JPH06179883A - Production of oxygen-rich fuel oil - Google Patents

Production of oxygen-rich fuel oil

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Publication number
JPH06179883A
JPH06179883A JP33404892A JP33404892A JPH06179883A JP H06179883 A JPH06179883 A JP H06179883A JP 33404892 A JP33404892 A JP 33404892A JP 33404892 A JP33404892 A JP 33404892A JP H06179883 A JPH06179883 A JP H06179883A
Authority
JP
Japan
Prior art keywords
oxygen
water
oil
heavy oil
mixed
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
Application number
JP33404892A
Other languages
Japanese (ja)
Inventor
Takeji Motai
武治 甕
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.)
Kankyo Kagaku KK
Original Assignee
Kankyo Kagaku KK
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
Application filed by Kankyo Kagaku KK filed Critical Kankyo Kagaku KK
Priority to JP33404892A priority Critical patent/JPH06179883A/en
Publication of JPH06179883A publication Critical patent/JPH06179883A/en
Pending legal-status Critical Current

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Abstract

PURPOSE:To obtain an oxygen-rich fuel oil which has a stable combusitibility, enables high-temp. combustion, and reduces pollution economically by dispersing an oily oxygen synthesis fluid into water and mixing the dispersion with a heavy oil. CONSTITUTION:Carbon, an oily compatibilizer, an oxygen compd., a dispersant, sodium, etc., are mixed to give an oily oxygen synthesis fluid, which is dispersed in water to give an oxygen synthesis fluid, which is further mixed with a heavy oil to give the oxygen-rich fuel oil. The obtd. oil, though obtd. from water and the heavy oil, can be completely burned at a high temp., achieving an economic saving 30-40% in comparison with combustion of the heavy oil alone. The complete combustion at high temp. reduces amts. of soot and dust, NOx, and SOx each by 30% or higher when compared with a usual fuel oil, greatly contributing not only to economy but also to the environment.

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、現在コストメリット燃
料として各国で大量に消費されている重油に対し、水を
混合して、水と油の混合油を経済的に燃焼させ、ばいじ
ん,NOx ,SOx 等の公害発生量を大幅に減少させる
ことに関するものである。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention mixes water with heavy oil, which is currently consumed in large quantities in each country as a cost-effective fuel, and burns the mixed oil of water and oil economically to reduce dust and NO. The present invention is concerned with significantly reducing the amount of pollution such as x and SO x .

【0002】[0002]

【従来の技術】油に水を混合燃焼する従来技術は数多く
研究されているが、代表的なものとしては、次のような
技術がある。代表的技術として界面活性剤を用いて水を
重油中に分散する方法がある。この方法は、時間の経過
とともに水と油とが分離し、重油そのものの燃焼よりス
ムーズな燃焼ができない欠点が生じている。このため、
試験的燃焼が中心で、長期間本格的な燃料油として採用
されずに来ている。
2. Description of the Related Art Many conventional techniques for mixing and burning water with oil have been studied, but the following techniques are typical. A typical technique is to disperse water in heavy oil using a surfactant. This method has a drawback that water and oil are separated with the lapse of time, and smooth combustion cannot be performed as compared with combustion of heavy oil itself. For this reason,
It is mainly used for trial combustion and has not been adopted as a full-scale fuel oil for a long time.

【0003】又、重油に水を強圧で噴射して混合燃焼す
る方法、油に水を混合し、超音波を作用させる方法など
がある。これらの方法も、水を少量にして重油と混合
し、油と分離しない短時間の燃焼に限定され、燃焼の経
済性よりも、ばいじん,NOx,SOx の発生量を少し
でも減少することを目的とした場合に使用されるに過ぎ
ない。しかも、燃焼を長時間継続した場合には、ボイラ
ーの内壁が錆びる傾向があり、これも問題となってい
る。
Further, there are a method of injecting water into heavy oil at a high pressure and mixing and burning, a method of mixing water with oil and applying ultrasonic waves. These methods are also limited to short-time combustion in which a small amount of water is mixed with heavy oil and the oil is not separated, and the amount of soot, NO x , SO x is reduced as much as possible, rather than the economical efficiency of combustion. It is only used for the purpose. Moreover, when the combustion is continued for a long time, the inner wall of the boiler tends to rust, which is also a problem.

