JPH0598272A - Activation of liquid fuel - Google Patents

Activation of liquid fuel

Info

Publication number
JPH0598272A
JPH0598272A JP28400991A JP28400991A JPH0598272A JP H0598272 A JPH0598272 A JP H0598272A JP 28400991 A JP28400991 A JP 28400991A JP 28400991 A JP28400991 A JP 28400991A JP H0598272 A JPH0598272 A JP H0598272A
Authority
JP
Japan
Prior art keywords
liquid fuel
fuel
granular solid
energy
radiator
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
JP28400991A
Other languages
Japanese (ja)
Inventor
Kiyonori Niino
清憲 新納
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.)
KAWASAKI SEISAKUSHO KK
NIPPON GIJUTSU KAIHATSU CENTER KK
Original Assignee
KAWASAKI SEISAKUSHO KK
NIPPON GIJUTSU KAIHATSU CENTER 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 KAWASAKI SEISAKUSHO KK, NIPPON GIJUTSU KAIHATSU CENTER KK filed Critical KAWASAKI SEISAKUSHO KK
Priority to JP28400991A priority Critical patent/JPH0598272A/en
Publication of JPH0598272A publication Critical patent/JPH0598272A/en
Pending legal-status Critical Current

Links

Abstract

PURPOSE:To activate a liquid fuel by bringing it into contact under agitation with a granular solid comprising an energy radiator. CONSTITUTION:A container 1 is a stainless steel cylinder with its top covered with a lid 2. The container 1 has an outlet pipe 4 for an activated fuel on its bottom, and a screen is set on the upper end of the pipe 4. An inlet pipe 3 for fuel penetrates through the lid 2 and extends to the vicinity of the bottom wall 1b. A liquid fuel 7 (e.g. heavy oil) injected into the container 1 is subjected to the so-called activation by contact under agitation with a granular solid 6 (ceramic granules which can radiate far-infrared energy) and discharged gradually from the outlet pipe 4. This treatment can improve the flow and combustibility of the fuel and heighten its heating value. Examples of the solids include an infrared radiator of a wavelength peak of 3-15mum, a single or compound energy radiator which radiates alpha, beta or gamma-rays of an intensity of 1000CMP or above, and a magnetic substance which radiates a magnetic flux of a flux density of 300G or above.

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【産業上の利用分野】本発明は液体燃料の活性化処理方
法の改良に関するものである。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to an improvement in a liquid fuel activation treatment method.

【0002】[0002]

【従来の技術】重油や軽油等の低質燃料の燃焼性能や発
熱量を高めるには、通常重油等を燃焼前に加熱したり、
或いは重油等に若干の高質燃料を添加したりする方法が
採用されている。また、ガソリン等の高級燃料に於いて
は、少量の活性剤をこれに混合することにより、その燃
焼性能の向上が図られている。しかし、前記従前の方法
は、何れも液体燃料内へ他の物質を添加するものであ
り、液体燃料そのものの改質を図るものでない。
2. Description of the Related Art In order to improve the combustion performance and heat generation amount of low-quality fuels such as heavy oil and light oil, it is common to heat heavy oil before combustion,
Alternatively, a method of adding some high quality fuel to heavy oil or the like is adopted. In addition, in high-grade fuels such as gasoline, the combustion performance is improved by mixing a small amount of activator with it. However, each of the above-mentioned conventional methods adds another substance to the liquid fuel, and does not attempt to reform the liquid fuel itself.

【0003】一方、近年強力な磁場や電場内へ重油や軽
油等を通し、重油や軽油の構成分子や原子のエネルギー
レベルを高めることにより燃料を改質し、その発熱量等
を増加するようにした燃料の所謂活性化処理方法が開発
されている。しかし、従前の活性化処理方法は、何れも
大容量の電源設備や活性化処理装置を必要とする上、電
力消費量が増大し、燃料コストの高騰を招くと云う問題
がある。また、電場や磁場内を液体燃料を流通させる方
法に於いては、流通する液体燃料の全体を均等に、しか
も高能率で活性化処理することが困難であり、液体燃料
を高能率で連続処理し難いと云う難点がある。
On the other hand, in recent years, heavy oil or light oil has been passed through a strong magnetic field or electric field to increase the energy level of the constituent molecules or atoms of the heavy oil or light oil so as to reform the fuel and increase the calorific value thereof. So-called activation treatment methods for such fuels have been developed. However, each of the conventional activation treatment methods requires a large-capacity power supply facility and an activation treatment device, and also has a problem that power consumption increases and fuel cost rises. Further, in the method of circulating the liquid fuel in the electric field or magnetic field, it is difficult to uniformly and highly efficiently activate the entire circulating liquid fuel, and the liquid fuel is continuously treated with high efficiency. It is difficult to do.

