JPH11140470A - Water-fossil fuel mixed emulsion - Google Patents
Water-fossil fuel mixed emulsionInfo
- Publication number
- JPH11140470A JPH11140470A JP30895897A JP30895897A JPH11140470A JP H11140470 A JPH11140470 A JP H11140470A JP 30895897 A JP30895897 A JP 30895897A JP 30895897 A JP30895897 A JP 30895897A JP H11140470 A JPH11140470 A JP H11140470A
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- JP
- Japan
- Prior art keywords
- water
- fossil fuel
- fuel
- emulsion
- fossil
- 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.)
- Pending
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Abstract
Description
【０００１】[0001]
【発明の属する技術分野】本発明は、水と石油等の化石
液体燃料とを混合してなる新規な燃料である、水−化石
燃料混合エマルジョンに関する。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a water-fossil fuel mixed emulsion, which is a novel fuel obtained by mixing water and a fossil liquid fuel such as petroleum.
【０００２】[0002]
【従来の技術】従来、省エネ等の観点から、化石液体燃
料に水を混合して燃料エマルジョンとして燃焼すること
が種々提案されている。しかし、このような燃料エマル
ジョンは水と石油系成分との割合が５５：４５位で試み
られており、燃料として石油系成分をこれ以上減少でき
ない。また、エマルジョンの安定性の上からも、石油系
成分を比較的多量に必要とし、省資源の点でまだ満足で
きるものでなく、水成分の燃料化という点で十分ではな
かった。さらに、このような従来の化石液体燃料と水を
混合してなる混合燃料においても、化石液体燃料成分が
多いと燃焼排ガスとしてＣＯ2 （炭酸ガス）を多量に含
むガスを排出する。しかし、近年、地球規模でＣＯ2 の
排出削減が求められている状況に照らすと、このような
燃料でも必ずしも満足しうるものではない。したがって
一定の燃焼カロリーをできるだけ少ないＣＯ2 排出で得
られる燃料の開発が切望されている。2. Description of the Related Art Conventionally, from the viewpoint of energy saving, various proposals have been made to mix fossil liquid fuel with water and burn it as a fuel emulsion. However, such fuel emulsions have been tried with a ratio of water to petroleum-based components of about 55:45, and the petroleum-based components cannot be further reduced as fuel. Further, from the viewpoint of the stability of the emulsion, a relatively large amount of petroleum-based components is required, which is not yet satisfactory in terms of resource saving, and is not sufficient in terms of converting water components into fuel. Furthermore, even in such a conventional mixed fuel obtained by mixing a fossil liquid fuel and water, if the fossil liquid fuel component is large, a gas containing a large amount of CO 2 (carbon dioxide) is discharged as combustion exhaust gas. However, in light of the recent demand for reduction of CO 2 emission on a global scale, such a fuel is not always satisfactory. Therefore, development of a fuel that can obtain a constant calorie of combustion with as little CO 2 emission as possible has been desired.
【０００３】[0003]
【発明が解決しようとする課題】本発明は、石油等の化
石液体成分を減少させた、水を高加水率で含有させて燃
料化できる水−化石燃料混合エマルジョンを提供するこ
とを目的とする。また、本発明は、水と化石液体成分と
をエマルジョン混合させた燃料であって、化石液体成分
の割合を低減し、高加水率での燃焼が可能であり、化石
液体成分の低減により、燃焼排出ガス中のＣＯ2 量を低
減できる水−化石燃料混合エマルジョンを提供すること
を目的とする。SUMMARY OF THE INVENTION An object of the present invention is to provide a water-fossil fuel mixed emulsion in which the fossil liquid component such as petroleum is reduced and which can be made into fuel by containing water at a high water content. . Further, the present invention is a fuel in which water and a fossil liquid component are mixed in an emulsion, and the ratio of the fossil liquid component is reduced, and combustion at a high water content is possible. An object of the present invention is to provide a water-fossil fuel mixed emulsion capable of reducing the amount of CO 2 in exhaust gas.
