JP2018136112A - Method of manufacturing device for supplying nano micro-particle water (particle diameter 1 to 100 nm) as high functional air for combustion, improving combustion efficiency and generating such high functional air for combustion - Google Patents
Method of manufacturing device for supplying nano micro-particle water (particle diameter 1 to 100 nm) as high functional air for combustion, improving combustion efficiency and generating such high functional air for combustion Download PDFInfo
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- 239000001301 oxygen Substances 0.000 claims description 38
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Abstract
Description
本発明は燃焼装置(火力発電所・自動車・船舶エンジン・発電機・汎用ボイラー・冷暖房給湯器)等の燃料基油には重油・灯油・軽油・廃油がある。その燃焼装置に供給される燃焼空気に、ナノ微細粒子水(粒子径1〜100nm)を生成含有することにより、高度化された燃焼用高機能空気が生成される。それを燃焼装置に燃焼空気として供給する。そして燃焼装置の燃焼室において、水分子(H2O)が熱エネルギーにより存在出来なくなり酸素と水素に分解する。その水素と酸素の反応(分解・結合)現象が天文学的な数字レベルにて起こる。その活性化運動の時に大きな発熱エネルギーが発生する。それが水素燃焼化となり燃焼効率を高めるシステムに関するものである。In the present invention, fuel base oils for combustion apparatuses (thermal power plants, automobiles, ship engines, generators, general-purpose boilers, heating / cooling water heaters), etc. include heavy oil, kerosene, light oil, and waste oil. By producing and containing nano fine particle water (particle diameter: 1 to 100 nm) in the combustion air supplied to the combustion apparatus, sophisticated high-performance air for combustion is generated. It is supplied to the combustion device as combustion air. In the combustion chamber of the combustion apparatus, water molecules (H 2 O) can no longer exist due to thermal energy and decompose into oxygen and hydrogen. The reaction between hydrogen and oxygen (decomposition / bonding) occurs at the astronomical numerical level. Large heat energy is generated during the activation movement. It relates to a system that increases hydrogen combustion efficiency and combustion efficiency.
燃焼装置に使用される燃焼空気は、一般的に火力発電所等の大型からボイラーのような小型機器の燃焼機器を含めて、導入される大気中の空気は冷却・加熱・除湿・加湿処理はせずに燃焼装置に直接供給されている。その場所の外気の空気をそのまま、処理することなく導入される。そして1年間通じて温度・湿度をコントロールせずに簡単なフィルター程度を装着して燃焼装置にそのまま燃焼空気として送っているのが実情である。Combustion air used for combustion equipment is generally used for cooling, heating, dehumidification, and humidification treatment of air in the atmosphere, including combustion equipment for large to small boilers such as boilers. Without being supplied directly to the combustion device. The outside air in the place is introduced without being processed. The actual situation is that the temperature and humidity are not controlled throughout the year, and a simple filter is attached to the combustion device as it is as combustion air.
一般的な、エンジンの原動出力は、エンジンの空気加速に使われるエネルギーと噴射された後の空気運動エネルギーの差異で表される。それは空気重量(密度kg/m3)と空気速度(m/s)の2乗の積に比例する。従って原動出力エネルギーを増加させるためには空気重量をいかに増加させることが技術改革の大きな課題であると言われている。Generally, the engine power output is expressed by the difference between the energy used for air acceleration of the engine and the air kinetic energy after being injected. It is proportional to the product of the square of air weight (density kg / m 3 ) and air velocity (m / s). Therefore, it is said that how to increase the air weight is a major issue of technological reform in order to increase the driving output energy.
一般的な空気の密度(kg/m3)について温度毎の空気密度の値を下記に示す。(1気圧の状態の時)
乾球温度 −50℃ 空気密度 1.534kg/m3
乾球温度 0℃ 空気密度 1.293kg/m3
乾球温度 +20℃ 空気密度 1.205kg/m3
乾球温度 +40℃ 空気密度 1.127kg/m3
上記に示すように1気圧の時の空気密度は温度の低い状態が空気密度値は高い値を示す。The value of air density at each temperature is shown below for general air density (kg / m 3 ). (At 1 atm)
Dry bulb temperature −50 ° C. Air density 1.534 kg / m 3
Dry bulb temperature + 20 ° C. Air density 1.205 kg / m 3
Dry bulb temperature + 40 ° C Air density 1.127kg / m 3
As described above, the air density at 1 atm indicates a high air density value when the temperature is low.
昨年、大きな国際環境会議が開催された。気候変動枠約21回締結国会議(COP21)及び京都議定書第11回締結国際会議が開催された。それにより日本国の二酸化炭素の削減目標が策定された。我国は2030年までに26%削減(2013年度比)することが決まりました。しかし二酸化炭素の排出量の内、燃焼装置の割合が非常に高い。燃焼装置に使用される基油の総量規制が喫緊の課題であることは誰しも承知している。しかし装置の燃焼装置は戦後から殆ど改善されていないに等しい。部分的な機器の熱効率改善技術の向上はあるが、燃焼効率改善の抜本的な改革装置は今もって生まれていない。Last year, a big international environmental conference was held. The 21st Conference of the Parties to the Climate Change (COP21) and the 11th International Conference of the Kyoto Protocol were held. As a result, Japan's carbon dioxide reduction target was formulated. Japan has decided to reduce by 26% (compared to FY2013) by 2030. However, of the carbon dioxide emissions, the proportion of combustion equipment is very high. Everyone knows that the regulation of the total amount of base oil used in combustion equipment is an urgent issue. However, the combustion device of the device is equivalent to little improvement since the war. Although there are improvements in technology for improving the thermal efficiency of partial equipment, no drastic reformer for improving combustion efficiency has yet been born.
