WO2000065679A1 - Electric vehicle - Google Patents
Electric vehicle Download PDFInfo
- Publication number
- WO2000065679A1 WO2000065679A1 PCT/JP1999/002235 JP9902235W WO0065679A1 WO 2000065679 A1 WO2000065679 A1 WO 2000065679A1 JP 9902235 W JP9902235 W JP 9902235W WO 0065679 A1 WO0065679 A1 WO 0065679A1
- Authority
- WO
- WIPO (PCT)
- Prior art keywords
- water
- hydrogen
- electric vehicle
- oxygen
- centrifuge
- Prior art date
Links
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 77
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 claims abstract description 36
- 239000001257 hydrogen Substances 0.000 claims abstract description 35
- 229910052739 hydrogen Inorganic materials 0.000 claims abstract description 35
- 239000000446 fuel Substances 0.000 claims abstract description 29
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 claims abstract description 27
- 239000001301 oxygen Substances 0.000 claims abstract description 27
- 229910052760 oxygen Inorganic materials 0.000 claims abstract description 27
- 239000003990 capacitor Substances 0.000 claims abstract description 13
- 239000007788 liquid Substances 0.000 claims abstract description 13
- 239000006182 cathode active material Substances 0.000 claims abstract description 6
- 239000006183 anode active material Substances 0.000 claims abstract description 5
- 239000000956 alloy Substances 0.000 claims description 15
- 229910045601 alloy Inorganic materials 0.000 claims description 15
- 238000010438 heat treatment Methods 0.000 claims description 15
- 238000002347 injection Methods 0.000 claims description 6
- 239000007924 injection Substances 0.000 claims description 6
- 238000005868 electrolysis reaction Methods 0.000 claims description 3
- 239000008236 heating water Substances 0.000 claims description 3
- 238000000926 separation method Methods 0.000 claims description 2
- 238000005507 spraying Methods 0.000 claims 2
- 238000000354 decomposition reaction Methods 0.000 description 7
- 125000004435 hydrogen atom Chemical group [H]* 0.000 description 7
- 125000004430 oxygen atom Chemical group O* 0.000 description 7
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 4
- 229910052799 carbon Inorganic materials 0.000 description 4
- 238000005119 centrifugation Methods 0.000 description 4
- 238000010494 dissociation reaction Methods 0.000 description 4
- 230000005593 dissociations Effects 0.000 description 4
- 238000006243 chemical reaction Methods 0.000 description 3
- 238000000034 method Methods 0.000 description 3
- MWUXSHHQAYIFBG-UHFFFAOYSA-N nitrogen oxide Inorganic materials O=[N] MWUXSHHQAYIFBG-UHFFFAOYSA-N 0.000 description 3
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 description 2
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 description 2
- 238000010586 diagram Methods 0.000 description 2
- 239000007789 gas Substances 0.000 description 2
- MYMOFIZGZYHOMD-UHFFFAOYSA-N Dioxygen Chemical compound O=O MYMOFIZGZYHOMD-UHFFFAOYSA-N 0.000 description 1
- 239000007864 aqueous solution Substances 0.000 description 1
- 230000033228 biological regulation Effects 0.000 description 1
- 238000007664 blowing Methods 0.000 description 1
- 229910002092 carbon dioxide Inorganic materials 0.000 description 1
- 239000001569 carbon dioxide Substances 0.000 description 1
- 239000000919 ceramic Substances 0.000 description 1
- 238000002485 combustion reaction Methods 0.000 description 1
- 230000007423 decrease Effects 0.000 description 1
- 229910001882 dioxygen Inorganic materials 0.000 description 1
- 238000007599 discharging Methods 0.000 description 1
- 239000008151 electrolyte solution Substances 0.000 description 1
- 238000000703 high-speed centrifugation Methods 0.000 description 1
- 150000004678 hydrides Chemical class 0.000 description 1
- 150000002431 hydrogen Chemical class 0.000 description 1
- 239000008188 pellet Substances 0.000 description 1
- 230000001737 promoting effect Effects 0.000 description 1
- 238000012827 research and development Methods 0.000 description 1
- 239000008400 supply water Substances 0.000 description 1
- 230000002195 synergetic effect Effects 0.000 description 1
Classifications
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- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M16/00—Structural combinations of different types of electrochemical generators
- H01M16/003—Structural combinations of different types of electrochemical generators of fuel cells with other electrochemical devices, e.g. capacitors, electrolysers
