JP2012241185A - Method of producing additive for supramolecular fuel, and method of producing the supramolecular fuel using the additive - Google Patents

Method of producing additive for supramolecular fuel, and method of producing the supramolecular fuel using the additive Download PDF

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JP2012241185A
JP2012241185A JP2011125785A JP2011125785A JP2012241185A JP 2012241185 A JP2012241185 A JP 2012241185A JP 2011125785 A JP2011125785 A JP 2011125785A JP 2011125785 A JP2011125785 A JP 2011125785A JP 2012241185 A JP2012241185 A JP 2012241185A
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Shuichi Suehiro
修一 末廣
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Abstract

PROBLEM TO BE SOLVED: To provide an additive for producing supramolecular fuel, capable of improving a combustion state by mixing oil such as an A-heavy oil with water, to enhance a combustion efficiency.SOLUTION: The additive for producing the supramolecular fuel for mixing the oil such as the A-heavy oil with the water contains, by weight, 68.6%-75.2% of oleic acid, 12.3%-14.1% of methanol, 3.0%-3.8% of linoleic acid, 6.8%-8.6% of propylene glycol, and 4.0%-5.5% of ammonia.

Description

本発明は、A重油、灯油、軽油等の油と水とを混合して得られる超分子化燃料として、特に油と水が分離するエマルジョン(乳化)状態にはならず、また、植物性油を原料に含み、環境汚染物質を増加させることのない超分子化燃料製造用添加剤の製造方法と該添加剤を用いた超分子化燃料の製造方法に関するものである。  The present invention is a supermolecular fuel obtained by mixing oil such as heavy oil A, kerosene, and light oil with water, and is not particularly in an emulsion (emulsified) state in which the oil and water are separated. The present invention relates to a method for producing an additive for producing a supramolecular fuel that does not increase environmental pollutants and a method for producing a supramolecular fuel using the additive.

近年、A重油、灯油、軽油等の化石燃料を使用する際に排出されるCO2等の環境負荷物質の低減化の観点から、これらの燃料に適量の水を混合させた、いわゆるエマルジョン燃料の研究が盛んに行われている。  In recent years, research on so-called emulsion fuels, in which an appropriate amount of water is mixed with these fuels from the viewpoint of reducing environmentally hazardous substances such as CO2 emitted when using fossil fuels such as heavy oil A, kerosene, and light oil Has been actively conducted.

しかしながら、従来のエマルジョン燃料は、燃料と水が分離することにより備蓄や輸送が困難であった。また、含水の影響による燃焼温度・カロリーの低下や熱効率の低下による燃費の低下、燃焼室の腐食など様々な欠点や問題点を有していた。  However, conventional emulsion fuels are difficult to stockpile and transport due to separation of fuel and water. In addition, it has various drawbacks and problems such as a decrease in combustion temperature and calories due to the influence of water content, a decrease in fuel consumption due to a decrease in thermal efficiency, and corrosion in the combustion chamber.

これらの要因が重なり、数十年前から研究、開発が繰り返されているにもかかわらずエマルジョン燃料は市場での普及がなされていなかった。  Even though these factors overlap and research and development have been repeated for decades, emulsion fuel has not been popularized in the market.

この発明は、上記のような問題点に鑑み、その問題点を解決しようと考え出されたもので、その目的とするところは、油と水を均一に混合融合状態として分離することなく、しかも燃焼効率を高めることができ、また、環境負荷物質を低減させることのできる超分子化燃料製造用添加剤の製造方法および該添加剤を用いた超分子化燃料の製造方法を提供することを目的とする。  The present invention has been devised to solve the above problems in view of the above problems, and the object of the present invention is to separate oil and water into a uniform mixed and fused state, and An object of the present invention is to provide a method for producing an additive for producing a supramolecular fuel capable of enhancing combustion efficiency and reducing environmental load substances, and a method for producing a supramolecular fuel using the additive. And

本発明の超分子化燃料製造用添加剤は、A重油等の油と水とを混合するため、オレイン酸68.6%〜75.2%、メタノール12.3%〜14.1%、リノール酸3.0%〜3.8%、プロピレングリコール6.8%〜8.6%、及びアンモニア4.0%〜5.5%を含むものである。  The additive for producing supramolecularized fuel of the present invention mixes oil such as A heavy oil and water, so that oleic acid is 68.6% -75.2%, methanol 12.3% -14.1%, linole It contains 3.0% to 3.8% acid, 6.8% to 8.6% propylene glycol, and 4.0% to 5.5% ammonia.