一般的な燃焼とは、物質が光と熱を出して酸素と結合する化学反応である、多種多様な燃焼機械装置と、ごみ焼却も燃焼そのものである。燃焼を理解するには基礎的ことを知る必要がある。そこで内燃機関燃料の性状について、A重油は炭素分86.2%・水素分13.5%・硫黄分0.5%以下・酸素分0・比重0.86以下・水分0.2%以下・窒素分0.02%以下・発熱量10200kcal/kg。軽油は炭素分85.5%・水素分14.0%・硫黄分0.001%以下・酸素分0・比重0.86以下・水分0・窒素分0.05%・発熱量10200kcal/kg。灯油は炭素分85.5%・水素分14.5%・硫黄分0.5%以下・酸素分0・比重0.79・水分0.001%・窒素分0.001%・発熱量10300kcal/kg以上である。General combustion is a chemical reaction in which a substance emits light and heat and combines with oxygen, and a wide variety of combustion machinery and waste incineration are combustion itself. To understand combustion, you need to know the basics. Therefore, regarding the properties of the internal combustion engine fuel, A heavy oil has a carbon content of 86.2%, a hydrogen content of 13.5%, a sulfur content of 0.5% or less, an oxygen content of 0, a specific gravity of 0.86 or less, a water content of 0.2% or less, Nitrogen content 0.02% or less, calorific value 10200 kcal / kg. Light oil has 85.5% carbon, 14.0% hydrogen, 0.001% or less sulfur, 0 oxygen, 0.86 or less moisture, 0% nitrogen, 0.05% nitrogen, and a calorific value of 10200 kcal / kg. Kerosene has a carbon content of 85.5%, a hydrogen content of 14.5%, a sulfur content of 0.5% or less, an oxygen content of 0, a specific gravity of 0.79, a moisture content of 0.001%, a nitrogen content of 0.001%, and a calorific value of 10300 kcal / kg or more.
また、燃焼とは物質と酸素が化合する酸化の化学変化である。酸化(燃焼)は熱や光を出しながら激しく酸化することを燃焼という。炭素の燃焼は炭素C+酸素O2→二酸化炭素CO2となり、熱・光を出して燃え、反応はガス物質となる。水素の燃焼は、水素2H2+酸素O2→水2H2Oとなり、熱・光を出して爆発的に燃える、反応後に水素は水となる、酸素は水蒸気の状態で発生し、冷えると水滴になる。硫黄の燃焼は、硫黄S+酸素O2→SO2二酸化硫黄となり、熱・うすい青色の光を出して燃える。Combustion is an oxidation chemical change in which a substance and oxygen combine. Oxidation (combustion) is violent oxidation while giving off heat or light. The combustion of carbon becomes carbon C + oxygen O 2 → carbon dioxide CO 2, and it burns by emitting heat and light, and the reaction becomes a gas substance. Combustion of hydrogen becomes hydrogen 2H2 + oxygen O2 → water 2H2O, which generates heat and light and burns explosively. After the reaction, hydrogen becomes water, oxygen is generated in the state of water vapor, and when cooled, it becomes water droplets. The combustion of sulfur becomes sulfur S + oxygen O 2 → SO 2 sulfur dioxide, and it burns with heat and light blue light.
燃焼空気量は、燃焼の基礎反応から求める。可燃物質を構成する主な要素は炭素C、水素H、硫黄Sの3つのいずれか全部からなっている。これらの元素の燃焼反応の量的な関係から、燃焼に要する空気量や燃焼生成ガス量を求めることができる。次に3元素の酸素量すなわち理論空気量を求める。
炭素はC(12kg)+O2(22.4nm3)→CO2(22.4Nm3)から12kgの炭素が22.4Nm3の酸素と反応(燃焼)して、22.4Nm3の炭酸ガス(二酸化炭素)ができる。よって、炭素1kgの燃焼に必要な酸素は22.4Nm3/12kg→1.867Nm3/kgである。
水素はH2(2kg)+1/2O2(11.2Nm3)→H2O(22.4Nm3蒸気又は水18kg)から2kgの水素が11.2Nm3の酸素と燃焼反応22.4Nm3の水蒸気ができる。又は18kgの水ができる。よって水素1kgの燃焼に必要な酸素は11.2Nm3÷2kg→5.6Nm3である。
硫黄はS(32kg)+O2(22.4Nm3)→SO2(22.4Nm3)から32kgの硫黄が22.4Nm3の酸素と反応(燃焼)して、22.4Nm3の二酸化硫黄ができる。
よって、硫黄1kgの燃焼に必要な酸素は22.4Nm3÷32kg→0.7Nm3である。The amount of combustion air is obtained from the basic reaction of combustion. The main elements constituting the combustible material are all three of carbon C, hydrogen H, and sulfur S. From the quantitative relationship of the combustion reaction of these elements, the amount of air required for combustion and the amount of combustion product gas can be obtained. Next, the oxygen amount of the three elements, that is, the theoretical air amount is obtained.