【0004】更に、水に墨汁を混合し、この墨汁水を重
油にいれて燃焼する方法が提案されている。この場合、
油と水の分離はみられず、燃焼効率も重油単体を燃焼す
るよりも良い結果が得られると報告されているが、自動
燃焼装置の燃焼にあたって、安定燃焼が得られず、トラ
ブルを生じがちである。これは墨汁水が下部に沈降し
て、分散が不安定になるものと予想されている。
Further, a method has been proposed in which India ink is mixed with water, and the India ink water is added to heavy oil and burned. in this case,
It has been reported that oil and water are not separated, and the combustion efficiency is better than that of burning heavy oil alone.However, stable combustion is not obtained when the automatic combustion device burns, and troubles tend to occur. Is. It is expected that the ink water will settle to the bottom and the dispersion will become unstable.

【0005】[0005]

【発明が解決しようとする課題】このような状況におい
て、限りある油性燃料の効率的燃焼を図り、かつ、年々
増加しているばいじん,窒素酸化物(NOx ),硫黄酸
化物(SOx )の発生量を減少させ、環境にやさしい燃
料とすることが望まれている。本発明は、カーボンを核
とし、これにケロシン,過酸化水素,分散剤,ナトリウ
ム等を混合し、油性酸素合成液を加工し、これを水に分
散混合させ、その分散混合水を重油に入れて混合燃焼す
ることにより、安定燃焼性を確保でき、更に又、重油単
体では望めない高温燃焼を可能とし、大幅な経済的メリ
ットを上げ並びに公害発生を著しく軽減可能とすること
を目的とするものである。
Under such circumstances, it is attempted to efficiently burn a limited oil fuel, and the amount of dust, nitrogen oxides (NO x ), sulfur oxides (SO x ) is increasing year by year. It is desired to reduce the generation amount of methane and use it as an environmentally friendly fuel. In the present invention, carbon is used as a core, and kerosene, hydrogen peroxide, a dispersant, sodium and the like are mixed with this to process an oil-based oxygen synthesis solution, which is dispersed and mixed in water, and the dispersed mixed water is put into heavy oil. By mixing and burning in a stable manner, stable combustion can be secured, and further, high temperature combustion that can not be expected with heavy oil alone can be achieved, and it is intended to raise significant economic merit and significantly reduce pollution generation. Is.

【0006】[0006]

【課題を解決するための手段】重油の燃焼公害は重油の
不完全燃焼要素によって生ずるものとおもわれるが、本
願発明は、重油の完全燃焼の手段として、カーボン,油
性親和材,酸素化合剤,分散剤,ナトリウム等を混合
し、油性酸素合成液に加工し、これを水中に分散混合し
て酸素合成液と水の混合水となし、更にこの混合水を重
油と混合したものである。
It is considered that the combustion pollution of heavy oil is caused by an incomplete combustion element of heavy oil. However, the present invention uses carbon, an oily affinity material, an oxygen compound, as a means for complete combustion of heavy oil. A dispersant, sodium and the like are mixed and processed into an oily oxygen synthesis liquid, which is dispersed and mixed in water to form a mixed water of oxygen synthesis liquid and water, and this mixed water is mixed with heavy oil.

【0007】[0007]

【作用】本願発明の酸素リッチ燃料油の製造法によれ
ば、 (1)酸素化合剤として過酸化水素を使用し、これを重
油に対し、均一、かつ、長期安定状に混合することによ
り、重油の容易な燃焼性と高温による完全燃焼を実現
し、燃焼効率を大幅にアップさせた。過酸化水素は液体
であり、加熱気化により1650倍に膨張し、微小なガ
ス状となって重油と融合飛散し、高温で完全燃焼した。
この混合過酸化水素の量がわずかであっても、分散剤の
働きにより燃焼重油の全ての部分に浸透融合し、大量の
混合水の同時膨張爆発飛散する水性ガスとともに、高温
完全燃焼効果を極限にまで高めた。
According to the method for producing an oxygen-rich fuel oil of the present invention, (1) hydrogen peroxide is used as an oxygen compound, and this is mixed with heavy oil in a uniform and long-term stable state, Achieves easy combustion of heavy oil and complete combustion at high temperature, greatly improving combustion efficiency. Hydrogen peroxide was a liquid, expanded 1650 times by heating and vaporizing, became a minute gas, was fused and scattered with heavy oil, and was completely burned at a high temperature.
Even if the amount of this mixed hydrogen peroxide is small, it will permeate and fuse to all parts of the burning heavy oil by the action of the dispersant, and the simultaneous expansion and explosion of a large amount of mixed water will cause the high temperature complete combustion effect to the limit together with the scattered water gas. Raised to.