【0004】[0004]

【発明が解決しようとする課題】本件発明は、従前の液
体燃料の活性化処理方法に於ける上述の如き問題、即ち
大容量の電源設備や処理装置を必要とし、簡便にしか
も能率良く液体燃料の活性化処理が出来ないこと、液
体燃料の活性化処理に要する消費エネルギーが増大し、
燃料コストが上昇すること、等の問題を解決せんとする
ものであり、極く少量の電力エネルギー消費でもって高
能率で簡便に、しかも高度に液体燃料を活性化処理でき
るようにした処理方法を提供するものである。
DISCLOSURE OF THE INVENTION The present invention has the above-mentioned problems in the conventional liquid fuel activation treatment method, that is, requires a large-capacity power supply facility and a treatment device, and is simple and efficient. Inability to perform the activation process of, the energy consumption required for the activation process of the liquid fuel increases,
It is intended to solve problems such as increase in fuel cost, and a treatment method that enables highly efficient and easy liquid fuel activation treatment with a very small amount of power energy consumption. Is provided.

【0005】[0005]

【課題を解決するための手段】本件発明は、エネルギー
放射体から成る粒状固体を容器本体内へ封入すると共
に、当該容器本体内へ液体燃料を圧送して液体燃料と粒
状固体とを接触流動させ、前記両者が接触流動する間に
粒状固体からの放射エネルギーを液体燃料内へ吸収させ
ることを発明の基本構成とするものである。
According to the present invention, a granular solid composed of an energy radiator is enclosed in a container body, and liquid fuel is pressure-fed into the container body so that the liquid fuel and the granular solid are brought into contact flow. It is a basic constitution of the invention that the radiant energy from the particulate solid is absorbed into the liquid fuel during the contact flow between the two.

【0006】[0006]

【作用】燃料導入管から容器本体内へ噴出された燃料
は、底壁へ衝突して反転し、上方へ向けて流動する。ま
た、燃料の衝突反転によって容器本体内の粒状固体に衝
撃力が与えられ、これが拡散されて燃料と混合される。
両者が容器本体内を流動する間に、燃料と粒状固体とが
十分に接触し、粒状固体からの放射エネルギーが燃料内
へ吸収されて燃料が活性化される。粒状固体と十分に接
触流動した混合体中の燃料は、スクリーンを通して流体
導出管から容器本体外へ排出されて行く。本発明に於い
ては、封入された粒状固体の全量が燃料によって流動さ
れるため、粒状固体の全部が燃料の活性化処理に活用さ
れる。また、粒状固体と燃料とが流動し乍ら相当長時間
に亘って直に接触をするため、粒状固体からの放射エネ
ルギーが燃料内へ効率よく吸収され、燃料が高度に活性
化処理されることになる。
The fuel ejected from the fuel introducing pipe into the container body collides with the bottom wall, is inverted, and flows upward. Further, due to the collision reversal of the fuel, an impact force is applied to the granular solid in the container body, which is diffused and mixed with the fuel.
While both flow in the container body, the fuel and the particulate solid sufficiently come into contact with each other, the radiant energy from the particulate solid is absorbed into the fuel, and the fuel is activated. The fuel in the mixture that has sufficiently flowed in contact with the particulate solid is discharged from the fluid discharge pipe to the outside of the container body through the screen. In the present invention, the entire amount of the encapsulated granular solids is made to flow by the fuel, so that the entire granular solids are utilized for the fuel activation treatment. Further, since the granular solid and the fuel flow and come into direct contact with each other for a considerably long time, the radiant energy from the granular solid is efficiently absorbed into the fuel, and the fuel is highly activated. become.

