JPH04171262A - Fuel reforming method and filter device - Google Patents
Fuel reforming method and filter deviceInfo
- Publication number
- JPH04171262A JPH04171262A JP2294830A JP29483090A JPH04171262A JP H04171262 A JPH04171262 A JP H04171262A JP 2294830 A JP2294830 A JP 2294830A JP 29483090 A JP29483090 A JP 29483090A JP H04171262 A JPH04171262 A JP H04171262A
- Authority
- JP
- Japan
- Prior art keywords
- fuel
- gasoline
- filter device
- ceramic
- water
- 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
Links
- 239000000446 fuel Substances 0.000 title claims abstract description 38
- 238000000034 method Methods 0.000 title claims description 11
- 238000002407 reforming Methods 0.000 title claims description 10
- 239000000919 ceramic Substances 0.000 claims abstract description 27
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 22
- 239000004215 Carbon black (E152) Substances 0.000 claims abstract description 9
- 230000003213 activating effect Effects 0.000 claims abstract description 9
- 229930195733 hydrocarbon Natural products 0.000 claims abstract description 9
- 150000002430 hydrocarbons Chemical class 0.000 claims abstract description 9
- 238000001914 filtration Methods 0.000 claims description 7
- 230000009467 reduction Effects 0.000 abstract description 5
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 abstract description 3
- 229910052799 carbon Inorganic materials 0.000 abstract description 3
- 230000006866 deterioration Effects 0.000 abstract description 2
- 230000006872 improvement Effects 0.000 abstract description 2
- 230000002265 prevention Effects 0.000 abstract description 2
- 230000000694 effects Effects 0.000 description 10
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 description 8
- 239000000843 powder Substances 0.000 description 7
- 230000005684 electric field Effects 0.000 description 5
- 239000000463 material Substances 0.000 description 5
- 238000002485 combustion reaction Methods 0.000 description 4
- 239000007789 gas Substances 0.000 description 4
- 239000002245 particle Substances 0.000 description 4
- 239000000377 silicon dioxide Substances 0.000 description 4
- ZAMOUSCENKQFHK-UHFFFAOYSA-N Chlorine atom Chemical compound [Cl] ZAMOUSCENKQFHK-UHFFFAOYSA-N 0.000 description 3
- 230000009471 action Effects 0.000 description 3
- PNEYBMLMFCGWSK-UHFFFAOYSA-N aluminium oxide Inorganic materials [O-2].[O-2].[O-2].[Al+3].[Al+3] PNEYBMLMFCGWSK-UHFFFAOYSA-N 0.000 description 3
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 3
- 239000000460 chlorine Substances 0.000 description 3
- 229910052801 chlorine Inorganic materials 0.000 description 3
- 238000002156 mixing Methods 0.000 description 3
- 239000001301 oxygen Substances 0.000 description 3
- 229910052760 oxygen Inorganic materials 0.000 description 3
- 238000000926 separation method Methods 0.000 description 3
- 239000011230 binding agent Substances 0.000 description 2
- 238000006243 chemical reaction Methods 0.000 description 2
- 239000013078 crystal Substances 0.000 description 2
- 238000010586 diagram Methods 0.000 description 2
- 238000003411 electrode reaction Methods 0.000 description 2
- 238000004070 electrodeposition Methods 0.000 description 2
- 238000005516 engineering process Methods 0.000 description 2
- 239000008187 granular material Substances 0.000 description 2
- 229910001385 heavy metal Inorganic materials 0.000 description 2
- 150000002500 ions Chemical class 0.000 description 2
- 230000007794 irritation Effects 0.000 description 2
- 238000004519 manufacturing process Methods 0.000 description 2
- 230000004048 modification Effects 0.000 description 2
- 238000012986 modification Methods 0.000 description 2
- 230000003647 oxidation Effects 0.000 description 2
- 238000007254 oxidation reaction Methods 0.000 description 2
- 229920002635 polyurethane Polymers 0.000 description 2
- 239000004814 polyurethane Substances 0.000 description 2