【0008】(2)重油に過酸化水素を均一、かつ、長
期安定状態に融合させ、完全燃焼を図る手段として、カ
ーボンを核として、これにケロシンを混合し、更に酸素
リッチの根幹をなす過酸化水素を混合する。過酸化水素
は、ケロシン,水,重油の全てに親和性が強く、安定で
あり、かつ、加熱気化により1650倍もの膨張性を発
揮するため、その量は少量でも高温完全燃焼の推進先導
を図るのに有効な働きをする。
(2) As a means for fusing heavy oil with hydrogen peroxide uniformly and in a stable state for a long period of time to achieve complete combustion, carbon is used as a nucleus, and kerosene is mixed therewith, and the excess of oxygen is the basis. Mix hydrogen oxide. Hydrogen peroxide has a strong affinity for kerosene, water, and heavy oil, is stable, and expands 1650 times by heating and vaporizing, so even if the amount is small, it will promote the promotion of high temperature complete combustion. It works effectively.

【0009】(3)ケロシンは、カーボン,過酸化水
素,重油との親和性が強く、又、重油に比較して低温度
で着火し、重油の燃焼性を高める助燃剤としての役割り
を確実に有効に発揮する。
(3) Kerosene has a strong affinity with carbon, hydrogen peroxide, and heavy oil, and also ignites at a lower temperature than heavy oil, and thus plays a role as a combustion improver for enhancing the flammability of heavy oil. Exerts effectively.

【0010】(4)分散剤は、微細なカーボン粒子,ケ
ロシン,過酸化水素等の合成液を水中に均一に急速に分
散誘導する役割と、合成液と混合した水成分を重油中へ
帯同分散する役割りを果たし、従来、重油と界面活性剤
水を混合した場合、発生しがちであった水と油の分離が
なく、均一に安定して混合状態を長期間保持する。合成
液と混合した水成分と重油との混合油をポリ容器に入
れ、倉庫内へ保管し、一つは静置し、もう一つは大きな
振動を一定期間毎に与えることを繰り返し、1ヶ月後,
12ヶ月後,18ヶ月後の3回にわたり目視ならびに顕
微鏡によるチェックを実施したが、油と水の分離は全く
見られず、分散状態に変化がなかった。
(4) The dispersant serves to rapidly and uniformly disperse fine carbon particles, kerosene, hydrogen peroxide and other synthetic liquids in water, and also disperse the water component mixed with the synthetic liquids into heavy oil. When the heavy oil and the surfactant water are conventionally mixed, there is no separation of water and oil, which tends to occur, and the mixed state is maintained uniformly and stably for a long time. Put mixed oil of water component mixed with synthetic liquid and heavy oil in a plastic container and store it in a warehouse. One is left standing and the other is repeatedly given a large vibration every certain period. rear,
After 12 months and 18 months, a visual check and a microscope check were carried out three times, but no separation of oil and water was observed, and the dispersion state was unchanged.

【0011】(5)水酸化ナトリウムは、重油の完全燃
焼の強力な助燃剤として加熱により細かな瞬間爆発を行
い、ケロシン,過酸化水素,水の完全燃焼促進効果と相
俟って重油の爆発飛散による完全燃焼をより確実に促進
させる。
(5) Sodium hydroxide is a strong combustion aid for complete combustion of heavy oil, which causes a fine instantaneous explosion by heating, and combined with the effect of promoting complete combustion of kerosene, hydrogen peroxide, and water, the explosion of heavy oil. It promotes complete combustion by scattering more reliably.