【０００４】[0004]
【課題を解決するための手段】本発明者は、上記課題を
解決するため鋭意研究を重ねた結果、石油等の化石液体
成分に混合する水成分として、微粒状の電気石を分散さ
せて、界面張力を低下させた処理水を用いることによ
り、上記の目的を達成しうることを見い出し、この知見
に基づき、さらに検討を重ね本発明をなすに至った。し
たがって本発明は、（１）水と化石燃料液体とをエマル
ジョン混合してなる燃料であって、混合する水に少なく
とも３重量％の微粒状電気石を分散させて処理し、この
処理水を前記化石液体燃料とエマルジョン混合してなる
ことを特徴とする水−化石燃料混合エマルジョン、及び
（２）水と化石燃料液体との混合比が、容量比で９．
５：０．５〜７．０：３．０の範囲であることを特徴と
する（１）項記載の水−化石燃料混合エマルジョンを提
供するものである。Means for Solving the Problems As a result of intensive studies to solve the above-mentioned problems, the present inventor disperses fine-grained tourmaline as a water component to be mixed with a fossil liquid component such as petroleum, It has been found that the above object can be achieved by using the treated water with reduced interfacial tension, and based on this finding, the present inventors have further studied and came to the present invention. Therefore, the present invention provides (1) a fuel obtained by emulsion-mixing water and a fossil fuel liquid, wherein at least 3% by weight of fine-grained tourmaline is dispersed and treated in the water to be mixed, and the treated water is treated with the above-mentioned water. 8. A water-fossil fuel mixed emulsion, which is obtained by mixing an emulsion with a fossil liquid fuel, and (2) the mixing ratio of water to the fossil fuel liquid is 9.
It is intended to provide the water-fossil fuel mixed emulsion according to the above (1), wherein the ratio is in the range of 5: 0.5 to 7.0: 3.0.
【０００５】[0005]
【発明の実施の形態】本発明において化石燃料液体と混
合する水には、微粒状電気石を少なくとも３重量％添加
して処理する。水に対する電気石の添加量は、好ましく
は３〜１０重量％である。この電気石の量が少なすぎる
とその効果が不十分であり、多すぎると製造のスピード
が遅くなる。電気石としては、好ましくはトルマリンが
用いられ、それは微粒子であることが必要であり、粒径
は具体的には０．５〜２．５μｍが好ましく、０．８〜
１．０μｍがより好ましい。電気石はこのように微粒状
であることが必要であり、粒子が小さすぎると製造コス
トが極端に高くなり、大きすぎると目的の効果が得られ
ない。この電気石での処理温度は特に制限はないが、好
ましくは常温で行われ、時間はｐＨが下記のような値に
上昇するまでに行う。この電気石で処理することによ
り、水は通常、ｐＨが８．０〜１１．５に上昇する。こ
れは、水が電気石と反応して生成したヒドロニウムイオ
ンがＨ2 となり、水はＯＨ- の豊富なヒドロキシルイオ
ン水を形成していることによるものと思われる。また、
同時に水の表面張力が低下する。この電気石による処理
は、処理水の性質上、ガラス又はステンレス製の容器で
行うのが好ましい。DETAILED DESCRIPTION OF THE INVENTION In the present invention, water mixed with a fossil fuel liquid is treated by adding at least 3% by weight of finely divided tourmaline. The addition amount of tourmaline to water is preferably 3 to 10% by weight. If the amount of this tourmaline is too small, its effect is insufficient, and if it is too large, the production speed is reduced. As tourmaline, tourmaline is preferably used, and it is necessary that the tourmaline be fine particles. The particle size is specifically preferably 0.5 to 2.5 μm, and 0.8 to 2.5 μm.
1.0 μm is more preferred. Tourmaline must be fine in this way. If the particles are too small, the production cost becomes extremely high. If the particles are too large, the intended effect cannot be obtained. The treatment temperature with this tourmaline is not particularly limited, but is preferably carried out at room temperature, and the treatment is carried out until the pH rises to the following value. Treatment with this tourmaline usually raises the pH of the water to 8.0-11.5. This is probably due to the fact that hydronium ions generated by the reaction of water with tourmaline become H 2 , and the water forms hydroxyl-rich water that is rich in OH − . Also,
At the same time, the surface tension of water decreases. This treatment with tourmaline is preferably performed in a glass or stainless steel container due to the nature of the treated water.