【0007】[0007]

【実施例】以下、図面に基づいて本発明の実施例を説明
する。図1は本発明による液体燃料の活性化処理の説明
図であり、図に於いて1は容器本体、2は蓋体、3は導
入管、4は導出管、5はスクリーン、6は粒状固体、7
は液体燃料(重油)、8は処理済み燃料である。前記容
器本体1は、ステンレス鋼により円筒形に形成されてお
り、その上方部は蓋体2により閉鎖されている。また、
当該容器本体1の底面には処理済み燃料8の導出管4が
取り付けられており、その先端にはスクリーン5が設け
られている。更に、前記蓋体2には燃料導入管3がこれ
を貫通して固着されており、導入管3の下端部3aは容
器本体1の底壁1bの近傍にまで達している。
Embodiments of the present invention will be described below with reference to the drawings. FIG. 1 is an explanatory view of a liquid fuel activation process according to the present invention, in which 1 is a container body, 2 is a lid, 3 is an introducing pipe, 4 is an outlet pipe, 5 is a screen, and 6 is a granular solid. , 7
Is a liquid fuel (heavy oil), and 8 is a treated fuel. The container body 1 is formed of stainless steel into a cylindrical shape, and an upper portion thereof is closed by a lid 2. Also,
A lead-out pipe 4 for the treated fuel 8 is attached to the bottom surface of the container body 1, and a screen 5 is provided at the tip thereof. Further, a fuel introduction pipe 3 is fixed to the lid 2 so as to penetrate therethrough, and a lower end portion 3a of the introduction pipe 3 reaches near the bottom wall 1b of the container body 1.

【0008】前記粒状固体6としては、遠赤外線エネル
ギーを放射するセラミック粒子(粒径2.0mm〜10.
0mm)が使用されており、容器本体1内へ圧入された
液体燃料7は、当該セラミック粒子6と接触流動するこ
とにより所謂活性化処理を受け、燃料導出管4から順次
取り出されて行く。尚、前記容器本体1内へ充填される
粒状固体6の量は、通常容器内容積の30〜80%程度
である。また、本実施例ではセラミック粒子として、常
温に於いて波長が3〜15μmの範囲にピーク値をもつ
エネルギーを放射する所謂遠赤外線放射体が使用されて
おり、軽油や重油等の液体燃料7を当該セラミック粒子
を用いて活性化処理することにより、燃料の流動性が向
上すると共に燃焼性も向上して発熱量が増し、その結果
大幅な燃料の削減が可能となる(軽油を活性化処理した
場合には、同一燃焼装置に於いて、約10%程度の発熱
量の増加が可能なことが確認されている)。
[0008] As the particulate solid 6, the ceramic particles (particle size 2 to radiate far infrared energy. 0mm~10.
0 mm) is used, and the liquid fuel 7 press-fitted into the container body 1 is subjected to a so-called activation treatment by being brought into contact with the ceramic particles 6 to flow, and is sequentially taken out from the fuel outlet pipe 4. The amount of the particulate solid 6 filled in the container body 1 is usually about 30 to 80% of the internal volume of the container. Further, in this embodiment, a so-called far-infrared radiator that radiates energy having a peak value in the wavelength range of 3 to 15 μm at room temperature is used as the ceramic particles, and the liquid fuel 7 such as light oil or heavy oil is used. By performing activation treatment using the ceramic particles, the fluidity of the fuel is improved, the combustibility is also improved, and the calorific value is increased. As a result, it is possible to significantly reduce the fuel (light oil is activated. In this case, it has been confirmed that the amount of heat generation can be increased by about 10% in the same combustion device).