【0012】(6)重油にほぼ等量を混合する水は経済
性,完全燃焼,公害発生防止を実現させる主役であり、
主役の仕事を完全に成し遂げる仕組みの第一は、カーボ
ン,ケロシン,過酸化水素,分散剤,水酸化ナトリウム
等の合成液との混合である。混合に使用する水は、真水
を使用し、温度は20℃〜30℃が理想的であり、混合
比率は、水100重量%に対し、合成液0.5重量%以上
の割合でよい。また、混合攪拌は、手動でも電動でも、
目測で分散状態が判断できる程度でよい。
(6) Water that mixes fuel oil in approximately equal amounts is the main role in achieving economic efficiency, complete combustion, and prevention of pollution.
The first of the mechanisms to completely accomplish the main task is to mix with carbon, kerosene, hydrogen peroxide, a dispersant, a synthetic solution such as sodium hydroxide. The water used for mixing is pure water, and the temperature is ideally 20 ° C. to 30 ° C. The mixing ratio may be 0.5% by weight or more of the synthetic liquid with respect to 100% by weight of water. In addition, mixing and stirring can be done manually or electrically.
It is sufficient that the dispersed state can be judged by visual inspection.

【0013】仕組みの第二は第一の混合水と重油との混
合であるが、この混合には十分注意する必要がある。最
初に重油は55℃〜65℃の範囲に加熱し、重油50%
容量以上、混合水50%容量以下、の条件で混合し、電
動プロペラ型攪拌機を使用し、上下,左右に重油と水が
十分流動するように攪拌する。攪拌スピードは100〜
150廻転/分とし、気泡の侵入を防止するように注意
して混合する。混合攪拌時間は、容量によって異なる
が、15分以上の時間を必要とする。
The second mechanism is the mixing of the first mixed water with the heavy oil, but this mixing needs to be carefully performed. First, heat the heavy oil to the range of 55 ℃ ~ 65 ℃, 50% heavy oil
The mixture is mixed under the conditions of the volume or more and the mixed water 50% or less, and the mixture is stirred using an electric propeller type agitator so that the heavy oil and the water can flow sufficiently in the vertical and horizontal directions. The stirring speed is 100 ~
Mix at 150 revolutions / minute, taking care to prevent air bubbles from entering. The mixing and stirring time depends on the volume, but requires 15 minutes or more.

【0014】(7)このようにして混合攪拌を終了した
酸素リッチ燃料油の重油をボイラーで燃焼すると、ボイ
ラー内へ噴射される油への着火スピードが非常に早く、
ボイラー(ハコダテ ボイラー A−500 2トン
型)での油と水の大小の爆発飛散の火炎が烈しく渦巻
き、普通の重油の炎の色が赤黄色で黒い煙を出すのに対
し、白黄色の炎で、肉眼では煙の発生が認められない程
度であった。
(7) When the heavy oil of the oxygen-rich fuel oil that has been mixed and agitated in this way is burned in the boiler, the speed of ignition of the oil injected into the boiler is very fast,
A large and small oil and water explosion and splash flame in a boiler (Hakodate Boiler A-500 2 ton type) swirls violently, and the color of ordinary heavy oil flame is red-yellow and black smoke, while white-yellow flame. No smoke was observed with the naked eye.

【0015】ボイラーの燃焼性からの予測ではあるが、
酸素リッチ重油の着火スピード,急速な高温燃焼,黒煙
皆無の燃焼性が発揮されるのは、 カーボン微粒子を核とし、これと親和,融合したケロ
シン,過酸化水素,ナトリウム,水等の混合液が、分散
剤と帯同して重油の中へ分散し、重油と融合混合し、分
離,遊離の生じない、均一、かつ、安定した状態で新し
い燃料油の形態となるものとおもわれ、また、
As predicted from the combustibility of the boiler,
Ignition speed of oxygen-rich heavy oil, rapid high-temperature combustion, and black smoke-free combustibility are exhibited by a mixture of kerosene, hydrogen peroxide, sodium, water, etc. Is dispersed in heavy oil together with a dispersant, and is mixed and mixed with heavy oil to form a new fuel oil in a uniform and stable state without separation and release, and

【0016】ボイラーでの燃焼のさい、普通は、重油
の燃焼温度が、1100℃程度であるのに対し、混合水
と重油との混合による酸素リッチ重油の燃焼温度は、最
高1480℃にものぼり、完全燃焼が認められた。これ
は、過酸化水素と水を主剤とする液体が、気体への加熱
気化現象のさいの1650倍という瞬間・急激な膨張・
爆発現象により、超微粒子となって重油組成分とともに
飛散し、完全燃焼し、高温を発するのが主要因とおもわ
れる。
During combustion in a boiler, the combustion temperature of heavy oil is usually about 1100 ° C, whereas the combustion temperature of oxygen-rich heavy oil produced by mixing mixed water and heavy oil is as high as 1480 ° C. , Complete combustion was observed. This is because the liquid containing hydrogen peroxide and water as the main ingredients is 1650 times the moment when it vaporizes by heating into a gas.
Due to the explosion phenomenon, it is thought that the main cause is that it becomes ultrafine particles and scatters with the heavy oil composition, complete combustion, and high temperature.