- 238000005245 sintering Methods 0.000 description 2
- 238000005507 spraying Methods 0.000 description 2
- 229940070527 tourmaline Drugs 0.000 description 2
- 229910052613 tourmaline Inorganic materials 0.000 description 2
- 239000011032 tourmaline Substances 0.000 description 2
- 102000004190 Enzymes Human genes 0.000 description 1
- 108090000790 Enzymes Proteins 0.000 description 1
- 206010015946 Eye irritation Diseases 0.000 description 1
- 230000002378 acidificating effect Effects 0.000 description 1
- 238000005054 agglomeration Methods 0.000 description 1
- 230000002776 aggregation Effects 0.000 description 1
- 210000003484 anatomy Anatomy 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 238000004061 bleaching Methods 0.000 description 1
- 150000001768 cations Chemical class 0.000 description 1
- 239000013043 chemical agent Substances 0.000 description 1
- 239000003795 chemical substances by application Substances 0.000 description 1
- 238000004132 cross linking Methods 0.000 description 1
- 230000006378 damage Effects 0.000 description 1
- 230000005611 electricity Effects 0.000 description 1
- 239000002659 electrodeposit Substances 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
- 238000002474 experimental method Methods 0.000 description 1
- 231100000013 eye irritation Toxicity 0.000 description 1
- 238000011049 filling Methods 0.000 description 1
- 239000010419 fine particle Substances 0.000 description 1
- 239000001257 hydrogen Substances 0.000 description 1
- 229910052739 hydrogen Inorganic materials 0.000 description 1
- 125000004435 hydrogen atom Chemical class [H]* 0.000 description 1
- 230000007062 hydrolysis Effects 0.000 description 1
- 238000006460 hydrolysis reaction Methods 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-M hydroxide Chemical class [OH-] XLYOFNOQVPJJNP-UHFFFAOYSA-M 0.000 description 1
- 125000002887 hydroxy group Chemical group [H]O* 0.000 description 1
- -1 hydroxyl ions Chemical class 0.000 description 1
- JEIPFZHSYJVQDO-UHFFFAOYSA-N iron(III) oxide Inorganic materials O=[Fe]O[Fe]=O JEIPFZHSYJVQDO-UHFFFAOYSA-N 0.000 description 1
- 229910052751 metal Inorganic materials 0.000 description 1
- 239000002184 metal Substances 0.000 description 1
- 229910021645 metal ion Inorganic materials 0.000 description 1
- 150000002739 metals Chemical class 0.000 description 1
- 238000006386 neutralization reaction Methods 0.000 description 1
- 229920000642 polymer Polymers 0.000 description 1
- 230000008569 process Effects 0.000 description 1
- 238000010298 pulverizing process Methods 0.000 description 1
- 239000002994 raw material Substances 0.000 description 1
- 238000005096 rolling process Methods 0.000 description 1
- 238000004062 sedimentation Methods 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
- 238000001179 sorption measurement Methods 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 239000004094 surface-active agent Substances 0.000 description 1
- 230000009182 swimming Effects 0.000 description 1
- 230000002195 synergetic effect Effects 0.000 description 1
- 239000008399 tap water Substances 0.000 description 1
- 235000020679 tap water Nutrition 0.000 description 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10L—FUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
- C10L10/00—Use of additives to fuels or fires for particular purposes
- C10L10/02—Use of additives to fuels or fires for particular purposes for reducing smoke development
Landscapes
- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Combustion & Propulsion (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Organic Chemistry (AREA)
- Supplying Secondary Fuel Or The Like To Fuel, Air Or Fuel-Air Mixtures (AREA)
- Filtration Of Liquid (AREA)
Abstract
Description
【発明の詳細な説明】
〔産業上の利用分野〕
本発明は、燃料の改質方法及びフィルター装置に関する
ものである。DETAILED DESCRIPTION OF THE INVENTION [Field of Industrial Application] The present invention relates to a fuel reforming method and a filter device.