本発明の超分子化燃料製造用添加剤の製造方法は、オレイン酸を68.6%〜75.2%を攪拌機に入れ、次にメタノール12.3%〜14.1%を攪拌機に入れ、次にリノール酸3.0%〜3.8%を攪拌機に入れ、次にプロピレングリコール6.8%〜8.6%を攪拌機に入れて攪拌混合する工程と、アンモニア4.0%〜5.5%を攪拌機に入れて攪拌混合する工程とからなる。  In the method for producing an additive for producing a supramolecular fuel according to the present invention, 68.6% to 75.2% of oleic acid is put into a stirrer, and then 12.3% to 14.1% of methanol is put into a stirrer. Next, 3.0% to 3.8% of linoleic acid is put into a stirrer, and then 6.8% to 8.6% of propylene glycol is put into the stirrer and stirred and mixed, and 4.0% to 5.5 of ammonia. And 5% in a stirrer and stirring and mixing.

本発明の超分子化燃料の製造方法は、上記超分子化燃料製造用添加剤を15%〜25%と油50%〜60%とを攪拌混合する工程と、これに水20%〜30%を攪拌混合する工程とを有し製造するものである。  The method for producing a supramolecular fuel according to the present invention comprises a step of stirring and mixing 15% to 25% of the above additive for producing a supramolecular fuel and 50% to 60% oil, and 20% to 30% water. With stirring and mixing.

本発明の超分子化燃料製造用添加剤により、水の粒子を微粒化して油中にムラなく均一に混合させることができるため、油と水を混ぜてもエマルジョン化にすることがなく透明性を有しており、長期間放置しても分離することがない。  The additive for producing a supramolecular fuel according to the present invention makes it possible to atomize water particles and mix them uniformly in the oil without any unevenness. And will not separate even if left for a long period of time.

超分子化燃料は、油に水が完全に溶け込んでおり、燃焼時には完全燃焼に近い状況となるため熱効率が低下することなく、また、CO2等環境負荷物質の発生も抑制することができる。  In the supramolecular fuel, water is completely dissolved in the oil, and it becomes a state close to complete combustion at the time of combustion. Therefore, thermal efficiency does not decrease and generation of environmental load substances such as CO 2 can be suppressed.

油と水が分離する最大の要因は、その両者の表面張力が極端に違うためであるが、本発明の超分子化燃料用添加剤を使えば油と水の表面張力をほぼ同じものとすることができ、その結果、水と油の分離を防ぐことができる。  The biggest cause of separation of oil and water is that the surface tension of the two is extremely different, but the surface tension of oil and water is made almost the same if the additive for supramolecular fuel of the present invention is used. As a result, separation of water and oil can be prevented.

本発明の超分子化燃料製造用添加剤は前記の通りであるが、先ずその製造方法について記載する。  The additive for producing a supramolecular fuel according to the present invention is as described above. First, the production method will be described.

本発明の超分子化燃料用添加剤の主成分であるオレイン酸(Oleic Acid)を添加剤の重量比で68.6%〜75.2%を攪拌機に入れ、次にメタノールを重量比で12.3%〜14.1%を入れ、次にリノール酸を重量比で3.0%〜3.8%攪拌機に入れ、次にプロピレングリコールを重量比で6.8%〜8.6%を攪拌機に入れて5〜10分攪拌して混合する。  The oleic acid (Oleic Acid), which is the main component of the additive for the supramolecular fuel of the present invention, is placed in a stirrer at a weight ratio of 68.6% to 75.2%, and then methanol is added at a weight ratio of 12%. .3% to 14.1%, then linoleic acid in a weight ratio of 3.0% to 3.8% and then propylene glycol in a weight ratio of 6.8% to 8.6%. Put in a stirrer and stir for 5-10 minutes to mix.

攪拌機は任意・公知のものが使用される。本製造方法では、循環モーターにより循環させるだけの簡単な攪拌を行う。  Arbitrary and publicly known stirrers are used. In this production method, simple agitation is performed by simply circulating with a circulation motor.

