oxides can be significantly reduced.
【0016】[0016]
【実施例】次に、本発明の具体的実施例を説明する。EXAMPLES Next, specific examples of the present invention will be described.
【0017】先ず、常温(室温)、常圧(大気圧)下
で、容量が300cc程度のビーカーにアニオン系界面
活性剤10のアルキルエーテル硫酸エステルナトリウム
と、アルキルベンゼンスルホン酸ナトリウムをそれぞれ
30ccと10ccずつ混合し、均一に攪拌してアニオ
ン系界面活性剤混合液を生成し、このアニオン系界面活
性剤混合液に60ccの蒸溜水を徐々に混入攪拌し泡立
たせた後、さらに、プロペラ攪拌機で泡が細かくムース
状なるまで1000rpm以下で攪拌して気泡の入った
ムース状の乳化剤を生成した。First, at room temperature (room temperature) and atmospheric pressure (atmospheric pressure), sodium alkyl ether sulfate of anionic surfactant 10 and sodium alkylbenzene sulfonate are added to a beaker having a capacity of about 300 cc and 30 cc and 10 cc, respectively. After mixing and stirring uniformly, an anionic surfactant mixed solution is generated, and 60 cc of distilled water is gradually mixed into this anionic surfactant mixed solution to stir and foam, and then a propeller stirrer is used to generate bubbles. The mixture was stirred at 1000 rpm or less until it became a fine mousse, and a mousse emulsifier containing bubbles was produced.
【0018】次に、このムース状の乳化剤をさらに大き
な容器に移し変えて、その中に15Lの石油、灯油、重
油、軽油等の液体化石炭化水素分留分中のオレフィン系
不飽和炭化水素をホイップ状態を維持しつつ攪拌しなが
ら、W/O型(油中水滴型)の濃縮エマルジョン燃料材
を生成した。Next, the mousse-like emulsifier was transferred to a larger container, and 15 L of petroleum, kerosene, heavy oil, light oil, and the like, olefinic unsaturated hydrocarbons in the liquefied coal-hydrogen fraction were fractionated therein. A W / O type (water-in-oil type) concentrated emulsion fuel material was produced while stirring while maintaining the whipped state.
【0019】そして、この濃縮エマルジョン燃料材をさ
らに大きい容器に移し替えた後、この濃縮エマルジョン
燃料材に、これに対してそれぞれ1.0〜1.5倍の水
を混入して攪拌し、30〜約40Lの白色のエマルジョ
ン燃料(燃料A、燃料B)を2種類製造した(燃料A=
濃縮エマルジョン燃料材:47.5%、水:52.5
%、燃料B=濃縮エマルジョン燃料材:50.0%、
水:50.0%)。Then, after transferring the concentrated emulsion fuel material to a larger container, 1.0 to 1.5 times of water is mixed into the concentrated emulsion fuel material, and the mixture is stirred. ~ 2 types of white emulsion fuel (fuel A, fuel B) of about 40 L were produced (fuel A =
Concentrated emulsion fuel material: 47.5%, water: 52.5
%, Fuel B = concentrated emulsion fuel material: 50.0%,
Water: 50.0%).
【0020】次に、図2に示すようなカマド型の炉を用
い、この炉内温度を予め400℃に一定に保つと共に、
この炉に3.8Lの水を張った容器を備え、上記燃料
A、B及び灯油をそれぞれ燃料として用い、この容器内
の水温が26℃から95℃に達するまでの時間と燃料消
費率を測定すると共に、燃焼排ガス中の煤塵と窒素酸化
物の量を測定した。Next, using a camouflage type furnace as shown in FIG. 2, the temperature inside the furnace was kept constant at 400 ° C. in advance, and
This furnace was equipped with a 3.8 L container filled with water, and the above fuels A, B and kerosene were used as fuels, and the time until the water temperature in this container reached from 26 ° C to 95 ° C and the fuel consumption rate were measured. In addition, the amounts of soot and nitrogen oxides in the combustion exhaust gas were measured.
【0021】この結果、図3に示すように、灯油を燃料
として用いた場合には、炉に備えられた容器内の水温が
所定温度(95℃)に達するまでの所要時間及び消費油
量は、それぞれ8分40秒、364ccであったのに対
し、本発明に係るエマルジョン燃料A、Bを用いた場合
はいずれも所要時間、消費油量は灯油の半分以下であ
り、優れた燃焼効率を発揮することが分かった。また、
燃焼排ガス中の煤塵と窒素酸化物の発生量も灯油を用い
た場合より大幅に減少し、高い燃焼効率と、煤塵及び窒
素酸化物の排出量を大幅に抑制されることが実証され
た。さらに、本発明に係る濃縮エマルジョン燃料材と従
来のエマルジョン燃料を同じ条件で保管しておいたとこ
ろ、従来のエマルジョン燃料は2週間で油と水分に分離
してしまったのに対し、本発明に係る濃縮エマルジョン
燃料材は2ヶ月以上経っても分離などが発生せず、高い
化学的安定性を発揮した。As a result, as shown in FIG. 3, when kerosene is used as the fuel, the time required for the water temperature in the vessel provided in the furnace to reach a predetermined temperature (95 ° C.) and the amount of oil consumed are , 8 minutes and 40 seconds and 364 cc, respectively, whereas in the case of using the emulsion fuels A and B according to the present invention, the time required and the amount of oil consumed are half or less of those of kerosene, and excellent combustion efficiency is obtained. I found it to work. Also,
It was also proved that the amount of soot and nitrogen oxides in the flue gas was significantly reduced compared with the case of using kerosene, and that the high combustion efficiency and the emission of soot and nitrogen oxides were significantly suppressed. Furthermore, when the concentrated emulsion fuel material according to the present invention and the conventional emulsion fuel were stored under the same conditions, the conventional emulsion fuel separated into oil and water in two weeks, whereas The concentrated emulsion fuel material did not cause separation or the like even after 2 months or more, and exhibited high chemical stability.