最近、自動車等の産業機械からの排ガスが環境破壊の原
因となるということで排ガスiらcot。Recently, exhaust gases from industrial machinery such as automobiles are said to be a cause of environmental destruction.
Co、HC,NOx、SOx等を除去しようとする種々
の提案がなされている。Various proposals have been made to remove Co, HC, NOx, SOx, and the like.
その一つに、ガソリンに強力な磁場と電場を作用させ、
その相乗効果によってガソリンそのものを改質し、ガソ
リンの完全燃焼を実行せしめようとする提案がある。One way is to apply strong magnetic and electric fields to gasoline.
There is a proposal to reform gasoline itself by utilizing this synergistic effect and to achieve complete combustion of gasoline.
しかし、この提案は、実現には電場、磁場が当然に必要
となり、従って、該提案はその分コスト高、複雑になる
とともに効果が不十分であり、−部のマニアが採用して
いるだけである。また、該提案の場合には、自動車のバ
ッテリ一部から電気を取らなければならず、それだけ該
バッテリ一部に負担をかけるという問題も生じる。However, this proposal naturally requires an electric field and a magnetic field to realize it, and therefore it is expensive, complicated, and insufficiently effective, and is only adopted by a few enthusiasts. be. In addition, in the case of this proposal, electricity must be drawn from a portion of the car's battery, which poses a problem of placing a corresponding burden on that portion of the battery.
本発明は、ガソリン等の燃料を完全燃焼し得る燃料に簡
単に改質してしまう燃料の改質方法及びガソリン等の燃
料を濾過すると同時に該燃料を簡単に改質するフィルタ
ー装置を提供することを技術的課題とするものである。The present invention provides a fuel reforming method for easily reforming fuel such as gasoline into a fuel that can be completely combusted, and a filter device for filtering fuel such as gasoline and at the same time easily reforming the fuel. is a technical issue.
添付図面を参照して本発明の詳細な説明する。 The present invention will now be described in detail with reference to the accompanying drawings.
容器Iに水を活性化する性質を有するセラミック2を配
在し、この容器lにガソリン、軽油等の炭化水素系燃料
を通過せしめることで該燃料を改質することを特徴とす
る燃料の改質方法に係るものである。A fuel modification characterized in that a ceramic 2 having a property of activating water is disposed in a container I, and hydrocarbon fuel such as gasoline or light oil is passed through the container I to reform the fuel. This relates to quality methods.
ガソリン、軽油等の炭化水素系燃料を濾過するフィルタ
ー装置3に水を活性化する性質を有するセラミック2を
配在せしめたことを特徴とするフィルター装置に係るも
のである。The present invention relates to a filter device characterized in that a filter device 3 for filtering hydrocarbon fuels such as gasoline and light oil is provided with a ceramic 2 having a property of activating water.
請求項1記載の発明の作用について説明する。 The operation of the invention according to claim 1 will be explained.
炭化水素系燃料は全て(+ )、(−)の電位により安
定した集合体構造となっている。セラミック2がこの集
合体に接解を繰り返すと、このセラミック2が水を活性
化する性質を有する為、集合体であった燃料は(−)帯
電せしめられ、従って、互いに拒否反応を起こして分子
間分離が激化し、よって、該分子は、個々の分子に分解
され、結果的に活性化されることになる。All hydrocarbon fuels have a stable aggregate structure due to (+) and (-) potentials. When ceramic 2 is repeatedly welded to this aggregate, since this ceramic 2 has the property of activating water, the fuel in the aggregate becomes (-) charged, causing a mutual rejection reaction and the molecules The separation between molecules becomes intensified and the molecule is thus broken down into individual molecules and consequently becomes activated.
燃料が個々に分解せしめられている為、酵素と結合する
面積が飛躍的に増大することになり、従って、該燃料の
完全燃焼が実現されることになる。Since the fuel is individually decomposed, the area for binding with enzymes increases dramatically, and complete combustion of the fuel is therefore achieved.