次いで、アンモニア(Ammonium hydroxide)を重量比で4.0%〜5.5%を約30分かけて混入する。この時、混入後発熱が始まるが、発熱を52℃以下に保持しながら少量ずつ投入することが重要である。攪拌中に気泡状物質が発生するが、気泡の発生は化学反応の進行を意味し、この消滅が反応終了を意味する。  Next, ammonia (Ammonium hydride) is mixed at a weight ratio of 4.0% to 5.5% over about 30 minutes. At this time, heat generation starts after mixing, but it is important to add small amounts while keeping the heat generation at 52 ° C. or less. Although a bubble-like substance is generated during stirring, the generation of bubbles means the progress of a chemical reaction, and this disappearance means the end of the reaction.

この気泡が消滅した後10分〜15分攪拌する。  After the bubbles disappear, the mixture is stirred for 10 to 15 minutes.

最終工程終了後、液温が35℃以下になれば完成となる。  When the liquid temperature is 35 ° C. or lower after the final process is completed, the process is completed.

本発明で使用される5種類の成分である原材料の主な性質は次の通りである。  The main properties of the raw materials, which are the five components used in the present invention, are as follows.

オレイン酸(oleic Acid.分子式:C18H34O2)・・・分子量282.47g/mol。比重(25℃)0.89g/cm3。融点16.3℃。沸点195℃/100pa。外観は浅黄色から黄褐色をした液体で、ラードのような臭いをしている動植物に含まれる脂肪酸。水には溶けず、有機溶剤に溶ける。本発明の超分子化燃料製造用添加剤の主成分。凝固点8℃以下が好ましい。  Oleic acid (oleic Acid. Molecular formula: C18H34O2) ... molecular weight 282.47 g / mol. Specific gravity (25 ° C.) 0.89 g / cm 3. Melting point 16.3 ° C. Boiling point 195 ° C / 100pa. The appearance is a light yellow to yellowish brown liquid, fatty acid contained in animals and plants that smell like lard. Not soluble in water but soluble in organic solvents. The main component of the additive for producing supramolecular fuel according to the present invention. A freezing point of 8 ° C. or lower is preferred.

メタノール(Methanol分子式:CH4O)・・・分子量32.04g/mol。比重(20℃)0.7915g/cm3。融点−97.8℃。沸点64.7℃。外観は無色透明液体。水溶性。水とはどのような比率でも溶けあえる。  Methanol (Methanol molecular formula: CH4O) ... molecular weight 32.04 g / mol. Specific gravity (20 ° C.) 0.7915 g / cm 3. Melting point-97.8 ° C. Boiling point 64.7 ° C. Appearance is colorless and transparent liquid. Water soluble. It can be dissolved in any ratio with water.

リノール酸(linoleic分子式:C18H32O2)・・・分子量280.44548g/mol。比重0.9g/cm3。
融点−5℃。沸点229℃。ベニバナ油やコーン油に多く含まれ、石鹸や乳化剤などの製造に用いられ化粧品にも使われている。
Linoleic acid (linoleic molecular formula: C18H32O2) ... molecular weight 280.44548 g / mol. Specific gravity 0.9 g / cm3.
Melting point -5 ° C. Boiling point 229 ° C. It is abundant in safflower oil and corn oil and is used in the manufacture of soaps and emulsifiers and in cosmetics.

プロピレングリコール(propylene glycol分子式:C3H8O2)・・・分子量76.09g/mol。比重1.036g/cm3。融点−59℃。沸点188.2℃。外観は無色、無味、無臭で吸湿性のある液体。保湿剤、潤滑剤、乳化剤、不凍液として用いられる。  Propylene glycol (propylene glycol molecular formula: C3H8O2) ... molecular weight 76.09 g / mol. Specific gravity 1.036 g / cm3. Melting point -59 ° C. Boiling point 188.2 ° C. Appearance is colorless, tasteless, odorless and hygroscopic. Used as a moisturizer, lubricant, emulsifier, antifreeze.