From carbon (12 kg) + O 2 (22.4 nm 3) → CO 2 (22.4 Nm 3), 12 kg of carbon reacts (combusts) with 22.4 Nm 3 of oxygen to produce 22.4 Nm 3 of carbon dioxide (carbon dioxide). Therefore, the oxygen required for combustion of 1 kg of carbon is 22.4 Nm3 / 12 kg → 1.867 Nm3 / kg.
From H2 (2 kg) +1/2 O2 (11.2 Nm3) → H2O (22.4 Nm3 steam or water 18 kg), 2 kg of hydrogen is 11.2 Nm3 of oxygen and a combustion reaction of 22.4 Nm3 of water. Or 18 kg of water. Therefore, the oxygen required for combustion of 1 kg of hydrogen is 11.2 Nm 3 ÷ 2 kg → 5.6 Nm 3.
Sulfur is S (32 kg) + O 2 (22.4 Nm 3) → SO 2 (22.4 Nm 3), 32 kg of sulfur reacts (combusts) with 22.4 Nm 3 of oxygen to produce 22.4 Nm 3 of sulfur dioxide.
Therefore, the oxygen required for combustion of 1 kg of sulfur is 22.4 Nm 3 ÷ 32 kg → 0.7 Nm 3.
理論空気量は可燃分1kgの燃焼に必要な理論的(化学組成から求める)酸素量である。(空気量ではない)ごみ1中に含まれる炭素、水素、酸素、硫黄の量(単位はkg)をそれぞれC、H、O,Sとすると理論酸素量は次式で与えられる。O0→1.87C+5.6(H―O/8)+0.7SThe theoretical air amount is the theoretical (determined from the chemical composition) oxygen amount necessary for combustion of 1 kg of combustible component. If the amounts (unit: kg) of carbon, hydrogen, oxygen, and sulfur contained in the waste 1 (not the amount of air) are C, H, O, and S, the theoretical oxygen amount is given by the following equation. O0 → 1.87C + 5.6 (H−O / 8) + 0.7S
また、理論空気量は実際にごみを焼却するときは酸素だけで燃やすのではなく、必要な酸素量を空気の形で供給する。この空気量を理論空気量といい,A0と書く。空気と酸素の体積比は100:21であるから,A0:O0→100:21となり∴A0→(100/21)×O0であるから、A0→(100/21)×{1.87C+5.6(H―O/8)+0.7S} ∴A0→8.89C+26.7(H―O/8)+3.3S Nm3/kgとなる。The theoretical amount of air does not burn only with oxygen when actually incinerating waste, but supplies the necessary amount of oxygen in the form of air. This air volume is called the theoretical air volume and is written as A0. Since the volume ratio of air and oxygen is 100: 21, A0: O0 → 100: 21 and ∴A0 → (100/21) × O0, so A0 → (100/21) × {1.87C + 5.6 (H−O / 8) + 0.7S} ∴A0 → 8.89C + 26.7 (H−O / 8) + 3.3S Nm3 / kg.
空気比について、実際の燃焼に使用した空気量をA(Nm3/kg)で表す。
また,Aを理論空気量A0で除した値を空気比と呼びmで表す。m→A/A0。
又空気比は排ガス中の酸素濃度から(O2%)から近似的に求める事ができる。その式は、m→21/(21―O2)である。Regarding the air ratio, the amount of air used for actual combustion is represented by A (Nm3 / kg).
A value obtained by dividing A by the theoretical air amount A0 is referred to as an air ratio and is represented by m. m → A / A0.
The air ratio can be approximately obtained from the oxygen concentration in the exhaust gas (O2%). The equation is m → 21 / (21−O2).
実際の理論空気量を次式からもとめてみる。ごみ1kgの燃焼に必要な理論空気量はいくらか。また空気比を2.6としたとき燃焼空気量はいくらか。
性状は炭素21.2%、水素2.94%、酸素16.47%、硫黄0.032%とする。組成より、ごみ1kgに含まれる各元素の重量はC→0.212kg,H→0.029kg、O→0.1647kg、S→0.00032kgである。これを9項で示した式に代入する。
A0→8.89×0.212+26.7×(0.0294―0.1647/8)+3.3×0.00032→2.12Nm3/kgとなる。そして実際に使用した空気量は次式からもとめる。A→m×A0→2.6×2.12→5.53Nm3/kgとなる。
以上の項目は一般空気(大気の空気をそのまま燃焼空気として取り入れる)を燃焼空気として燃焼させている。The actual theoretical air volume is calculated from the following equation. What is the theoretical amount of air required to burn 1 kg of garbage? What is the amount of combustion air when the air ratio is 2.6?
The properties are 21.2% carbon, 2.94% hydrogen, 16.47% oxygen, and 0.032% sulfur. From the composition, the weight of each element contained in 1 kg of garbage is C → 0.212 kg, H → 0.029 kg, O → 0.1647 kg, S → 0.00032 kg. This is substituted into the formula shown in item 9.
A0 → 8.89 × 0.212 + 26.7 × (0.0294−0.1647 / 8) + 3.3 × 0.00032 → 2.12 Nm3 / kg. The actual amount of air used can be obtained from the following equation. A → m × A0 → 2.6 × 2.12 → 5.53 Nm3 / kg.
In the above items, general air (intake of atmospheric air as combustion air as it is) is burned as combustion air.