ここでいうセラミック2の性質について説明する。The properties of the ceramic 2 mentioned here will be explained.
水を活性化する性質を有するセラミック2は次の通りで
ある。The ceramic 2 having the property of activating water is as follows.
タウマリン(トルマリン)のような極性結晶構造を持つ
セラミック2はどんなに細かく砕いても結晶両端の表面
に分極帯電する為かかる結晶体を含む電気石など(電気
石と同様な性能を有する永久電極を持つものならどんな
ものでも良い)のセラミック2を原料とし、一定の誘電
特性を持つアルミナ、シリカと混合・焼結して製造した
セラミック粒体、セラミック粉体は表面の無数の微小電
極による水分子との間に生ずる電極反応により水を活性
化する性質を有する。Ceramic 2, which has a polar crystal structure such as taumarine (tourmaline), is polarized and charged on the surface of both ends of the crystal no matter how finely it is crushed. Ceramic granules and ceramic powders are produced by mixing and sintering ceramic 2 with alumina and silica, which have certain dielectric properties, as a raw material. It has the property of activating water by the electrode reaction that occurs during the process.
この粉体1粒体の性質を更に詳述すると次の通りである
。The properties of this single grain of powder are as follows.
イ)界面活性作用
粉体、粒体との接触によって水は対象カチオンのない遊
離したOH−イオンの多い[ヒドロキシルイオン水」に
なり、電気化学的に不安定な、活性化した状態になる。(b) Surface active effect Upon contact with powders and granules, water becomes hydroxyl ionized water, which has no target cations and is rich in free OH- ions, becoming electrochemically unstable and activated.
このヒドロキシルイオン(OH”−)は水と固体の界面
で「浸透」 「解膠(コロイド化)」「分散」 「乳化
」や、「非付着性」などのいわゆる界面活性作用を示す
。This hydroxyl ion (OH''-) exhibits so-called surfactant effects such as ``penetration'', ``peptization (colloidization)'', ``dispersion'', ``emulsification'', and ``non-adherence'' at the interface between water and solids.
このことは化学薬剤を用いずに界面活性を持つ水ができ
るということである。This means that surface-active water can be produced without using chemical agents.
口)穏やかな酸化、還元作用
水は電解圧以下における電場作用によりHIC)、H+
OH″″に解離する。(1) Mild oxidation, reduction effect Water becomes HIC (HIC), H+ due to the action of an electric field below the electrolytic pressure.
Dissociates into OH″″.
発生する0H−1及び水素によって穏やかな酸化、還元
作用を呈し、漂白効果も発揮する。It exhibits mild oxidation and reduction effects due to the generated 0H-1 and hydrogen, and also exhibits a bleaching effect.
ハ)溶存酸素の増加
ヒドロキシルイオン(OH−)は、活性化した不安定な
状態にある為いずれは酸素と水になり、溶存酸素が増加
する。C) Increase in dissolved oxygen Since hydroxyl ions (OH-) are in an activated and unstable state, they eventually turn into oxygen and water, resulting in an increase in dissolved oxygen.
ニ)塩素刺激緩和作用
塩素は水道水の塩素臭、味、プールの水による目への刺
激、給水配管での赤錆の発生の原因になっている。d) Reducing chlorine irritation Chlorine causes the odor and taste of tap water, eye irritation from swimming pool water, and the formation of red rust in water supply pipes.
粉体3粒体はC1,(分子)の加水分解を促進し、゛塩
素の刺激を大巾に緩和する。The three powder particles promote the hydrolysis of C1 (molecule) and greatly alleviate the irritation caused by chlorine.
ホ)PH中和作用
水が酸性、アルカリ性であるかを問わず、そのPH値を
中性に近付ける作用を有するので、放れ流し公害の緩和
に役立つことになる。e) PH neutralization effect Regardless of whether the water is acidic or alkaline, it has the effect of bringing the pH value closer to neutrality, so it is useful for alleviating pollution caused by effluent.