【0017】(8)油性酸素合成液のそれぞれの薬剤の
重量比%は、カーボンブラック1%,油性親和剤44
%,酸素化合剤40%,分散剤10%,ナトリウム5%
によって混合加工する。これらの素材は何れも市販され
ており、その取り扱いも危険性が少なく、簡単であり、
水,重油に対する分散混合も容易である。また、油性酸
素合成液と水との混合比は、合成液1に対し、水200
以下であり、合成液と水とを混合した混合水と重油との
混合比は、ほぼ等量にすることが可能である。
(8) The weight ratio% of each drug in the oil-based oxygen synthesis liquid is 1% of carbon black and 44 of the oil-based affinity agent.
%, Oxygen compound 40%, dispersant 10%, sodium 5%
Mix and process by. All of these materials are commercially available, and their handling is less dangerous and simple,
Easy to disperse and mix with water and heavy oil. In addition, the mixing ratio of the oil-based oxygen synthesis solution and water is 200
The ratio is as follows, and the mixing ratio of the mixed water obtained by mixing the synthetic liquid and water and the heavy oil can be made substantially equal.

【0018】上述のようにして混合製造される酸素リッ
チ燃料油は、水を重油と等量使用した油でありながら、
通常の油よりも高温で完全燃焼することにより、その経
済効果は試験燃焼における測定で30%以上にもなっ
た。また、高温完全燃焼により、ばいじん発生量,NO
x ,SOx の発生量が通常の油に比較してそれぞれ30
%以上の減少が認められ、経済性と社会環境に対する貢
献がきわめて大きいことが確認された。
The oxygen-rich fuel oil produced by mixing as described above is an oil containing water in an amount equal to that of heavy oil,
By fully burning at higher temperatures than regular oil, its economic effect was over 30% as measured in test burning. Also, due to high temperature complete combustion, soot and dust generation amount, NO
The amount of x and SO x generated is 30 each compared to normal oil.
A decrease of more than% was confirmed, and it was confirmed that the contribution to economy and social environment was extremely large.

【0019】[0019]

【実施例】以下、本願発明の実施例を述べる。 (1)油性酸素合成液の混合は、カーボンブラック10
g,ケロシン440g,過酸化水素400g,ポリオキ
シエチレナルキル硫酸エステル塩系のナフタレンスルフ
ォン酸100g,炭酸ナトリウム50gとし、これをプ
ラスチックもしくはステンレス容器に入れて、十分混合
するように攪拌して混合液を加工する。
EXAMPLES Examples of the present invention will be described below. (1) Carbon black 10
g, kerosene 440g, hydrogen peroxide 400g, polyoxyethylenalkyl sulfate ester salt-based naphthalene sulfonic acid 100g, sodium carbonate 50g, put this in a plastic or stainless steel container, and stir to mix well To process.

【0020】(2)水温20℃〜30℃の水を200リ
ットル準備する。水は水道水でも井戸水でもよい。容器
は、プラスチック製もしくはステンレス製のものがよ
い。この水に上記(1)で加工した合成液1リットルを
入れ、目視で十分混合されるまで攪拌する。攪拌は、手
動でも電動でもよいが、プロペラ型の攪拌翼付のものが
便利である。
(2) Prepare 200 liters of water having a water temperature of 20 ° C to 30 ° C. The water may be tap water or well water. The container is preferably made of plastic or stainless steel. 1 liter of the synthetic solution processed in the above (1) is added to this water, and the mixture is stirred until it is visually well mixed. The stirring may be manual or electric, but it is convenient to use a propeller type stirring blade.