基油の燃焼について、炎の中の炎は、燃料と空気中の酸素との化学反応である。基油と空気中の水分の水素は、2H2+O2→2H2Oである、しかしこの反応は全体として成り立っている物であって「総括反応」と呼ばれている。の中で実際にこの反応が起きているわけではない。実際の燃焼中の基油成分及び空気中成分の燃焼現象理論は成立していない、それぞれの学者は百家争鳴であるのが実際のところである。しかし水素の場合は簡単なので例にあげる。他は完全に分かって言えるわけではない。高温になるとH2、O2分子は存在できなくなり、結合が外れてH、H、O、O原子に勝手に動きだす、そしてエネルギーが与えられて分解する。全部がそうなるわけではなく、一部が化学的に活性な種が出来ることが重要である。それらは分子に戻ろうとする性質がある、その動きはエネルギーを必要としない。例えば、酸素と水素が存在すると、O2+H→OH+Oが反応して、つの活性種が(OH、O)が形成される。この反応は「総括反応」にたいして「素反応」という。一つの活性種から二つの活性種がうまれ、「連鎖分岐反応」と呼んでネズミ算式に活性種が増えてくる。これはエネルギーを必要としない。このような活性腫同士が再び結合する時は、大きな発熱を伴うので、火炎は高温になる。Hが1gあたり、約120キロカロリーの熱を放出する。水素と酸素の反応は、約20個程度の素反応から成り立っている。Regarding the combustion of base oil, the flame in the flame is a chemical reaction between the fuel and oxygen in the air. The hydrogen in the base oil and the water in the air is 2H2 + O2 → 2H2O, but this reaction is established as a whole and is called “overall reaction”. In fact, this reaction is not happening. The theory of combustion phenomena of base oil components and air components during actual combustion has not been established, and each scientist is in fact a hundred controversy. But in the case of hydrogen, it's easy, so I'll give you an example. Others are not completely understood. At high temperatures, H2 and O2 molecules can no longer exist, bonds are released and H, H, O, and O atoms start to move on their own, and energy is applied to decompose them. It is important that not all are, but that some are chemically active species. They have the property of trying to return to molecules, their movement does not require energy. For example, in the presence of oxygen and hydrogen, O2 + H → OH + O reacts to form one active species (OH, O). This reaction is called “elementary reaction” as opposed to “summary reaction”. Two active species are born from one active species, which is called “chain branching reaction”, and the active species increases in the mouse formula. This does not require energy. When such active tumors recombine with each other, there is a large fever and the flame becomes hot. H releases about 120 kilocalories of heat per gram. The reaction between hydrogen and oxygen consists of about 20 elementary reactions.
エマルジョン燃料(ガソリン・重油・灯油・軽油・廃油)は水と界面活性剤や乳化剤を添加し撹拌・混合させ乳化させた燃料である。液中の粒子が瞬時にミクロ爆発し油粒子を微細化、飛散させることで酸素との接触面を大きくし、完全燃焼する。これにより二酸化炭素や窒素酸化物、粒子状物質の発生を抑え内燃機関が排出するガスがもたらす環境負荷を低減する効果がある。これらの乳化された燃料の外見は乳化して白濁した液体である。水粒子を油の膜層が界面活性剤を介在しているのですぐには分離しない。A重油と水を混合したエマルジョン燃料であればA重油の成分を含んだエマルジョン燃料になり、軽油であれば軽油の性質、灯油あれば灯油の性質、というようにエマルジョン燃料の性質は水と混合する燃料によって異なる。Emulsion fuel (gasoline, heavy oil, kerosene, light oil, waste oil) is a fuel that is emulsified by adding water, surfactant and emulsifier, stirring and mixing. The particles in the liquid instantly micro-explode and refine and disperse the oil particles, increasing the contact surface with oxygen and complete combustion. This has the effect of suppressing the generation of carbon dioxide, nitrogen oxides, and particulate matter, and reducing the environmental burden caused by the gas discharged from the internal combustion engine. The appearance of these emulsified fuels is an emulsified and cloudy liquid. Water particles are not separated immediately because the oil film layer contains a surfactant. If the emulsion fuel is a mixture of A heavy oil and water, it will be an emulsion fuel containing the components of A heavy oil. If it is light oil, the nature of light oil, if it is kerosene, the nature of kerosene, and so on. It depends on the fuel used.
本項からは燃焼空気の様々な取組みの技術を紹介する。
高湿度型ガスタービンエンジンは1981年に提案されたAHAT(advanced humid air turbine)である燃焼空気に湿分を添加しタービンの高効率化を図る研究が行われている。しかし、この湿分噴霧の微細水の粒径は、平均粒径14μmと大きく平均化されていることにより、噴霧後すぐ水粒子同士が結合し装置内が結露するため、有効な燃焼空気とは言えないのが実情である。AHATの発電機効率の目標が100MWの出力において55%が目標と言われている。ここでは約5%の改善効果があった。This section introduces various technologies for combustion air.
A high-humidity gas turbine engine, which is AHAT (Advanced Humid Air Turbine) proposed in 1981, has been studied to increase the efficiency of the turbine by adding moisture to combustion air. However, since the particle size of the fine water in this moisture spray is greatly averaged to an average particle size of 14 μm, the water particles are combined immediately after spraying and the inside of the apparatus is condensed. The fact is that I can't say that. The target of AHAT generator efficiency is said to be 55% at 100 MW output. Here, there was an improvement effect of about 5%.