へ)凝集分離作用
界面活性作用によって解膠、分散された微粒子は大きな
粒子に凝集し、沈降、濾過等で水から分離する必要があ
る。粉体1粒体に含まれているアルミナ、シリカの酸化
物は、中性付近の水ではイオン化しにくいが、粉体。f) Agglomeration and separation action Fine particles peptized and dispersed by surface active action aggregate into large particles, which must be separated from water by sedimentation, filtration, etc. The alumina and silica oxides contained in a single powder particle are difficult to ionize in near-neutral water, but they are powder.
粒体の電極反応により、イオン化やOH架橋等が促進さ
れ、活性シリカポリマーを作り、分離除去が容易となる
。The electrode reaction of the particles promotes ionization, OH crosslinking, etc., creating active silica polymers that can be easily separated and removed.
ト)重金属イオンなどの電着作用
粉体1粒体の表面にある無数の電極は、金属イオンを電
気的に強く吸着してその電極面に電着析出する。G) Electrodeposition of heavy metal ions, etc. The numerous electrodes on the surface of a single powder strongly adsorb metal ions and electrodeposit them on the electrode surface.
特に導電性金属の場合は、強い電着反応を示し、従来の
化学結合や、吸着と違って速やかで強力であり、重金属
イオンなどの除去に役立つことになる。Particularly in the case of conductive metals, they show a strong electrodeposition reaction, which is faster and stronger than conventional chemical bonding or adsorption, and is useful for removing heavy metal ions.
請求項2記載の発明は、上記請求項1記載の発明の作用
にガソリンを濾過する作用が付加されることになる。The invention according to claim 2 adds the function of filtering gasoline to the function of the invention according to claim 1.
図面は、本発明の実施例を図示したもので、第1図は既
存の自動車に設けられているフィルター装置IS内に数
センチメートルの径のセラミック2を充填した場合であ
る。The drawings illustrate an embodiment of the present invention, and FIG. 1 shows a case where a ceramic 2 having a diameter of several centimeters is filled into a filter device IS installed in an existing automobile.
尚、セラミック2の充填量は容量の80%位が望ましい
。Note that the filling amount of the ceramic 2 is preferably about 80% of the capacity.
図中符号4はガソリンを導入する導入管、符号5はガソ
リンをキャブレターに導出する導出管である。In the figure, reference numeral 4 is an inlet pipe for introducing gasoline, and reference numeral 5 is an outlet pipe for leading out gasoline to a carburetor.
第2.3図は、第1図のフィルター材6及び粒状のセラ
ミック2の代わりに軟質ポリウレタンを発泡せしめて互
いに連通ずる空間7を連続的に形成した三次元網状骨格
を有する弾性網状材8に前記と同様の粒状のセラミック
2を微粉化した粉状のセラミック2を付着せしめたもの
をフィルター装置に装着した場合である。Fig. 2.3 shows an elastic reticular material 8 having a three-dimensional reticular skeleton in which a soft polyurethane is foamed instead of the filter material 6 and the granular ceramic 2 in Fig. 1 to continuously form spaces 7 that communicate with each other. This is a case where a filter device is attached with a powdered ceramic 2 obtained by pulverizing the granular ceramic 2 similar to that described above.
この弾性網状材8としては、市販されている株式会社プ
リジストン製の[エバーライトSFJを用い、この[エ
バーライトSFJをバインダー(ガソリン等に溶けない
バインダーを用いる。)に含浸し、その後粉状のセラミ
ック2を吹き付は付着して該実施品を形成する。As the elastic network material 8, commercially available Everlite SFJ manufactured by Prigiston Co., Ltd. is used, and the Everlite SFJ is impregnated with a binder (a binder that is insoluble in gasoline, etc.), and then powdered Ceramic 2 is deposited by spraying to form the embodiment.