【0009】前記軽油や重油の活性化は「重油等が外部
からエネルギーを吸収し、重油等の構成分子若しくは構
成原子の振動が活発になっている状態を云う」と一般に
説明されており、内部に含有される炭化水素等の各種有
機物質の固有振動数に近い波長のエネルギーを照射する
と、照射エネルギーが効率よく物質内へ吸収され、重油
等が活性化されることになる。また、照射エネルギーが
吸収されて重油等が活性化されると、物理的には内部に
含有されている水分の分子が水素イオンH+と水酸イオ
ンOH-に解離したり、炭化水素が炭素と水素に解離し
たり、或いは外部から酸素等の気体分子を取り込む力が
増加(例えば溶存酸素の増加)したりし、燃焼性が向上
してより大きな発熱量を得ることが出来る。尚、重油等
の活性化に関する理論的な解析は未だ十分に行われてい
ないが、同一条件下で燃料を燃焼させた場合には、本実
施例により活性化処理した重油の方が前述の通り約10
%程度発熱量が増加することが確認されている。
The activation of light oil or heavy oil is generally described as "a state in which heavy oil or the like absorbs energy from the outside and the vibration of constituent molecules or constituent atoms of the heavy oil or the like is active". When energy with a wavelength close to the natural frequency of various organic substances such as hydrocarbons contained in is irradiated, the irradiation energy is efficiently absorbed into the substance, and heavy oil is activated. Further, when the irradiation energy is absorbed and the heavy oil or the like is activated, physically the water molecules contained therein are dissociated into hydrogen ions H + and hydroxide ions OH , and the hydrocarbons are carbonized. And dissociate into hydrogen, or the force of taking in gas molecules such as oxygen from the outside increases (for example, the amount of dissolved oxygen increases), the combustibility is improved, and a larger heat generation amount can be obtained. It should be noted that although theoretical analysis on activation of heavy oil and the like has not been sufficiently performed, when the fuel is burned under the same conditions, the heavy oil activated according to the present example is as described above. About 10
It has been confirmed that the calorific value increases by about%.

【0010】次に、本発明による液体燃料の活性化処理
方法を例に挙げて説明する。処理に際しては、先ず、容
器本体1内へセラミック粒子(粒径約5mmφ)の粒状
固体6を所定量(容器内容積の約30〜80%の容積率
となるだけの粒状固体)だけ封入したあと、蓋体2によ
り容器本体1の上方開口を密封する。次に、導入管3よ
り容器本体1内へ液体燃料(重油)7を圧送(圧力→約
.5〜7Kg/cm2)し、軸線方向に容器本体の底壁
1bに向かって噴出する。噴出された重油7は、底面1
bへ衝突して反転する。これにより、内部に充填した粒
状固体6も衝撃を受け、容器本体1内に拡散されて重油
7と十分に混合接触する。一方、反転して上方へ向かっ
た重油7は、粒状固体6と相互に接触しつつ流動し、こ
の間に重油7が粒状固体6からの放射エネルギーを吸収
して、所謂活性化処理を受けることになる。セラミック
粒子6との接触循環流動によって活性化処理された重油
8は、順次流体導出管4を通して排出されて行く。ま
た、容器本体1内のセラミック粒子6は、スクリーン5
によって外部への流出が阻止されると共に、スクリーン
外表面へ到達したセラミック粒子6は、流動する旋回流
によってスクリーン外表面から引き離される。
Next, the liquid fuel activation treatment method according to the present invention will be described as an example. In the processing, first, a predetermined amount (granular solids having a volume ratio of about 30 to 80% of the inner volume of the container) of granular solids 6 of ceramic particles (particle diameter of about 5 mmφ) is enclosed in the container body 1 and thereafter. The lid 2 closes the upper opening of the container body 1. Then, the liquid fuel (heavy oil) 7 to inlet pipe 3 from the container body 1 and pumped (pressure → about 0. 5~7Kg / cm 2), ejected toward the bottom wall 1b of the container body in the axial direction. The spouted heavy oil 7 has a bottom surface 1
It collides with b and reverses. As a result, the granular solid 6 filled inside is also impacted, diffused in the container body 1 and sufficiently mixed and contacted with the heavy oil 7. On the other hand, the heavy oil 7 which has been inverted and directed upward flows while contacting with the granular solid 6 while the heavy oil 7 absorbs radiant energy from the granular solid 6 and undergoes so-called activation treatment. Become. The heavy oil 8 activated by the contact circulation flow with the ceramic particles 6 is sequentially discharged through the fluid outlet pipe 4. In addition, the ceramic particles 6 in the container body 1 are
As a result, the ceramic particles 6 that have reached the outer surface of the screen are separated from the outer surface of the screen by the flowing swirling flow.