一般的に応用されているエンジンの出力を高めるには、推進力の値は燃焼消費量を除した値で決まるが、更に増加させるためには圧縮機の圧縮効率を高めて密度(空気重量)を大きくする。また燃焼温度を高く設定する。
以上2点が現状行われている方法である。In order to increase the output of engines that are generally applied, the value of propulsive force is determined by dividing combustion consumption, but in order to increase it further, the compression efficiency of the compressor is increased and the density (air weight) is increased. Increase Also set the combustion temperature high.
The above two points are currently used methods.
酸素燃焼を用いたCO2を排出しない石炭火力発電所の実現に向けて現在進んでいる。空気燃焼は、文字通り燃料の燃焼に空気を使用する。空気は容量ベースで約79%の窒素と約21%の酸素で構成されているため、空気燃焼の排ガスにも約79%の窒素が含まれることからCO2は約18%にしかならない。一方酸素燃焼は、燃料の燃焼に、空気に替えて純酸素を使用する。窒素がそもそも含まれていないため、排ガスの主成分がCO2となる上、排ガス量が約5分の1に減少する。この特徴から、酸素燃焼では容易にCO2を回収することが可能となる。以下に酸素燃焼のメリットを示す。
1.燃焼排ガス中のCO2濃度が高いので、排ガス精製,CO2液化などの後処理が不要あるいは簡素化できる。
2.燃焼排ガスを再循環した際に、ガス中のNOXが炉内で還元されるため、NOX発生量が低減する。
3.再循環ガス量を減らし,人工酸素濃度を上げることで、ボイラーをコンパクトにできる可能性がある。
4.新設はもちろんのこと、既設ボイラーへの酸素燃焼適用改造も可能である。
5.酸素製造設備で分離したN2やArの商用利用も計画できる。
本件プロジェクトはカライド酸素燃焼プロジェクトという。豪州にて進められている。Progress is currently being made toward the realization of a coal-fired power plant that does not emit CO2 using oxyfuel combustion. Air combustion literally uses air to burn fuel. Since air is composed of about 79% nitrogen and about 21% oxygen on a volume basis, CO2 is only about 18% because the exhaust gas from air combustion also contains about 79% nitrogen. On the other hand, oxygen combustion uses pure oxygen instead of air for fuel combustion. Since nitrogen is not included in the first place, the main component of the exhaust gas becomes CO2, and the amount of exhaust gas is reduced to about 1/5. From this feature, CO2 can be easily recovered by oxyfuel combustion. The merit of oxygen combustion is shown below.
1. Since the CO2 concentration in the combustion exhaust gas is high, post-treatment such as exhaust gas purification and CO2 liquefaction is unnecessary or simplified.
2. When NOx in the gas is reduced in the furnace when the combustion exhaust gas is recirculated, the amount of NOX generated is reduced.
3. There is a possibility that the boiler can be made compact by reducing the amount of recirculated gas and increasing the artificial oxygen concentration.
4). In addition to new installations, it is possible to remodel existing boilers by applying oxyfuel combustion.
5. Commercial use of N2 and Ar separated by oxygen production facilities can also be planned.
This project is called Callide Oxyfuel Project. It is underway in Australia.
現在の日本と世界における、燃焼機械の装置効率向上の技術は、一般空気燃焼装置が100%近い状態である。燃焼装置の効率を更に高めるためには、燃料の改革はもとより、燃焼装置の改善には自ずと限界があると考える。
本発明特許は燃焼空気にナノ微細粒子水(水分子に近い0〜100nm)を混合したことから、水素エネルギーを活用できる。本発明はこれらのことを可能にする装置である。
先行技術0007項に記載している、燃料に含有している水素H2は燃焼室内において、爆発的に燃焼し燃焼室を高温度になり燃焼効率を高めていることが科学的にも明らかになっている。今後燃焼空気に赴きを置き、燃焼効率を高めるために更なる技術革新が必要と考える。The current technology for improving the efficiency of combustion machines in Japan and the world is that the general air combustion system is nearly 100%. In order to further improve the efficiency of the combustor, there is a limit to the improvement of the combustor as well as the reform of the fuel.
The present invention patent can utilize hydrogen energy because nano fine particle water (0-100 nm close to water molecules) is mixed with combustion air. The present invention is an apparatus that enables these things.
Scientifically, it has become clear that the hydrogen H2 contained in the fuel described in the prior art 0007 is explosively burned in the combustion chamber, raising the temperature of the combustion chamber to increase the combustion efficiency. ing. We think that further technological innovation will be necessary in order to increase the combustion efficiency.
高湿度型ガスタ―ビンエンジンAHATは国内においても産学共同実証実験が行われて来た。本装置の燃焼効率は5%前後改善されたと報道がなされていた。本装置は水微細粒子口径が14μm前後の大きさであると報告書に記載されている、燃焼空気室周辺の写真によると装置内の殆どの部位が結露していることが見受けられた。
本来の目的は結露させない技術であったと思われる。例えば水粒子口径が、ナノレベル口径技術では結露することなく、且つ燃焼効率は格段と改善されていたと考えられる。本実証実験での検討課題改善報告書は開示されていない。A high-humidity gas turbine engine, AHAT, has undergone industry-university joint demonstration experiments in Japan. It was reported that the combustion efficiency of this equipment was improved by around 5%. According to the photograph around the combustion air chamber, which is described in the report that the diameter of the water fine particle is about 14 μm, it was found that most parts in the apparatus were condensed.