アンモニア(Ammonium hydroxide分子式:NH3)・・・モル質量17.0306g/mol。密度0.6942。融点−77.73℃。沸点−33.34℃。外観は常温常圧では無色の気体で、特有の強い刺激臭を持つ。水によく溶けるため、水溶液(アンモニア水)として使用されることも多い。  Ammonia (Ammonium hydride molecular formula: NH3) ... Molar mass 17.0306 g / mol. Density 0.6942. Melting point-77.73 ° C. Boiling point -33.34 ° C. Appearance is a colorless gas at room temperature and normal pressure, and has a characteristic strong irritating odor. Since it dissolves well in water, it is often used as an aqueous solution (ammonia water).

上記製造方法により、重量比でオレイン酸68.6%〜75.2%、メタノール12.3%〜14.1%、リノール酸3.0%〜3.8%、プロピレングリコール6.8%〜8.6%およびアンモニア4.0%〜5.5%を含む超分子化燃料製造用添加剤が製造される。  According to the above production method, oleic acid in a weight ratio of 68.6% to 75.2%, methanol 12.3% to 14.1%, linoleic acid 3.0% to 3.8%, propylene glycol 6.8% to An additive for producing a supramolecular fuel containing 8.6% and 4.0% to 5.5% ammonia is produced.

該添加剤の5成分の混合割合について説明する。該添加剤を用いて超分子化燃料を製造する場合(製造方法は後述する)、オレイン酸は重量比で75.2%を超えると乳化の進行は鈍化し、他の成分の機能を抑制することになる。また、68.6%未満では十分な乳化を達成できない。  The mixing ratio of the five components of the additive will be described. When a supramolecular fuel is produced using the additive (the production method will be described later), if oleic acid exceeds 75.2% by weight, the progress of emulsification slows down and the functions of other components are suppressed. It will be. Further, if it is less than 68.6%, sufficient emulsification cannot be achieved.

メタノールは14.1%を超えると水、油の表面張力の変化が鈍化し、12.3%未満では表面張力の変化が不十分であった。  When the methanol content exceeded 14.1%, the change in the surface tension of water and oil slowed down, and when it was less than 12.3%, the change in the surface tension was insufficient.

リノール酸は重量比で3.8%を超えると水分子の結合力の増加が鈍化し、3.0%未満では結合力が不十分であった。  When the weight ratio of linoleic acid exceeded 3.8%, the increase in the binding strength of water molecules slowed down, and when it was less than 3.0%, the binding strength was insufficient.

プロピレングリコールは、8.6%を超えると添加剤の改質作用が鈍化し、6.8%未満では添加剤の改質作用が不十分であった。  When propylene glycol exceeds 8.6%, the modifying action of the additive slows down, and when it is less than 6.8%, the modifying action of the additive is insufficient.

アンモニアは5.5%を超えるとメタノールのエステル作用が鈍化し、4.0%未満ではメタノールのエステル作用が不十分であった。  When ammonia exceeds 5.5%, the ester action of methanol was slowed down, and when less than 4.0%, the ester action of methanol was insufficient.

次に前記のようにして製造された添加剤を用いて油・水混合燃料である超分子化燃料を製造する方法について説明する。  Next, a method for producing a supramolecular fuel, which is an oil / water mixed fuel, using the additive produced as described above will be described.

まず、添加剤と水とを混合するための油を用意する。本発明の添加剤が対象とする油は、A重油、灯油、軽油などで、これらの油に水を混合せしめることが可能である。  First, an oil for mixing the additive and water is prepared. The oils targeted by the additive of the present invention are A heavy oil, kerosene, light oil, etc., and water can be mixed with these oils.

最初に、前記添加剤製造の攪拌機と同様の攪拌機により、油に前記のようにして製造された添加剤を混入して循環攪拌する。攪拌時間は5分〜10分間行う。油の中にまんべんなく均一に添加剤なじませることが重要であり、こうすることでこの後加えられる水を油中に溶解せしめることが可能となる。  First, the additive produced as described above is mixed into the oil by a stirrer similar to the stirrer for producing the additive, and the mixture is circulated and stirred. The stirring time is 5 minutes to 10 minutes. It is important to make the additive evenly and evenly distributed in the oil, so that water added thereafter can be dissolved in the oil.