【0021】(3)C重油200リットルを、ステンレ
ス製のタンクに入れ、蒸気もしくは電熱により60℃に
加温する。加温終了したC重油の中へ、上記(2)で加
工した混合水200リットルを少量づつ投入しながら攪
拌する。攪拌は電動の力の大きいプロペラ型の攪拌機を
使用し、油と混合水が均一になるように、上と下,右と
左に、液が流れるように行う。攪拌機の回転は低速で行
い、100〜150回転/分を標準とする。C重油20
0リットルの場合、15分以上の連続攪拌を行う。
(3) 200 liters of C heavy oil is placed in a stainless steel tank and heated to 60 ° C. by steam or electric heating. 200 liters of the mixed water processed in the above (2) is added little by little into the heated heavy oil C and stirred. Stirring is carried out by using a propeller type stirrer with a large electric power so that the liquid flows to the upper and lower sides and the right and left sides so that the oil and the mixed water become uniform. The stirrer is rotated at a low speed, and 100 to 150 rpm is standard. C heavy oil 20
In the case of 0 liter, continuous stirring for 15 minutes or more is performed.

【0022】(4)上記(3)により製造した酸素リッ
チC重油を、ロータリーバーナーダイワ製TR−5を使
用して燃焼試験を行った。試験は、通常のC重油15分
燃焼,酸素リッチC重油30分燃焼を1セットとし、最
初の試験から、1ヶ月後,1年後,1年半後の3回に分
けてそれぞれ1セットづつ実施した。
(4) The oxygen rich C heavy oil produced in (3) above was subjected to a combustion test using TR-5 manufactured by Rotary Burner Daiwa. The test consists of normal C heavy oil 15 minutes combustion and oxygen-rich C heavy oil 30 minutes combustion as one set, and one set each for three months, one month, one year, and one and a half years after the initial test. Carried out.

【0023】試験の内容は次の通りである。図1に示す
ように、ステンレス製タンク1に保管した酸素リッチC
重油製造油400リットルを燃料油供給ポンプ2により
電熱ヒーター3側に供給し、試験直前に80℃に電熱ヒ
ーター3により加温し、ロータリーバーナー4で、着
火,燃焼室5への噴射,燃焼を行った。燃焼に要した油
量は670g/分平均であり、この量は通常のC重油も
酸素リッチC重油も等量流動させた。
The contents of the test are as follows. As shown in FIG. 1, oxygen-rich C stored in a stainless steel tank 1
400 liters of heavy oil production oil was supplied to the electric heater 3 side by the fuel oil supply pump 2, heated to 80 ° C. by the electric heater 3 immediately before the test, and ignited, injected into the combustion chamber 5 and burned by the rotary burner 4. went. The amount of oil required for combustion was an average of 670 g / min, and this amount was caused to flow equally in both normal C heavy oil and oxygen-rich C heavy oil.

【0024】尚、図中、6はタンク1内の燃料油の温度
を検出する温度計、7は電熱ヒーター3により加熱され
た燃料油の温度を検出する温度計、8は排油・排気口、
9は送風メーター、10は燃料油供給調整メーター、1
1は燃料油の噴射口1は着火口、13は排気筒を示す。
In the figure, 6 is a thermometer for detecting the temperature of the fuel oil in the tank 1, 7 is a thermometer for detecting the temperature of the fuel oil heated by the electric heater 3, and 8 is a drainage / exhaust port. ,
9 is a blower meter, 10 is a fuel oil supply adjustment meter, 1
Reference numeral 1 is a fuel oil injection port 1, 1 is an ignition port, and 13 is an exhaust stack.