【0022】[0022]
【発明の効果】以上、要するに本発明によれば、水と液
体化石燃料が分離し難くなって化学的安定性が向上する
ため、長期間の保存が可能となる。また、必要とする燃
焼空気の量が少なくても高い熱効率を発揮することがで
きるため、燃焼温度を上昇させても煤塵や窒素酸化物の
発生量が大幅に抑制される等といった優れた効果を有す
る。As described above, in short, according to the present invention, it becomes difficult to separate water and liquid fossil fuel, and the chemical stability is improved, so that it can be stored for a long period of time. Further, even if the required amount of combustion air is small, high thermal efficiency can be exhibited, so even if the combustion temperature is increased, the amount of soot and nitrogen oxides generated is greatly suppressed, which is an excellent effect. Have.
【図1】本発明に係る濃縮エマルジョン燃料材及びエマ
ルジョン燃料の製造方法の一形態を示す概略図である。FIG. 1 is a schematic view showing one embodiment of a concentrated emulsion fuel material and a method for producing an emulsion fuel according to the present invention.
【図2】本発明に係るエマルジョン燃料の燃焼試験方法
を示す概略図である。FIG. 2 is a schematic diagram showing a combustion test method for emulsion fuel according to the present invention.
【図3】燃料別の燃焼による昇温度試験結果を示すグラ
フ図である。FIG. 3 is a graph showing a temperature rise test result by combustion for each fuel.
3 乳化剤 5 液体燃料 6 濃縮エマルジョン燃料材 8 水 9 エマルジョン燃料 10 界面活性剤 11 蒸溜水 3 emulsifier 5 Liquid fuel 6 Concentrated emulsion fuel material 8 water 9 Emulsion fuel 10 Surfactant 11 distilled water
───────────────────────────────────────────────────── フロントページの続き (58)調査した分野(Int.Cl.7,DB名) C10L 1/32 JICSTファイル(JOIS)─────────────────────────────────────────────────── ─── Continuation of front page (58) Fields surveyed (Int.Cl. 7 , DB name) C10L 1/32 JISST file (JOIS)
Claims (2)
ル硫酸エステルナトリウムとアルキルベンゼン酸ナトリ
ウムとを混合均一化した合成アニオン系界面活性溶液剤
に蒸留水を投入攪拌し気泡性を均一に含有するムース状
乳化剤に、石油系液体燃料材を混入攪拌してなることを
特徴とする濃縮エマルジョン燃料材。1. A mousse-like emulsifier that uniformly mixes and agitates distilled water into a synthetic anionic surfactant solution obtained by mixing and homogenizing sodium alkyl ether sulfate as an anionic surfactant and sodium alkylbenzenate. A concentrated emulsion fuel material, characterized in that a petroleum-based liquid fuel material is mixed and stirred.
に、容量比で1〜1.5倍の水を混入攪拌してなること
を特徴とするエマルジョン燃料。2. An emulsion fuel, characterized in that the concentrated emulsion fuel material according to claim 1 is mixed with water in a volume ratio of 1 to 1.5 times and stirred.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP27311095A JP3530286B2 (en) | 1995-10-20 | 1995-10-20 | Concentrated emulsion fuel material and emulsion fuel |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP27311095A JP3530286B2 (en) | 1995-10-20 | 1995-10-20 | Concentrated emulsion fuel material and emulsion fuel |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPH09111267A JPH09111267A (en) | 1997-04-28 |
| JP3530286B2 true JP3530286B2 (en) | 2004-05-24 |
Family
ID=17523276
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP27311095A Expired - Fee Related JP3530286B2 (en) | 1995-10-20 | 1995-10-20 | Concentrated emulsion fuel material and emulsion fuel |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JP3530286B2 (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2009280780A (en) * | 2008-05-26 | 2009-12-03 | Kanagawa Kogyo Reform:Kk | Gel liquid fuel, o/w/o triplex structure colloidal fuel, and method and device for producing it |
Families Citing this family (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| EP0922081A1 (en) * | 1997-05-30 | 1999-06-16 | Ju Heung Sung | Emulsified fuel |
| CN103897765B (en) * | 2014-04-03 | 2016-07-13 | 冯智勇 | A kind of coal-burning boiler combustion adjuvant of efficient energy-saving and emission-reducing |
-
1995
- 1995-10-20 JP JP27311095A patent/JP3530286B2/en not_active Expired - Fee Related
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2009280780A (en) * | 2008-05-26 | 2009-12-03 | Kanagawa Kogyo Reform:Kk | Gel liquid fuel, o/w/o triplex structure colloidal fuel, and method and device for producing it |
Also Published As
| Publication number | Publication date |
|---|---|
| JPH09111267A (en) | 1997-04-28 |
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