【０００６】本発明で用いる水としては、水道水（不純
物は除去）、蒸留水を用いることができる。本発明の水
−化石燃料混合エマルジョンにおいて、化石燃料液体と
しては、灯油、軽油、Ａ重油、Ｂ重油、Ｃ重油などがあ
げられる。この化石燃料液体には、予め界面活性剤を微
量添加しておくのが好ましい。界面活性剤としては、陰
イオン性界面活性剤があり、例えばアルキルベンゼンス
ルホン酸塩があげられるが、これに制限されるものでは
ない。その添加量は、表面張力を低下させるのに十分な
量であればよく、具体的には化石燃料液体に対し、１〜
３重量％以下である。As the water used in the present invention, tap water (to remove impurities) and distilled water can be used. In the water-fossil fuel mixed emulsion of the present invention, examples of the fossil fuel liquid include kerosene, light oil, fuel oil A, fuel oil B, fuel oil C, and the like. It is preferable to add a trace amount of a surfactant to this fossil fuel liquid in advance. Surfactants include anionic surfactants, such as, but not limited to, alkyl benzene sulfonates. The addition amount may be an amount sufficient to reduce the surface tension, and specifically, 1 to 1 with respect to the fossil fuel liquid.
Not more than 3% by weight.
【０００７】本発明の水−化石燃料混合エマルジョンに
おいて、水を最大９５容量％まで含有させることができ
る。水と化石燃料液体との混合割合は、上記の範囲であ
れば特に制限はないが容量比で好ましくは９．５：０．
５〜７．０：３．０である。この場合、上記範囲を越え
て化石燃料液体の割合が大きすぎるとこの水の効果によ
るエマルジョン化が劣化する。また少なすぎると燃焼し
なくなる。本発明では、化石燃料液体の割合を従来の燃
料エマルジョンに比べ少なく、かつ、水の割合を大きく
でき、水の燃料化を図ること、及び化石燃料液体の低減
によりＣＯ2 の発生を低減できることを１つの大きな特
徴としている。[0007] The water-fossil fuel mixed emulsion of the present invention can contain up to 95% by volume of water. The mixing ratio of the water and the fossil fuel liquid is not particularly limited as long as it is in the above range, but the mixing ratio is preferably 9.5: 0.
5-7.0: 3.0. In this case, if the ratio of the fossil fuel liquid is too large beyond the above range, the emulsification due to the effect of the water is deteriorated. If it is too small, it will not burn. In the present invention, the ratio of the fossil fuel liquid is smaller than that of the conventional fuel emulsion, the ratio of water can be increased, the fuel can be converted to water, and the generation of CO 2 can be reduced by reducing the fossil fuel liquid. One major feature.
【０００８】本発明の水−化石燃料混合エマルジョンか
らなる燃料の燃焼方法は特に制限はないが、自己完結性
のガスであるブラウンズガスの高温炎によって、炉内に
水分解の反応場を設け、混合ガスを燃焼させる方法が好
ましい。[0008] The method of burning the fuel comprising the water-fossil fuel mixed emulsion of the present invention is not particularly limited, but a reaction field for water decomposition is provided in the furnace by a high-temperature flame of Brown's gas which is a self-contained gas. A method of burning the mixed gas is preferable.