【0025】このような試験装置を用いて試験を行った
結果、 着火の容易性は、酸素リッチC重油が全て1回の着火
でスタートできたのに対し、通常のC重油は数回の着火
操作を必要とした。 煙の発生は、通常のC重油が黒い煙を烈しく出したの
に対し、酸素リッチC重油は燃焼スタート時に若干の黒
い煙を出しただけで、試験30分間、ほとんど煙を意識
しない程クリアーなものであった。なお、ばいじん濃度
は、JIS 28808 円筒ろ紙法で、C重油が0.1
8g/m3 に対し、酸素リッチC重油は0.04g/m3
であった。 炎の色は、通常のC重油が赤黄色であるのに対し、酸
素リッチC重油は白黄色であり、温度測定機での数値
は、C重油が1000℃〜1100℃であるのに対し、
酸素リッチC重油は1400℃〜1480℃であった。 NOx とSOx の発生量は、NOx が、JIS B7
982 化学発光方式でC重油が250/cm3 /m3
であるのに対し、酸素リッチC重油は150/cm3 /m
3 Nであった。また、SOx は、JIS K0103沈
澱滴定法で、C重油が900PPMであるのに対し、酸
素リッチC重油は540PPMであった。
As a result of conducting a test using such a test apparatus, the ease of ignition was found to be able to start with oxygen-rich C heavy oil all by one ignition, whereas with ordinary C heavy oil several ignitions were possible. Needed operation. As for the smoke generation, the oxygen-rich C heavy oil produced a little black smoke at the start of combustion, whereas the normal C heavy oil produced a black smoke violently. It was a thing. The dust concentration is JIS 28808 cylindrical filter paper method, and C heavy oil is 0.1
Oxygen-rich C heavy oil is 0.04 g / m 3 compared to 8 g / m 3.
Met. The color of the flame is red-yellow for normal C-heavy oil, whereas it is white-yellow for oxygen-rich C-heavy oil, and the value measured by the temperature measuring machine is 1000 ° C to 1100 ° C for C-heavy oil.
Oxygen-rich C heavy oil was 1400 ° C-1480 ° C. As for the amount of NO x and SO x generated, NO x is JIS B7
982 Chemistry emission method, C heavy oil is 250 / cm 3 / m 3 N
On the other hand, oxygen-rich C heavy oil is 150 / cm 3 / m
It was 3 N. Further, SO x was JIS K0103 precipitation titration method, and C heavy oil was 900 PPM, while oxygen-rich C heavy oil was 540 PPM.

【0026】なお、試験未使用の酸素リッチC重油を、
100リットルづつ透明のプラスチック容器に移し、一
方はそのまま静置し、他方を1週間毎に15分間烈しく
振動を与え、水の分離状態を、1ヶ月後,1年後,1年
半後に測定したが、3回とも水の分離は全く認められな
かった。また、その都度顕微鏡によって混合水と油の結
合状況をチェックしたが、全く変わりなかった。
The oxygen-rich C heavy oil which has not been tested is
100 liters each was transferred to a transparent plastic container, one was left as it was, the other was violently vibrated for 15 minutes every week, and the state of water separation was measured after one month, one year, one and a half years. However, no separation of water was observed at all three times. In addition, each time the binding state of the mixed water and oil was checked with a microscope, but it did not change at all.

【0027】[0027]

【発明の効果】以上説明したように、本発明により製造
される酸素リッチ燃料油は、水と重油を等量使用した油
でありながら、高温で完全燃焼することにより、重油単
体燃焼と比較し、その経済的メリットは30〜40%と
大幅な効果がある。また、高温完全燃焼により、ばいじ
ん発生量,NOx ,SOx の発生量が通常の油に比較し
てそれぞれ30%以上の減少が認められ、経済性ととも
に社会環境に対する貢献がきわめて大きい効果がある。
As described above, the oxygen-rich fuel oil produced according to the present invention is an oil containing equal amounts of water and heavy oil, but is completely combusted at high temperature, so that it can be compared with heavy fuel oil single combustion. The economic merit is 30 to 40%, which is a great effect. Also, due to the high temperature complete combustion, the amount of soot and dust, the amount of NO x , and the amount of SO x generated are reduced by 30% or more respectively as compared with normal oil, which has an extremely great effect on the economical and social environment. .

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

【図1】この発明の製造法によって得られた燃料油の燃
焼試験装置の概略説明図である。
FIG. 1 is a schematic explanatory view of a fuel oil combustion test apparatus obtained by a manufacturing method of the present invention.