粉状のセラミック2は0.3μlI〜0.5μlのアル
ミナ、シリカと3μl程度の電気石とを混合焼結して1
0μM〜20μm程度に形成したものを用いる。Powdered ceramic 2 is prepared by mixing and sintering 0.3 μl to 0.5 μl of alumina, silica, and about 3 μl of tourmaline.
A material formed to have a thickness of about 0 μM to 20 μm is used.
尚、粉状のセラミック2の付着は、上記した吹き付は手
段の他、「エバーライトSFJを製造する段階において
、溶融状態のポリウレタンに粉状のセラミック2を混入
せしめる手段を用いても良い。In addition to the above-mentioned spraying method, the powdered ceramic 2 may be attached by a method of mixing the powdered ceramic 2 into molten polyurethane at the stage of manufacturing Everlite SFJ.
以上の構造のフィルター 装置3を自動車に装着すると
、ガソリンは該フィルター装置3によって濾過(浄化)
せしめられることは勿論、ガソリンが改質され、燃費の
飛躍的な向上(実験の結果10%近いガソリンの消費料
軽減が確認されている。)、カーボンの、発生の激減、
排ガスのクリーン化、エンジン馬力の向上、オイル劣化
の防止等が実現されることになる。□
以上のことは、排ガスを分析し、カーボン、NOx、C
Ot、HC,CO,SOx等が減少していることにより
確認済である。When the filter device 3 with the above structure is installed in a car, gasoline is filtered (purified) by the filter device 3.
Of course, gasoline has been reformed, resulting in a dramatic improvement in fuel efficiency (experiments have confirmed a nearly 10% reduction in gasoline consumption), a drastic reduction in carbon emissions,
This will result in cleaner exhaust gas, improved engine horsepower, and prevention of oil deterioration. □ The above is based on analyzing exhaust gas and detecting carbon, NOx, and C.
This has been confirmed by the decrease in Ot, HC, CO, SOx, etc.
このように、実施例は、燃料部に磁場や電場を作用させ
ることで燃焼効率を高めようとする従来技術とは異なり
、磁場、電場を必要としない簡単な手段により燃焼効率
を高めることが可能となるものである。In this way, unlike the conventional technology that attempts to increase combustion efficiency by applying a magnetic field or electric field to the fuel part, the embodiment can increase combustion efficiency by a simple means that does not require a magnetic field or electric field. This is the result.
この実施例が呈する作用効果は、ファンデヴアール(分
子内引力)理論によって基礎づけられているものである
。The effects exhibited by this embodiment are based on the Van de Vouard (intramolecular attraction) theory.
本発明は上述のようにしたから簡単に燃料の改質を実現
し得る燃料の改質方法及び燃料を簡単に改質し且つフィ
ルター作用も十分発揮するフィルター装置を提供するこ
とになる。As described above, the present invention provides a method for reforming fuel that can easily reform fuel, and a filter device that can easily reform fuel and exhibit a sufficient filtering effect.