【０００９】これを実施する燃焼装置を図２に従って説
明する。図中１は水−化石燃料混合エマルジョンの貯蔵
タンク、２は供給ポンプ、３はマイクロ波（極超短波）
照射装置、４はブラウンズガス発生装置、５はブラウン
ズガスの燃焼バーナ、７はバーナ、８は燃焼室、９は水
−化石燃料混合エマルジョンの気化室、１０はノズル、
１１は耐熱被覆材である。なお、ブラウンズガスは水の
電気分解により得られる非爆発性の水素／酸素ガス混合
体であって、その燃焼温度は理論値として３，４５０℃
となる公知のガスであり、１９７０年初頭にブルガリア
生れのユール・ブラウン教授によって発明されたもので
ある。ブラウンズガスの特徴は、水素の体積２に対して
酸素の体積１という割合が厳格に維持されれば安全に混
合（燃焼）できる点にあり、貯蔵しておくことも可能で
ある。まず、水−化石燃料混合エマルジョンは、貯蔵タ
ンク１から供給ポンプ２により開閉バルブＶ1 を経由し
てマイクロ波（極超短波）照射装置３へ導入され、照射
装置３内でマイクロ波（２４５０メガヘルツ）が照射さ
れて４００〜６００℃に昇温される。次いで、この昇温
された水−化石燃料混合ガスは、気化室９に導入され、
ノズル１０から噴出されて気化される。なお、該気化室
９は気液分離室を兼ねており、そして該室内に溜まった
液状物はバルブＶ5 を開くことにより排出することがで
きる。その後、この昇温され気化された水−化石燃料混
合エマルジョンは、バルブＶ2 を介して燃焼室８のバー
ナ７へ供給される。この高温の混合ガスの移送において
は、配管を耐熱被覆材１１で被覆しておくことが好まし
い。A combustion apparatus for carrying out this will be described with reference to FIG. In the figure, 1 is a storage tank of a water-fossil fuel mixed emulsion, 2 is a supply pump, and 3 is a microwave (ultra-high frequency).
Irradiation device, 4 is Brown's gas generator, 5 is Brown's gas combustion burner, 7 is burner, 8 is combustion chamber, 9 is water-fossil fuel mixed emulsion vaporization chamber, 10 is nozzle,
11 is a heat-resistant covering material. Browns gas is a non-explosive hydrogen / oxygen gas mixture obtained by electrolysis of water, and its combustion temperature is 3,450 ° C. as a theoretical value.
And was invented in early 1970 by Prof. Yule Brown, born in Bulgaria. Brown's gas is characterized in that it can be safely mixed (combusted) if the ratio of 1 volume of oxygen to 2 volume of hydrogen is strictly maintained, and can be stored. First, a water-fossil fuel mixed emulsion is introduced from a storage tank 1 to a microwave (ultra-high frequency) irradiation device 3 by a supply pump 2 via an opening / closing valve V 1 , and the microwave (2450 MHz) is irradiated in the irradiation device 3. And the temperature is raised to 400 to 600 ° C. Next, this heated water-fossil fuel mixed gas is introduced into the vaporization chamber 9,
It is ejected from the nozzle 10 and vaporized. Incidentally, vaporization chamber 9 also serves as a gas-liquid separation chamber, and accumulated liquid product in the chamber can be discharged by opening the valve V 5. Thereafter, the temperature is increased vaporized water - fossil fuel mixed emulsion is supplied to the burner 7 of the combustion chamber 8 via a valve V 2. In transferring the high-temperature mixed gas, it is preferable that the pipe is covered with the heat-resistant coating material 11.
【００１０】他方、水を電気分解して得られる水素２容
量と酸素１容量の混合比からなるブラウンズガスを発生
させるブラウンズガス発生装置４からブラウンズガスを
発生させ、このガスをバルブＶ3 を介して燃焼させて１
５００〜２５００℃に高温化する。ブラウンズガス燃焼
室６内には、外部から空気、酸素又はオゾンのうちの１
種以上をバルブＶ4 を介して添加することができ、それ
らの種類及び供給量を調整して供給することによって、
燃焼室８のバーナ７へ供給する高温化されたブラウンズ
ガス燃焼気体の組成を調整（例えば、酸素過剰のもの
に、あるいは窒素含有のものに）することができる。On the other hand, browns gas is generated from a browns gas generator 4 for generating browns gas having a mixing ratio of 2 volumes of hydrogen and 1 volume of oxygen obtained by electrolysis of water, and this gas is supplied via a valve V 3 . And burn 1
The temperature is raised to 500-2500C. Inside the Browns gas combustion chamber 6, one of air, oxygen or ozone is externally supplied.
Can be added or species through the valve V 4, by feeding by adjusting their types and supply,
The composition of the high-temperature browns gas combustion gas supplied to the burner 7 of the combustion chamber 8 can be adjusted (for example, to an oxygen-excessive one or a nitrogen-containing one).