【0011】前記第1実施例においては、粒状固体とし
て波長3μm〜15μmの間に放射エネルギーのピーク
値を有するセラミック製遠赤外線放射体を利用している
が、これに替えてトリウム等のγ線やβ線、α線を放射
する物質を粒状固体として使用することも可能である。
この場合、前記粒状固体6の放射エネルギーは、100
0CPM以上の強度を有することが望ましく、実験によ
れば、前記遠赤外線放射体の場合とほぼ同程度に液体燃
料(重油)が活性化処理される。
In the first embodiment, a far infrared radiator made of ceramics having a peak value of radiant energy in the wavelength range of 3 μm to 15 μm is used as the granular solid, but instead of this, gamma rays such as thorium are used. It is also possible to use a substance that emits β-rays or α-rays as a granular solid.
In this case, the radiant energy of the granular solid 6 is 100
It is desirable that the liquid fuel (heavy oil) has an intensity of 0 CPM or more. According to the experiment, the liquid fuel (heavy oil) is activated to the same extent as in the case of the far infrared radiator.

【0012】また、粒状固体6を電気分極特性を備えた
電束の放射体、例えば電気石(トリマリン)から成る粒
状固体としてもよい。この場合には粒状固体6から放射
される電界エネルギーが液体燃料内へ吸収され、その活
性化が行われる。
Further, the granular solid 6 may be a radiator of an electric flux having an electric polarization characteristic, for example, a granular solid made of tourmaline. In this case, the electric field energy radiated from the granular solid 6 is absorbed in the liquid fuel and activated.

【0013】更に、前記粒状固体6を磁束を放射する磁
性材料例えば磁化された鉄鉱石等から形成してもよい。
この場合、粒状固体6の磁化の強さは、固体6から放射
される磁束の磁束密度が約300ガウス以上であること
が望ましく、粒状固体6から放射される所謂磁気エネル
ギーにより、液体燃料が活性化される。
Furthermore, the granular solid 6 may be formed of a magnetic material that radiates a magnetic flux, such as magnetized iron ore.
In this case, the strength of magnetization of the granular solid 6 is preferably such that the magnetic flux density of the magnetic flux emitted from the solid 6 is about 300 gauss or more, and the so-called magnetic energy emitted from the granular solid 6 activates the liquid fuel. Be converted.

【0014】一方、前記第1実施例に於いては、液体燃
料7として重油を活性化処理したが、軽油や灯油、ガソ
リン、ケロシン等であっても、重油とほぼ同程度に燃焼
特性を向上させることができ、約10〜15%程度の発
熱量の増加が確認されている。また、本実施例では、図
1に示す如き形状の処理装置を使用しているが、使用す
る処理装置の構造等は如何なるものであってもよい。
On the other hand, in the first embodiment, the heavy oil was activated as the liquid fuel 7. However, even with light oil, kerosene, gasoline, kerosene, etc., the combustion characteristics are improved to almost the same level as heavy oil. It has been confirmed that the amount of heat generation is increased by about 10 to 15%. Further, in the present embodiment, the processing device having the shape shown in FIG. 1 is used, but the structure of the processing device to be used may be any structure.

【0015】[0015]

【発明の効果】本件発明に於いては、容器本体1内にエ
ネルギー放射体である粒状固体6を充填し、容器本体1
内で粒状固体6と液体燃料7とを直に接触流動させるこ
とにより、液体燃料7を活性化するようにしている。そ
の結果、従前の液体燃料の活性化方法のように大型の活
性化装置や大容量のエネルギー源を別途に必要とせず、
粒状固体6の有する固有のエネルギーを用いて連続的に
液体燃料7を活性化することができ、消費エネルギーの
削減が可能となる。また、粒状固体6と液体燃料7とを
直に接触流動させるため、液体燃料7内への放射エネル
ギーの吸収が効率よく行え、液体燃料7を効率よく且つ
高度に活性化することが出来る。本発明は上述の通り、
優れた実用的効用を奏するものである。
According to the present invention, the container body 1 is filled with the granular solid 6 which is an energy radiator, and
The liquid fuel 7 is activated by directly contacting and flowing the granular solid 6 and the liquid fuel 7 therein. As a result, unlike the conventional liquid fuel activation method, it does not require a large-scale activation device or a large-capacity energy source separately,
The liquid fuel 7 can be continuously activated by using the unique energy of the granular solid 6, and the energy consumption can be reduced. Further, since the granular solid 6 and the liquid fuel 7 are directly brought into contact with each other to flow, the radiant energy can be efficiently absorbed in the liquid fuel 7, and the liquid fuel 7 can be efficiently and highly activated. The present invention is as described above.
It has excellent practical utility.

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

【図1】本発明による液体燃料の活性化処理の説明図で
ある。
FIG. 1 is an explanatory diagram of a liquid fuel activation process according to the present invention.