図面は本発明の一実施例を示すもので、第1図は本発明
の使用状態を示す説明図、第2図は本発明の使用状態を
示す別例の説明図、第3図は本発明のフィルター材の一
部を拡大した説明斜視図である。
1・・・容器、2・・・セラミック、3・・・フィルタ
ー装置。
平成 2年lθ月31日
出願人 平 澤 信 夫
代理人 吉 井 昭 栄
9〜74つ
夕′
)Z嶺
7りj
平成 3年 2月23[1
■ 事件の表示
平成 2年 特 願 第294830号2 発明の名称
燃料の改τ1方法及びフィルター装置
ソ
5 桶jオ′命名のに1例 平成 年 月
ト−」6 袖−IF−の対蓼・11、明細書「国−4\
1f許請求の範囲丁発明の詳細な説明−JO)’4剖
ニジ、図面「−第1. l’4−1i−”?、い2EN
l−1′l 補i[: j7’>内容 1、別紙の。
勇りツシ、別紙の通り(1−第1図−[[〜第2図1符
号のみ訂正5、[−第3図−1は内容に作中なし)
特許 平2−294830号手続補正書本願に関し、明
細書中丁記の個所を補正する。
記
] 特許請求の範囲を次のように補正する。
「1 容器に水をP性化する性質を有するセラミックを
配在し、この容器にカッリン、軽油等の炭化水素系燃料
を通過せし7zろることて該燃料を活性化さ第1た燃料
に改質することを特徴とする燃料の改質方法。
2 ガソリン、軽油等の炭化水素系燃料を濾過するフィ
ルター装置に水を改質する性質を有オるセラミックを配
在せしめたことを特徴とするフィルター装置。]
2 第3頁第1行目から第5行目の「容器]−に・・・
係るものて゛ある。」とあるを次のように補正する。
[容器1に水を活性化する性質を有するセラミック2を
配在し、この容器1にガソリン、軽油等の炭化水素系燃
料を通過セし7、めることで該燃料を活性化された燃料
に改質する、ことを特徴とずる燃料の改質方法に係るも
のである。」3 第3頁第15行目から第17行目の「
集合体であった・・・が激化し、」とあるを「集合体で
あった燃料は、分子間分離が激化し、」と補正する。
4 第7頁第15行目の「数センチメートル」とあるを
「数ミリメートル」と補正する。
平成 3年 2月23日
出願人 平 澤 信 夫
代理人 吉 井 昭 栄
さl暮
1ス2嶺
7り、細The drawings show one embodiment of the present invention, and FIG. 1 is an explanatory diagram showing a state of use of the present invention, FIG. 2 is an explanatory diagram of another example of a state of use of the present invention, and FIG. It is an explanatory perspective view which expanded a part of filter material of. 1... Container, 2... Ceramic, 3... Filter device. January 31, 1990 Applicant: Nobuo Hirasawa Attorney: Akira Yoshii 9-74 April 2010 February 23, 1991 [1 ■ Description of the case 1990 Patent Application No. 294830 No. 2 Name of the invention Fuel modification τ1 Method and filter device 5 An example of naming a bucket 1989
To-" 6 Sode-IF- vs. 11, Specification "Country-4\
1f Claims D Detailed Description of the Invention - JO) '4 Anatomy, Drawing "-1.l'4-1i-"? ,i2EN
l-1'l Supplementary i[: j7'>Contents 1. Attachment. Yuritsushi, as shown in the attached sheet (1-Figure 1-[[~Figure 2-1 only the code is corrected 5, [-Figure 3-1 is not included in the content] Patent No. 1994-294830 procedural amendment main application Regarding this, the portions mentioned in the specification will be amended. ] The scope of the claims is amended as follows. 1. A ceramic having the property of converting water into P-type is placed in a container, and a hydrocarbon fuel such as gas oil is passed through the container and the fuel is activated by rolling. 2. A method for reforming fuel, characterized in that a ceramic having the property of reforming water is disposed in a filter device for filtering hydrocarbon fuel such as gasoline and light oil. 2. Container in lines 1 to 5 of page 3...
There are things like that. ” should be corrected as follows. [A ceramic 2 having the property of activating water is placed in the container 1, and a hydrocarbon fuel such as gasoline or light oil is passed through the container 1 to make the fuel activated.] The present invention relates to a method for reforming fuel, which is characterized in that the fuel is reformed to ” 3 Page 3, lines 15 to 17, “
The statement "The fuel, which was an aggregate, became intensified," is corrected to "The fuel, which was an aggregate, intermolecular separation became intensified." 4. Correct the phrase "several centimeters" on page 7, line 15 to "several millimeters." February 23, 1991 Applicant: Nobuo Hirasawa Agent: Akira Yoshii
Claims (1)
在し、この容器にガソリン、軽油等の炭化水素系燃料を
通過せしめることで該燃料を改質することを特徴とする
燃料の改質方法。 2 ガソリン、軽油等の炭化水素系燃料を濾過するフィ
ルター装置に水を活性化する性質を有するセラミックを
配在せしめたことを特徴とするフィルター装置。[Claims] 1. A container is provided with a ceramic having the property of activating water, and hydrocarbon fuel such as gasoline or light oil is passed through the container to reform the fuel. A method for reforming fuel. 2. A filter device for filtering hydrocarbon fuels such as gasoline and light oil, which is characterized by disposing a ceramic having a property of activating water.