次に、本発明の添加剤が加えられた油に水を加えてよく攪拌する。攪拌時間は10〜15分間行うことが好ましい。水を加えた直後のエマルジョン状態(乳化状態)を経て、完全に水が油に可溶化し、透明性を有する油・水混合燃料が製造される。  Next, water is added to the oil to which the additive of the present invention has been added and stirred well. The stirring time is preferably 10 to 15 minutes. Through the emulsion state (emulsified state) immediately after adding water, water is completely solubilized in the oil, and an oil / water mixed fuel having transparency is produced.

本発明の添加剤は、硬水、軟水など水の種類についても特に限定することなく通常の水道水や井戸水を用いることができる。  As the additive of the present invention, normal tap water or well water can be used without any particular limitation on the type of water such as hard water and soft water.

油、水および本発明の添加剤それぞれの配合割合については、それぞれ体積比で、油:水:添加剤=50〜60:20〜30:15〜25の割合で混合する。  About each compounding ratio of oil, water, and the additive of this invention, it mixes by the ratio of oil: water: additive = 50-60: 20-30: 30-15-25, respectively by volume ratio.

水混入の際には、なるべくゆっくりと定量を混入することが好ましい。  When mixing with water, it is preferable to mix a fixed amount as slowly as possible.

本発明の添加剤によって製造された各種超分子化燃料の実験結果について以下に説明する。  The experimental results of various supramolecular fuels produced with the additive of the present invention will be described below.

表1はA重油を用いた従来燃料と本発明の超分子化燃料との燃焼結果後の比較を示す。本発明による超分子化燃料は従来燃料に比して燃焼効率が高く、環境負荷物質排出量が少量で、また、価格/体積が安価で極めて優れた効果を示す。  Table 1 shows a comparison after combustion results between the conventional fuel using A heavy oil and the supramolecular fuel of the present invention. The supramolecular fuel according to the present invention has a combustion efficiency higher than that of the conventional fuel, a small amount of environmental load substance emission, a low price / volume and an extremely excellent effect.

Figure 2012241185
Figure 2012241185

次にボイラー燃焼試験の例を表2に示す。

Figure 2012241185
Next, Table 2 shows an example of a boiler combustion test.
Figure 2012241185

上記試験はボイラー会社での燃焼試験の例であり、使用燃料はA重油と超分子化燃料(A重油55%、添加剤20%、水25%)の2種類である。  The above test is an example of a combustion test at a boiler company, and there are two types of fuel used: A heavy oil and supramolecularized fuel (55% A heavy oil, 20% additive, 25% water).

燃焼温度は、バージンA重油の926℃に対して、超分子化燃料は982℃と約6%上昇している。燃料55%、水が25%も含まれているにも関わらず上記の結果を得られたのは燃焼効率ならびに熱効率向上を意味する。  Combustion temperature is about 6% for supermolecular fuel, 982 ° C, compared to 926 ° C for virgin A heavy oil. The fact that the above results were obtained despite the inclusion of 55% fuel and 25% water means improved combustion efficiency and thermal efficiency.

A重油に比べ超分子化燃料は、燃焼温度、カロリーが上昇するにもかかわらず、環境負荷物質排出量が軽減されることがわかる。  It can be seen that supramolecular fuel compared to heavy fuel oil A reduces the discharge of environmentally hazardous substances despite an increase in combustion temperature and calories.

燃焼実験の結果は次のようにまとめることができる。
ボイラーでの燃焼は燃料液滴の燃焼であり、燃料液滴の表面に物理的現象により気化した燃料と空気中の酸素が混合気を形成していろいろな空気過剰率で燃焼する。
このとき、液滴中に含まれている水粒子もこの燃焼により輻射熱を受けて加熱されて沸点に達し、次々とミクロ爆発し、周囲の油滴を飛散させることにより二次微粒化が起きる。
この様に油が瞬時に超微粒化することにより空気との接触面積が増大し、急速に完全燃焼を行い、燃焼排ガス中の煙や未燃炭素の発生を抑える。
また、この接触面積の増大は、燃焼に必要な過剰空気を低く抑えることができるため省エネルギー効果が大きくなる。
The results of the combustion experiment can be summarized as follows.
Combustion in a boiler is combustion of fuel droplets, and fuel vaporized by a physical phenomenon on the surface of the fuel droplets and oxygen in the air form an air-fuel mixture that burns at various excess air ratios.
At this time, the water particles contained in the droplets are also heated by receiving the radiant heat due to this combustion, reach the boiling point, undergo micro explosions one after another, and secondary atomization occurs by scattering the surrounding oil droplets.
In this way, when the oil is instantly atomized, the contact area with the air is increased, complete combustion is rapidly performed, and generation of smoke and unburned carbon in the combustion exhaust gas is suppressed.
In addition, the increase in the contact area increases the energy saving effect because the excess air required for combustion can be kept low.