【００１１】こうして得られた高温化されたブラウンズ
ガス燃焼気体を、前記燃焼室８のバーナ７にその外周を
囲む二重管構造の空隙部に供給することが好ましい。そ
の結果、該バーナ７は、外周から内部まで加熱され、か
つその先端からブラウンズガス燃焼気体がそれを包むよ
うにして燃焼室８内に放出される。燃焼室８内において
は、こうして外周より内部まで加熱されたバーナ７口か
ら、昇温され気化された水−化石燃料混合ガスが放出さ
れ燃焼される。It is preferable that the thus-heated Brown's gas combustion gas thus obtained is supplied to the burner 7 of the combustion chamber 8 into a double-pipe structure surrounding the outer periphery thereof. As a result, the burner 7 is heated from the outer periphery to the inside, and the Brown's gas combustion gas is discharged from the tip into the combustion chamber 8 so as to envelop it. In the combustion chamber 8, the water-fossil fuel mixed gas that has been heated and vaporized is released from the burner 7 heated from the outer periphery to the inside, and burned.
【００１２】[0012]
【実施例】次に、本発明を実施例に基づきさらに詳細に
説明する。 実施例１ 図１に示す工程により水−化石燃料混合エマルジョンを
製造した。油タンク１０１に灯油０．５リットルを満た
した後、陰イオン界面活性剤スルホール＃４００（商品
名、村松石油研究所社製）を灯油に対し１重量％添加し
て、よく攪拌した。一方、ガラス製の水タンク１０２
に、水道水９．５リットルを満たした後、粒子サイズ１
μｍのトルマリン粉を水に５重量％散布した。次に、こ
の水タンク１０２を攪拌装置で３０分間よく攪拌した。
ｐＨをチェックした後に攪拌を停止し、トルマリン粉の
沈降を待ち、２時間位でトルマリン粉が完全に沈降させ
た。上澄液はヒドロキシルイオン水である。別に設けた
混合タンク１０３に、制御弁を調整して、油タンク１０
１及び水タンク１０２から灯油１０％量、水９０％量を
送液し、満たして、３０分間よく攪拌して、本発明の水
−化石燃料混合エマルジョンを製造した。Next, the present invention will be described in more detail with reference to examples. Example 1 A water-fossil fuel mixed emulsion was produced by the process shown in FIG. After filling the oil tank 101 with 0.5 liter of kerosene, 1% by weight of anionic surfactant Sulfol # 400 (trade name, manufactured by Muramatsu Petroleum Institute Co., Ltd.) was added to the kerosene and stirred well. On the other hand, a glass water tank 102
After filling with 9.5 liters of tap water, particle size 1
5 μm tourmaline powder was sprayed on water at 5% by weight. Next, the water tank 102 was well stirred with a stirring device for 30 minutes.
After checking the pH, the stirring was stopped, and the sedimentation of the tourmaline powder was awaited, and the tourmaline powder was completely settled in about two hours. The supernatant is hydroxyl ion water. The control valve is adjusted to the separately provided mixing tank 103 so that the oil tank 10
1 and 90% of kerosene were fed and filled from the water tank 102 and thoroughly stirred for 30 minutes to produce a water-fossil fuel mixed emulsion of the present invention.
【００１３】実施例２、３及び比較例１、２ 水及びトルマリンの添加条件を下記表１のようにした以
外は実施例１と同様にして、水−化石燃料混合エマルジ
ョンを製造した。なお水道精製水は不純物を浄化した水
道水（中性凝縮剤０．１重量％を添加して残留塩素、ト
リハロメタンなどを除去したもの）である。この時調製
された処理水のｐＨを表１に示した。Examples 2 and 3 and Comparative Examples 1 and 2 A water-fossil fuel mixed emulsion was produced in the same manner as in Example 1 except that the conditions for adding water and tourmaline were as shown in Table 1 below. The purified tap water is tap water in which impurities have been purified (residual chlorine, trihalomethane and the like are removed by adding 0.1% by weight of a neutral condensing agent). The pH of the treated water prepared at this time is shown in Table 1.