【符号の説明】[Explanation of symbols]

1は容器本体、2は蓋体、3は流体導入管、4は流体導
出管、5はスクリーン、6は粒状固体、7は液体燃料、
8は処理済み燃料。
1 is a container main body, 2 is a lid, 3 is a fluid inlet pipe, 4 is a fluid outlet pipe, 5 is a screen, 6 is a granular solid, 7 is liquid fuel,
8 is treated fuel.

Claims (6)

【特許請求の範囲】[Claims] 【請求項1】 エネルギー放射体から成る粒状固体を容
器本体内へ封入すると共に、当該容器本体内へ液体燃料
を圧送して液体燃料と粒状固体とを接触流動させ、前記
両者が接触流動する間に粒状固体からの放射エネルギー
を液体燃料内へ吸収させることを特徴とする液体燃料の
活性化処理方法。
1. A granular solid comprising an energy radiator is enclosed in a container body, and liquid fuel is pumped into the container body to bring the liquid fuel and the granular solid into contact flow, and while the two are in contact flow. A method for activating a liquid fuel, characterized in that the radiant energy from the granular solid is absorbed into the liquid fuel.
【請求項2】 粒状固体を、波長のピーク値が3〜15
μmの範囲内にある赤外線放射体とした請求項1に記載
の液体燃料の活性化処理方法。
2. A granular solid having a wavelength peak value of 3 to 15
The liquid fuel activation treatment method according to claim 1, wherein the infrared radiator is in the range of μm.
【請求項3】 粒状固体を、1000CPM以上の強度
を有するα線、β線、γ線の単一若しくは複合のエネル
ギー放射体とした請求項1に記載の液体燃料の活性化処
理方法。
3. The liquid fuel activation treatment method according to claim 1, wherein the granular solid is an α-ray, β-ray, or γ-ray single or complex energy radiator having an intensity of 1000 CPM or more.
【請求項4】 粒状固体を、磁束密度が300ガウス以
上の磁束を放射する磁性体とした請求項1に記載の液体
燃料の活性化処理方法。
4. The liquid fuel activation treatment method according to claim 1, wherein the granular solid is a magnetic material that radiates a magnetic flux having a magnetic flux density of 300 gauss or more.
【請求項5】 粒状固体を、電気分極性を備えた電束の
放射体とした請求項1に記載の液体燃料の活性化処理方
法。
5. The liquid fuel activation treatment method according to claim 1, wherein the granular solid is an electric flux radiator having electric polarizability.
【請求項6】 液体燃料を、重油、軽油、灯油、ガソリ
ン、ケロシンの何れか一種又はその混合体とした請求項
1に記載の液体燃料の活性化処理方法。
6. The method for activating treatment of liquid fuel according to claim 1, wherein the liquid fuel is any one of heavy oil, light oil, kerosene, gasoline, kerosene or a mixture thereof.
JP28400991A 1991-10-03 1991-10-03 Activation of liquid fuel Pending JPH0598272A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP28400991A JPH0598272A (en) 1991-10-03 1991-10-03 Activation of liquid fuel

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP28400991A JPH0598272A (en) 1991-10-03 1991-10-03 Activation of liquid fuel

Publications (1)

Publication Number Publication Date
JPH0598272A true JPH0598272A (en) 1993-04-20

Family

ID=17673118

Family Applications (1)

Application Number Title Priority Date Filing Date
JP28400991A Pending JPH0598272A (en) 1991-10-03 1991-10-03 Activation of liquid fuel

Country Status (1)

Country Link
JP (1) JPH0598272A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2008072619A1 (en) * 2006-12-11 2008-06-19 Opt Creation, Inc. Apparatus and process for production of nanobubble liquid
JP2009191261A (en) * 2008-01-15 2009-08-27 Yoshisuke Nagao Method for producing emulsion fuel

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2008072619A1 (en) * 2006-12-11 2008-06-19 Opt Creation, Inc. Apparatus and process for production of nanobubble liquid
US9416329B2 (en) 2006-12-11 2016-08-16 Opt Creation, Inc. Apparatus and process for production of nanobubble liquid
JP2009191261A (en) * 2008-01-15 2009-08-27 Yoshisuke Nagao Method for producing emulsion fuel

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