It seems that the original purpose was technology that did not cause condensation. For example, it is considered that the water particle diameter is not condensed by the nano-level diameter technique, and the combustion efficiency is remarkably improved. The report on improvement of the examination subject in this demonstration experiment is not disclosed.
前項の燃焼空気を高湿度にする目的は、水粒子を微細化することにより、水分子から水素を分離させ、水素燃焼化を行い、燃焼効率を高めることであったと思う。I think that the purpose of making the combustion air high humidity in the previous paragraph was to improve the combustion efficiency by separating the hydrogen from the water molecules by making the water particles finer, and performing hydrogen combustion.
発電機エンジンの燃焼空気条件は燃焼工学学会発行図書によると、温度15℃、相対湿度95%の温湿度が最も良いと記載されている。この条件の空気比重は1/0.83である。According to a book issued by the Society of Combustion Engineering, the combustion air condition of the generator engine is described as being best when the temperature is 15 ° C. and the relative humidity is 95%. The air specific gravity under this condition is 1 / 0.83.
他に現存する燃焼空気技術は酸素富加技術、純酸素技術があるが、普及するには程遠いと思われる。Other existing combustion air technologies include oxygen enrichment technology and pure oxygen technology, but they are far from widespread.
本発明は、従来の燃焼装置の燃焼空気は、大気中の外気の塵埃処理をするのみである。燃焼装置に燃料として供給される燃料基油は、その組成からも炭素・水素・硫黄の元素がほぼ100%占めている。基油の燃焼効率を高めるためには、燃焼空気品質を改善する必要性が高い。空気質機能改善は大きな要素を占めるものであると考える。しかし燃焼空気の高機能化の技術改善向上、改革は今日まで殆ど取組みされてこなかった。本発明は、自然界におけるナノ微細粒子水が生成される仕組みを、工学システムとして構築した。それにより1〜100nm粒子口径の水分子に近い粒径のナノ微細粒子水を高機能燃焼空気として、且つ水素エネルギーを活用する装置として燃焼効率を高めることを提供するものである。In the present invention, the combustion air of the conventional combustion apparatus only performs dust treatment of the outside air in the atmosphere. The fuel base oil supplied as fuel to the combustion apparatus is almost 100% carbon, hydrogen, and sulfur in terms of its composition. In order to increase the combustion efficiency of the base oil, it is highly necessary to improve the combustion air quality. Air quality improvement is a major factor. However, technological improvements and reforms to improve the functionality of combustion air have hardly been addressed to date. In the present invention, a mechanism for generating nano fine particle water in nature is constructed as an engineering system. Thereby, nano fine particle water having a particle size close to water molecules having a particle diameter of 1 to 100 nm is used as high-function combustion air, and as a device utilizing hydrogen energy, it is provided to increase combustion efficiency.
本発明は自然界の大気中におけるナノ微細水粒子が出来ている摂理として存在する。それは降雨時には大きな雨粒子が大きな粉塵を吸着降下処理し、その後太陽の日射により地表面の温度が上昇し草、土の水分が再蒸発し、その時大気中にナノ微細粒子水を大量に発生させ地表面の大気をその微細水で大量に覆い、その微細粒子水が細かな微細粉塵等を枕塵させて大気を浄化している。このような自然界の仕組みをシステムとして構築した。本装置はナノ微細粒子水1〜100nm口径を本発明装置内にて大量に発生させて燃焼空気として燃焼効率を高めることが本発明の特徴である。The present invention exists as a providence for producing nano-fine water particles in the natural atmosphere. When raining, large rain particles adsorb and process large dust particles, and then the surface temperature of the ground rises due to solar radiation and grass and soil moisture re-evaporates. At that time, a large amount of nano fine particle water is generated in the atmosphere. The air on the ground surface is covered with a large amount of fine water, and the fine particle water purifies the air by pulverizing fine fine dust. Such a mechanism of the natural world was constructed as a system. It is a feature of the present invention that this apparatus generates a large amount of nano fine particle water having a diameter of 1 to 100 nm in the apparatus of the present invention to increase combustion efficiency as combustion air.
本発明装置は噴霧室・空気加圧混合室及び沈殿室・沈殿水槽を備えた筐体とし、該噴霧室・空気加圧混合室は空気取り入れ口と燃焼高機能空気出口を設け、両者間には空気流通管制御ベンチュリー隔壁が設けられ隔壁板により空間が形成され、該空気取入れ口では燃焼空気を大気からの粉塵等を含んだ空気を取入れる。噴霧室・空気加圧混合室は、ナノ微細粒子水を噴霧し、燃焼用高機能空気の出口に向けて、更にナノ微細粒子に縮小化、又浄化しながら高機能化された空気に生成される。該給水槽と連結された給水管の先端となるノズルからポンプ圧により墳出された水をナノ微細粒子水として水煙を発生する水煙発生装置を構成し、該水煙出口より上記水煙を高機能空気に生成されて燃焼装置に供給するシステム特徴とする。The device of the present invention is a casing provided with a spray chamber / air pressurized mixing chamber and a sedimentation chamber / precipitation water tank, and the spray chamber / air pressurized mixing chamber is provided with an air intake and a combustion high function air outlet, Is provided with an air flow pipe control venturi partition, and a space is formed by the partition plate, and the air intake port takes in air containing dust and the like from the atmosphere. The spray chamber / air pressurization mixing chamber is sprayed with nano fine particle water, and is generated into highly functional air while being further reduced and purified to nano fine particles toward the outlet of high function air for combustion. The A smoke generator is configured to generate smoke from the water discharged by a pump pressure from a nozzle at the tip of a water supply pipe connected to the water tank as nano fine particle water, and the smoke from the smoke outlet is a highly functional air. System features that are generated and supplied to the combustion device.