【符号の説明】[Explanation of symbols]

1 ステンレス製タンク 2 燃料油供給ポンプ 3 電熱ヒーター 4 ロータリーバーナー 5 燃焼室 6 温度計 7 温度計 8 排油・排気口 9 送風メーター 10 燃料油供給調整メーター 11 噴射口 12 着火口 13 排気筒 1 Stainless Steel Tank 2 Fuel Oil Supply Pump 3 Electric Heater 4 Rotary Burner 5 Combustion Chamber 6 Thermometer 7 Thermometer 8 Oil Discharge / Exhaust Port 9 Blower Meter 10 Fuel Oil Supply Adjustment Meter 11 Injection Port 12 Ignition Port 13 Exhaust Tube

Claims (6)

【特許請求の範囲】[Claims] 【請求項1】 カーボン,油性親和材,酸素化合剤,分
散剤,ナトリウム等を混合し、油性酸素合成液に加工
し、これを水中に分散混合して酸素合成液と水の混合水
となし、更にこの混合水を重油と混合したことを特徴と
する酸素リッチ燃料油の製造方法。
1. A mixture of carbon, an oily affinity material, an oxygen compound, a dispersant, sodium, etc., is processed into an oily oxygen synthesis liquid, and this is dispersed and mixed in water to obtain a mixed water of the oxygen synthesis liquid and water. And a method for producing an oxygen-rich fuel oil, characterized in that the mixed water is mixed with heavy oil.
【請求項2】 カーボンは、スス,油煙,松煙等の微粒
子炭素分を含む請求項1に記載の製造法。
2. The production method according to claim 1, wherein the carbon contains fine carbon particles such as soot, oil smoke, and pine smoke.
【請求項3】 油性親和剤は、ケロシン,軽油を含む請
求項1に記載の製造法。
3. The method according to claim 1, wherein the oily affinity agent includes kerosene and light oil.
【請求項4】 酸素化合剤は、過酸化水素,オゾンを含
む請求項1に記載の製造法。
4. The production method according to claim 1, wherein the oxygen compound contains hydrogen peroxide and ozone.
【請求項5】 分散剤は、ポリオキシエチレンアルキル
硫酸エステル塩,ナフタレンスルフォン酸ホルマリン縮
合物,ポリオキシエチレンアルキルエーテル,アルキル
アミン塩,トリアジン系分散剤等を含む請求項1に記載
の製造法。
5. The method according to claim 1, wherein the dispersant includes a polyoxyethylene alkyl sulfate ester salt, a naphthalene sulfonic acid formalin condensate, a polyoxyethylene alkyl ether, an alkylamine salt, a triazine-based dispersant, and the like.
【請求項6】 ナトリウムは、マグネシウム,水酸化ナ
トリウム,塩化ナトリウム,炭酸ナトリウムを含む請求
項1に記載の製造法。
6. The method according to claim 1, wherein sodium includes magnesium, sodium hydroxide, sodium chloride and sodium carbonate.
JP33404892A 1992-12-15 1992-12-15 Production of oxygen-rich fuel oil Pending JPH06179883A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP33404892A JPH06179883A (en) 1992-12-15 1992-12-15 Production of oxygen-rich fuel oil

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP33404892A JPH06179883A (en) 1992-12-15 1992-12-15 Production of oxygen-rich fuel oil

Publications (1)

Publication Number Publication Date
JPH06179883A true JPH06179883A (en) 1994-06-28

Family

ID=18272933

Family Applications (1)

Application Number Title Priority Date Filing Date
JP33404892A Pending JPH06179883A (en) 1992-12-15 1992-12-15 Production of oxygen-rich fuel oil

Country Status (1)

Country Link
JP (1) JPH06179883A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4846642A (en) * 1986-11-08 1989-07-11 Wankel Gmbh Rotary piston blower with foamed synthetic material surfaces running along roughened metal surfaces
KR101240549B1 (en) * 2012-07-11 2013-03-11 서동관 Combustion efficiency improver for coal

Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH061983A (en) * 1992-06-19 1994-01-11 Mitsui Eng & Shipbuild Co Ltd Gas-and water-mixed fuel oil
JPH0617062A (en) * 1992-07-02 1994-01-25 Aroma Kagaku Kikai Kogyo:Kk Combustion aid for petroleum fuel

Patent Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH061983A (en) * 1992-06-19 1994-01-11 Mitsui Eng & Shipbuild Co Ltd Gas-and water-mixed fuel oil
JPH0617062A (en) * 1992-07-02 1994-01-25 Aroma Kagaku Kikai Kogyo:Kk Combustion aid for petroleum fuel

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4846642A (en) * 1986-11-08 1989-07-11 Wankel Gmbh Rotary piston blower with foamed synthetic material surfaces running along roughened metal surfaces
KR101240549B1 (en) * 2012-07-11 2013-03-11 서동관 Combustion efficiency improver for coal

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