この条件を満たすためには、水粒子のミクロ化が最も大事なことであるが、通常、水粒子は表面張力が大きいため水粒子をミクロ化することが困難である。  In order to satisfy this condition, micronization of water particles is the most important. However, since water particles usually have a large surface tension, it is difficult to micronize water particles.

表3はエマルジョン燃料と本発明の超分子化燃料との比較を示す。  Table 3 shows a comparison between the emulsion fuel and the supramolecularized fuel of the present invention.

Figure 2012241185
Figure 2012241185

本発明による超分子化燃料は、従来エマルジョン燃料と比しても燃焼温度・燃焼効率・カロリーが高く燃費が低下しない。また、燃料と水が乳化及び分離することがなく備蓄・輸送をすることが可能であり、腐食等燃焼機関への影響もほとんどない。  The supramolecular fuel according to the present invention has a high combustion temperature, combustion efficiency, and calories even when compared with conventional emulsion fuel, and does not lower fuel efficiency. Further, fuel and water can be stored and transported without being emulsified and separated, and there is almost no influence on the combustion engine such as corrosion.

超分子化燃料製造用添加剤は、オレイン酸を主成分とした添加剤のため水粒子を極限まで極小化(ナノサイズ)することが可能である。また、同時に単なる油・水の混合ではなく、水が油に溶ける状態となっているため長期備蓄が可能となった。  Since the additive for producing supramolecular fuel is an additive mainly composed of oleic acid, water particles can be minimized (nano-sized) to the limit. At the same time, it is not simply a mixture of oil and water, but water is dissolved in oil, so long-term stockpiling is possible.

以上本発明について説明したが、本発明は上記実施形態に限定されるものでない。上記実施形態は例示であり、本発明の特許請求の範囲に記載された技術的思想と実質的に同一な構成を有し、同様な作用効果を奏するものは、いかなるものであっても本発明の技術範囲に包含される。  Although the present invention has been described above, the present invention is not limited to the above embodiment. The above-described embodiment is an exemplification, and the present invention has any configuration that has substantially the same configuration as the technical idea described in the claims of the present invention and that exhibits the same effects. It is included in the technical scope.

Claims (4)

化石燃料と水とを混合するための、重量比でオレイン酸68.6%〜75.2%、メタノール12.3%〜14.1%、リノール酸3.0%〜3.8%、プロピレングリコール6.8%〜8.6%及びアンモニア4.0%〜5.5%を含み、順次混入攪拌することを特徴とする超分子化燃料製造用添加剤。  Oleic acid 68.6% to 75.2%, methanol 12.3% to 14.1%, linoleic acid 3.0% to 3.8%, propylene by weight for mixing fossil fuel and water An additive for producing a supramolecular fuel, which contains 6.8% to 8.6% glycol and 4.0% to 5.5% ammonia and is mixed and stirred in sequence. 攪拌機に入れて循環攪拌混合する工程からなることを特徴とする請求項1の超分子化燃料製造用添加剤の製造方法。  2. The method for producing an additive for producing a supramolecular fuel according to claim 1, comprising a step of circulating stirring and mixing in an agitator. 化石燃料50%〜60%と請求項1の添加剤を15%〜25%と、水20%〜30%を攪拌混合することを特徴とする超分子化燃料の製造方法。  A method for producing a supramolecular fuel comprising mixing 50% to 60% of fossil fuel, 15% to 25% of the additive of claim 1 and 20% to 30% of water. 化石燃料にはA重油(ローサルA重油含む)、灯油、軽油等を含み、請求項3記載の超分子化燃料の製造方法。  The method for producing a supramolecular fuel according to claim 3, wherein the fossil fuel includes A heavy oil (including Rosal A heavy oil), kerosene, light oil and the like.
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