【００１４】[0014]
【表１】 [Table 1]
【００１５】試験例 上記実施例及び比較例で製造した水−化石燃料混合エマ
ルジョンを図２に示す装置を用いて下記条件で燃焼させ
た。その結果を実験Ｎｏ．１〜５として表２に示した。 燃焼条件 １）バーナ７の水−化石燃料混合エマルジョンの線速
度：２ｍ／秒、噴出量：５０ｃｃ／分 ２）バーナ５のブランズガスの線速度２．７ｍ／秒、噴
出量６００ｌ／ｈ ３）バーナ７とバーナー５の交叉角：１５° ４）バーナ７より噴出されるガス温度１１０℃以上（初
速） なお、上記の灯油と水との比を、容量比で１：９から
３：７に変更した以外は各実施例及び各比較例と同様に
して水−化石燃料混合エマルジョンを製造し、これらに
ついても燃焼試験を行った。これを実験Ｎｏ．６〜１０
として表２に示した。Test Example The water-fossil fuel mixed emulsions produced in the above Examples and Comparative Examples were burned under the following conditions using the apparatus shown in FIG. The results are shown in Experiment Nos. The results are shown in Table 2 as 1 to 5. Combustion conditions 1) The linear velocity of the water-fossil fuel mixed emulsion of the burner 7: 2 m / sec, the ejection amount: 50 cc / min 2) The linear velocity of the brand gas of the burner 5: 2.7 m / sec, the ejection amount 600 l / h 3) Crossing angle between burner 7 and burner 5: 15 ° 4) Temperature of gas ejected from burner 7 is 110 ° C. or more (initial speed) The above ratio of kerosene to water is reduced from 1: 9 to 3: 7 by volume ratio. Water / fossil fuel mixed emulsions were produced in the same manner as in each of the examples and comparative examples except for the change, and combustion tests were also performed on these emulsions. This is referred to as Experiment No. 6-10
The results are shown in Table 2.
【００１６】[0016]
【表２】 [Table 2]
【００１７】[0017]
【発明の効果】本発明の水−化石燃料混合エマルジョン
は、水を高加水率で含有させて水を燃料化することがで
きる。また、化石燃料の消費量を低減でき、省資源の上
で優れるばかりでなく、化石燃料成分の割合を低減する
ことにより、燃焼による排出ＣＯ2 量を低減できるとい
う優れた作用効果を奏する。According to the water-fossil fuel mixed emulsion of the present invention, water can be converted into a fuel by adding water at a high water content. Further, not only is it possible to reduce the consumption of fossil fuel, which is excellent not only in resource saving, but also, by reducing the ratio of fossil fuel components, it is possible to reduce the amount of CO 2 emitted by combustion, thereby providing an excellent effect.
【図１】本発明の水−化石燃料混合エマルジョンの製造
工程図である。FIG. 1 is a production process diagram of a water-fossil fuel mixed emulsion of the present invention.
【図２】本発明の燃料の燃焼装置の構成の説明図であ
る。FIG. 2 is an explanatory diagram of a configuration of a fuel combustion device of the present invention.
１０１ 油タンク １０２ 水タンク １０３ 混合タンク １ 水−化石燃料混合エマルジョンの貯蔵タンク ２ 水−化石燃料混合エマルジョン供給ポンプ ３ マイクロ波（極超短波）照射装置 ４ ブラウンズガス発生装置 ５ バーナ ７ バーナ ８ 燃焼室 ９ 水−化石燃料エマルジョン気化室 １０ ノズル １１ 耐熱被覆材 Ｖ1 〜Ｖ5 バルブDESCRIPTION OF SYMBOLS 101 Oil tank 102 Water tank 103 Mixing tank 1 Storage tank of water-fossil fuel mixed emulsion 2 Water-fossil fuel mixed emulsion supply pump 3 Microwave (ultra-high frequency) irradiation device 4 Brown's gas generator 5 Burner 7 Burner 8 Combustion chamber 9 water - fossil fuel emulsion vaporization chamber 10 nozzle 11 heat resistant material V 1 ~V 5 valve
───────────────────────────────────────────────────── フロントページの続き (72)発明者 森 正弘 神奈川県平塚市代官町10番14号 ネオシテ ィ湘南平塚201 株式会社全眞電力エンジ ニヤリング内 (72)発明者 佐藤 利安 神奈川県平塚市八重咲町26番19−302号 ブルーハイツ高風荘 ──────────────────────────────────────────────────続 き Continued on the front page (72) Inventor Masahiro Mori No. 10-14, Daikanmachi, Hiratsuka-shi, Kanagawa Prefecture Neocity Shonan Hiratsuka 201 Zenshin Electric Power Engineering Co., Ltd. 26th 19-302 Blue Heights Takafuso
Claims (2)
してなる燃料であって、混合する水に少なくとも３重量
％の微粒状電気石を分散させて処理し、この処理水を前
記化石液体燃料とエマルジョン混合してなることを特徴
とする水−化石燃料混合エマルジョン。1. A fuel obtained by emulsion-mixing water and a fossil fuel liquid, wherein at least 3% by weight of fine-grained tourmaline is dispersed in water to be mixed, and the treated water is treated with the fossil liquid fuel. A water-fossil fuel mixed emulsion characterized by being mixed with an emulsion.