Priority Applications (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP2294830A JPH04171262A (en) | 1990-10-31 | 1990-10-31 | Fuel reforming method and filter device |
US07/641,400 US5108618A (en) | 1990-10-30 | 1991-01-15 | Method of and apparatus for modifying fuel |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP2294830A JPH04171262A (en) | 1990-10-31 | 1990-10-31 | Fuel reforming method and filter device |
Publications (1)
Publication Number | Publication Date |
---|---|
JPH04171262A true JPH04171262A (en) | 1992-06-18 |
Family
ID=17812808
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP2294830A Pending JPH04171262A (en) | 1990-10-30 | 1990-10-31 | Fuel reforming method and filter device |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH04171262A (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP1124053A2 (en) * | 2000-02-09 | 2001-08-16 | Nissan Motor Co., Ltd. | Fuel vapor treatment system |
-
1990
- 1990-10-31 JP JP2294830A patent/JPH04171262A/en active Pending
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP1124053A2 (en) * | 2000-02-09 | 2001-08-16 | Nissan Motor Co., Ltd. | Fuel vapor treatment system |
EP1124053A3 (en) * | 2000-02-09 | 2003-01-08 | Nissan Motor Co., Ltd. | Fuel vapor treatment system |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
WO2005021940A1 (en) | Exhaust gas processing method and exhaust gas processing system | |
DE69802906T2 (en) | METHOD FOR THE PHYSICAL-CHEMICAL TREATMENT OF WASTEWATER, IN PARTICULAR OF SURFACE WATER INTENDED FOR CONSUMPTION | |
CN101698523B (en) | Method for applying molded carbon in treatment of industrial waste water by electroflocculation | |
DE19820580B4 (en) | Regenerable diesel exhaust filter | |
JP4114091B2 (en) | Liquid purification device | |
JPH04171262A (en) | Fuel reforming method and filter device | |
Xie et al. | Cation exchange resin supported nanoscale zero-valent iron for removal of phosphorus in rainwater runoff | |
CN108211825B (en) | Metal organic framework composite membrane material and preparation and application thereof | |
CN100480198C (en) | Arsenic comprising groundwater processing method | |
WO2000068153A1 (en) | Apparatus for oxidatively destructing trace injurious substance | |
CN102897956A (en) | Method for treating high-arsenious wastewater | |
Deng et al. | Novel iron-modified chitosan for effective demulsification and oil recovery of emulsified oily wastewater | |
EP3866966A1 (en) | Fluoride removal process | |
GB2272942A (en) | Conditioning hydrocarbon fuel. | |
CN115385493A (en) | Pretreatment purification impurity removal process for uranium-containing fluorine-containing wastewater | |
CN212269731U (en) | Treatment system for sewage of spray tower in automobile paint spraying workshop | |
JPH07136645A (en) | Production of waste water purifying agent | |
KR20210093794A (en) | Manufacturing method of high purity ureasolution | |
CN110697832A (en) | Method for treating antimony-containing wastewater by dielectrophoresis enhanced iron oxide | |
Dahlan et al. | A study on the removal characteristic of zinc ion (Zn2+) from synthetic wastewater using a novel waste-derived siliceous sorbent | |
KR102477125B1 (en) | Material and method for purifying contaminant using natural zeolite pretreated | |
JP3125747U (en) | Liquid processing equipment | |
JPH0957251A (en) | Purifying device for pond water, river water and the like | |
CN209052514U (en) | One kind being suitable for automobile manufacture coating wastewater and regenerates cleaning equipment | |
JPH029876B2 (en) |