本発明装置は大気中の粉塵、臭気、二酸化炭素等を本装置にて除去処理することが可能であることが特徴である。The apparatus of the present invention is characterized in that dust, odor, carbon dioxide, etc. in the atmosphere can be removed by the apparatus.
以上の説明から明らかなように、本発明によって生成された、ナノ微細粒子水燃焼空気は次に列挙する効果が得られる。
(1)超微細水粒子の大きさを解析分析する粒度分布装置計測から、1〜100nmの分布の粒径を生成することが確認出来た。
(2)超微細水の密度個数を解析する装置計測により1000兆個の値が得られた。
(3)(2)の生成された密度個数から水分子個数を計算上であるが100億個であると予想することが出来る。この値からH2とOの個数を割出し水素H2のエネルギーを計算することが出来る。
(4)(3)で得られた計算から、本装置と従来燃焼空気との改善効果は約10倍の効果が得られることが予測できる。As is clear from the above description, the effects of the nano-fine particle water combustion air produced by the present invention are listed below.
(1) It was confirmed from the particle size distribution analyzer measurement that analyzes and analyzes the size of the ultrafine water particles that a particle size with a distribution of 1 to 100 nm is generated.
(2) 1000 trillion values were obtained by measuring the density of ultrafine water.
(3) Although the number of water molecules is calculated from the number of densities generated in (2), it can be expected to be 10 billion. From this value, the number of H2 and O can be calculated to calculate the energy of hydrogen H2.
(4) From the calculation obtained in (3), it can be predicted that the improvement effect of the present apparatus and the conventional combustion air is about 10 times as effective.
以下、本発明の実施の形態を図面に基づき実施例に沿って説明する。Hereinafter, embodiments of the present invention will be described with reference to the drawings.
図1は、装置内の噴霧室兼加圧混合室3aにてナノ微細粒子水を噴霧し、装置の空間が加圧されながら、ナノ微細粒子水が空気流通隔壁及び中間仕切り壁を下流側に蛇行しながら、順にナノ微細粒子水を生成しながら供給する。燃焼用高機能空気を生成する目的の発生装置の概略図を示している。
その装置を図1とする。FIG. 1 shows that the nano fine particle water is sprayed in the spraying and pressure mixing chamber 3a in the apparatus, and the nano fine particle water moves the air circulation partition wall and the intermediate partition wall downstream while the space of the apparatus is pressurized. While meandering, the nano fine particle water is supplied while being produced. 1 shows a schematic view of a generator for the purpose of producing combustion high-performance air.
The apparatus is shown in FIG.
大気中の空気を吸込むためのファン5を設けた噴霧室兼空気加圧混合室3a、に吸込まれた空気(標準空気である、比重1.2、温度0〜45℃、粉塵濃度0.5mg/m3以下、湿度0〜99%)は噴霧室兼空気加圧混合室3aの空間においてナノ微細粒子水を噴霧し、該噴霧室兼空気加圧混合室3aと空気加圧混合室3bcの空間にて更に微細化されたナノ微細粒子水が生成される。ナノ微細粒子水は空気流通管制御用隔壁18a.19b、及び空気流通用中仕切り壁20c、を空気は蛇行を繰り返すことにより、これら3個の空間を経て燃焼用高機能空気として燃焼装置に本装置の、燃焼用高機能空気出口17から高機能空気管21を経て燃焼装置に供給する。Air sucked into a spraying and air pressure mixing chamber 3a provided with a fan 5 for sucking air in the atmosphere (standard air, specific gravity 1.2,
図1の噴霧室兼空気加圧混合室3.aと空気加圧混合室bc、沈殿室兼沈殿水槽4abc,それらを装置に組み込むための、外部ケーシング6.を含めてまとめて構成している。沈殿水槽4abcの液中を冷却する目的とした冷却コイル14を液中底部に取り付け、沈殿室4abcの液中槽内温度を3〜10℃の温度に維持する。それは冷凍機13、冷却コイル14、と冷媒配管15、にて形成して冷却維持を維持することになる。2. Spraying and air pressurized mixing chamber of FIG. 5. a and air pressurized mixing chamber bc, precipitation chamber / precipitation water tank 4abc, external casing for incorporating them into the apparatus It is composed collectively including The cooling coil 14 intended to cool the liquid in the precipitation water tank 4abc is attached to the bottom of the liquid, and the temperature in the liquid tank of the precipitation chamber 4abc is maintained at a temperature of 3 to 10 ° C. It is formed by the refrigerator 13, the cooling coil 14, and the refrigerant pipe 15 to maintain cooling.
図1の噴霧室兼空気加圧混合室3aの中間部上方には側壁より、給水管10はその先端にノズル11を形成している。A nozzle 11 is formed at the tip of the water supply pipe 10 from the side wall above the middle part of the spraying and air pressure mixing chamber 3a in FIG.