で９．５：０．５〜７．０：３．０の範囲であることを
特徴とする請求項１記載の水−化石燃料混合エマルジョ
ン。2. The method according to claim 1, wherein the mixing ratio of the water and the fossil fuel liquid is in the range of 9.5: 0.5 to 7.0: 3.0 by volume. Fossil fuel mixed emulsion.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP30895897A JPH11140470A (en) | 1997-11-11 | 1997-11-11 | Water-fossil fuel mixed emulsion |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP30895897A JPH11140470A (en) | 1997-11-11 | 1997-11-11 | Water-fossil fuel mixed emulsion |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| JPH11140470A true JPH11140470A (en) | 1999-05-25 |
Family
ID=17987296
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP30895897A Pending JPH11140470A (en) | 1997-11-11 | 1997-11-11 | Water-fossil fuel mixed emulsion |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH11140470A (en) |
Cited By (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO2000029518A1 (en) * | 1998-11-17 | 2000-05-25 | Toshiyasu Satoh | Water/oil mixed fuel and process for producing the same |
| JP2003021312A (en) * | 2001-07-09 | 2003-01-24 | Get:Kk | Method of forming flame for heat source, and its device |
| WO2008139791A1 (en) * | 2007-05-15 | 2008-11-20 | Toshiharu Fukai | Oil emulsion |
| JP2008280489A (en) * | 2007-05-14 | 2008-11-20 | Santo Energy Kk | Oil water emulsion fuel and emulsifier used for its manufacturing |
| KR100937524B1 (en) | 2008-09-11 | 2010-01-19 | 주식회사 기성테크 | Eco-friendly emulsion fuel manufacture device |
| WO2010010635A1 (en) * | 2008-07-25 | 2010-01-28 | Kic株式会社 | Emulsion fuel production apparatus, process and emulsion fuel produced by the process |
| CN104232184A (en) * | 2008-04-19 | 2014-12-24 | 罗琮贵 | Tourmaline additive for saving energy and reducing emission |
-
1997
- 1997-11-11 JP JP30895897A patent/JPH11140470A/en active Pending
Cited By (9)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO2000029518A1 (en) * | 1998-11-17 | 2000-05-25 | Toshiyasu Satoh | Water/oil mixed fuel and process for producing the same |
| JP2003021312A (en) * | 2001-07-09 | 2003-01-24 | Get:Kk | Method of forming flame for heat source, and its device |
| JP2008280489A (en) * | 2007-05-14 | 2008-11-20 | Santo Energy Kk | Oil water emulsion fuel and emulsifier used for its manufacturing |
| WO2008139791A1 (en) * | 2007-05-15 | 2008-11-20 | Toshiharu Fukai | Oil emulsion |
| TWI471417B (en) * | 2007-05-15 | 2015-02-01 | ||
| CN104232184A (en) * | 2008-04-19 | 2014-12-24 | 罗琮贵 | Tourmaline additive for saving energy and reducing emission |
| WO2010010635A1 (en) * | 2008-07-25 | 2010-01-28 | Kic株式会社 | Emulsion fuel production apparatus, process and emulsion fuel produced by the process |
| JP5455908B2 (en) * | 2008-07-25 | 2014-03-26 | 新治 白太 | Emulsion fuel manufacturing apparatus and method, and emulsion fuel manufactured by the method |
| KR100937524B1 (en) | 2008-09-11 | 2010-01-19 | 주식회사 기성테크 | Eco-friendly emulsion fuel manufacture device |
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