第1ノズル11から墳出した高圧水を該衝突物体12に衝突させることによる結果ナノ微細水粒子水を生成し、噴霧室兼空気加圧混合室3cに吸込まれた空気と共に、吸入加圧ファン5(加圧ファンと兼ねる)により、空気中の汚染物質は沈殿室兼沈殿水槽4abcに溶解されて沈殿する。As a result of colliding the high-pressure water discharged from the first nozzle 11 with the collision object 12, nano fine water particle water is generated, and together with the air sucked into the spray chamber / air pressurizing and mixing chamber 3c, a suction pressure fan 5 (also serving as a pressure fan) causes contaminants in the air to be dissolved and precipitated in the precipitation chamber / precipitation water tank 4abc.
本発明は全世界の多くの燃焼装置に必要な石油・石炭・LNG等のエネルギー資源が枯渇する危機とその総量抑制を迫られている環境下で燃焼装置の効率を大幅に改善出来る燃焼空気にナノ微細粒子水を含有して供給する装置を提供する。且つ使用燃料の大幅削減効果と排ガスである二酸化炭素・SOX・NOXが大幅に削減される。又本発明の高効率燃焼用高機能空気装置は総合的にエネルギー革命を担うトータルの機能を持っている。そのシステム装置を提供するものである。需要先は火力発電所・自動車・化学工場・製紙関連工場・鉄鋼プラント・船舶エンジン・汎用ボイラー・灯油焚き冷暖房給湯器等々がある。国内は基より全世界にニーズがあると考える。The present invention provides a combustion air that can greatly improve the efficiency of the combustor in an environment where energy resources such as oil, coal, and LNG necessary for many combustors around the world are exhausted and in an environment where the total amount of the resource is being constrained. An apparatus for supplying nano-particle water is provided. In addition, the carbon dioxide, SOX, and NOX, which are exhaust gases, are greatly reduced and the exhausted fuel is greatly reduced. The highly efficient combustion high-performance air device according to the present invention has a total function for taking an energy revolution as a whole. The system apparatus is provided. The customers include thermal power plants, automobiles, chemical factories, paper-related factories, steel plants, ship engines, general-purpose boilers, kerosene-fired air-conditioning and heating water heaters, and so on. I think that domestic needs are more in the world than in the group.
▲1▼ 装置概念図 1
▲2▼ 吸込み室
▲3▼ a 噴霧室・空気加圧混合室
b 空気加圧混合室
c 空気加圧混合室
▲4▼ a 沈殿室・沈殿水槽
b 沈殿室・沈殿水槽
c 沈殿室・沈殿水槽
▲5▼ 吸入加圧ファン
▲6▼ 装置ケーシング底板
▲7▼ 装置ケーシング上板
▲8▼ 高圧ポンプ
▲9▼ ポンプ吸い込み口
▲10▼ 第1給水管
▲11▼ 第1ノズル
▲12▼ 衝突球体
▲13▼ 冷凍機
▲14▼ 冷却コイル
▲15▼ 冷媒配管
▲16▼ 給水槽
▲17▼ 燃焼用高機能空気の出口
▲18▼ a.空気流通管制御用ベンチュリー隔壁
▲19▼ b.空気流通管制御用ベンチュリー隔壁
▲20▼ c.空気流通用中仕切り壁
▲21▼ 燃焼用高機能空気管
▲22▼ 排水管
▲23▼ 排水槽(1) Conceptual diagram of equipment 1
(2) Suction chamber (3) a Spray chamber / air pressurized mixing chamber b Air pressurized mixing chamber c Air pressurized mixing chamber (4) a Precipitation chamber / precipitation water tank b Precipitation chamber / precipitation water tank c Precipitation chamber / precipitation water tank (5) Suction pressure fan (6) Equipment casing bottom plate (7) Equipment casing top plate (8) High pressure pump (9) Pump suction port (10) First water supply pipe (11) First nozzle (12) Colliding sphere 13) Refrigerator <14> Cooling coil <15> Refrigerant piping <16> Water tank <17> High-function air outlet for combustion <18> a. Venturi bulkhead for controlling air flow pipe (19) b. Venturi bulkhead for controlling air flow pipe (20) c. Partition wall for air flow ▲ 21 ▼ High performance air pipe for combustion ▲ 22 ▼ Drainage pipe ▲ 23 ▼ Drainage tank
Claims (8)
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| JP2017051890A JP2018136112A (en) | 2017-02-21 | 2017-02-21 | Method of manufacturing device for supplying nano micro-particle water (particle diameter 1 to 100 nm) as high functional air for combustion, improving combustion efficiency and generating such high functional air for combustion |
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| Application Number | Priority Date | Filing Date | Title |
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| JP2017051890A JP2018136112A (en) | 2017-02-21 | 2017-02-21 | Method of manufacturing device for supplying nano micro-particle water (particle diameter 1 to 100 nm) as high functional air for combustion, improving combustion efficiency and generating such high functional air for combustion |
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| Publication Number | Publication Date |
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| JP2018136112A true JP2018136112A (en) | 2018-08-30 |
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110527768A (en) * | 2019-08-29 | 2019-12-03 | 苏州艾铭森科技有限公司 | A kind of accurate atomizing de-dusting control method of blast fumance |
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110527768A (en) * | 2019-08-29 | 2019-12-03 | 苏州艾铭森科技有限公司 | A kind of accurate atomizing de-dusting control method of blast fumance |
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