- H01M16/006—Structural combinations of different types of electrochemical generators of fuel cells with other electrochemical devices, e.g. capacitors, electrolysers of fuel cells with rechargeable batteries
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B60—VEHICLES IN GENERAL
- B60L—PROPULSION OF ELECTRICALLY-PROPELLED VEHICLES; SUPPLYING ELECTRIC POWER FOR AUXILIARY EQUIPMENT OF ELECTRICALLY-PROPELLED VEHICLES; ELECTRODYNAMIC BRAKE SYSTEMS FOR VEHICLES IN GENERAL; MAGNETIC SUSPENSION OR LEVITATION FOR VEHICLES; MONITORING OPERATING VARIABLES OF ELECTRICALLY-PROPELLED VEHICLES; ELECTRIC SAFETY DEVICES FOR ELECTRICALLY-PROPELLED VEHICLES
- B60L58/00—Methods or circuit arrangements for monitoring or controlling batteries or fuel cells, specially adapted for electric vehicles
- B60L58/30—Methods or circuit arrangements for monitoring or controlling batteries or fuel cells, specially adapted for electric vehicles for monitoring or controlling fuel cells
-
- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
- C01B3/00—Hydrogen; Gaseous mixtures containing hydrogen; Separation of hydrogen from mixtures containing it; Purification of hydrogen
- C01B3/02—Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen
- C01B3/04—Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen by decomposition of inorganic compounds, e.g. ammonia
- C01B3/042—Decomposition of water
-
- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M8/00—Fuel cells; Manufacture thereof
- H01M8/06—Combination of fuel cells with means for production of reactants or for treatment of residues
- H01M8/0606—Combination of fuel cells with means for production of reactants or for treatment of residues with means for production of gaseous reactants
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B60—VEHICLES IN GENERAL
- B60K—ARRANGEMENT OR MOUNTING OF PROPULSION UNITS OR OF TRANSMISSIONS IN VEHICLES; ARRANGEMENT OR MOUNTING OF PLURAL DIVERSE PRIME-MOVERS IN VEHICLES; AUXILIARY DRIVES FOR VEHICLES; INSTRUMENTATION OR DASHBOARDS FOR VEHICLES; ARRANGEMENTS IN CONNECTION WITH COOLING, AIR INTAKE, GAS EXHAUST OR FUEL SUPPLY OF PROPULSION UNITS IN VEHICLES
- B60K1/00—Arrangement or mounting of electrical propulsion units
-
- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M2250/00—Fuel cells for particular applications; Specific features of fuel cell system
- H01M2250/20—Fuel cells in motive systems, e.g. vehicle, ship, plane
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E60/00—Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
- Y02E60/10—Energy storage using batteries
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E60/00—Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
- Y02E60/30—Hydrogen technology
- Y02E60/36—Hydrogen production from non-carbon containing sources, e.g. by water electrolysis
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E60/00—Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
- Y02E60/30—Hydrogen technology
- Y02E60/50—Fuel cells
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02T—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO TRANSPORTATION
- Y02T90/00—Enabling technologies or technologies with a potential or indirect contribution to GHG emissions mitigation
- Y02T90/40—Application of hydrogen technology to transportation, e.g. using fuel cells
Definitions
- the present invention relates to an electric vehicle using a fuel cell, and its purpose is to extract a large amount of hydrogen and oxygen from water in a short time and use it as fuel for a fuel cell, thereby enabling long-time operation. It is to provide a practical electric vehicle.
- One example is a fuel cell vehicle that uses hydrogen stored in a hydrogen storage alloy as fuel.
- the hydrogen release process of the hydrogen storage alloy is an endothermic reaction, so the temperature of the hydrogen storage alloy decreases with the release of hydrogen gas.
- the gas could hardly be released and the storage battery could not be charged.
- a method of supplying hydrogen and oxygen obtained by using a water electrolysis device to a fuel cell can be considered, but a small electrolysis device that can be mounted on a vehicle is considered. The equipment could not obtain a large amount of decomposed gas in a short time.
- the present inventor has conducted intensive studies in view of such circumstances, and as a result, has been found that water is separated into hydrogen and oxygen by high-speed centrifugal separation and supplied to a fuel cell, thereby causing the above-described problems of charging and decomposition efficiency. Have been found to be able to solve all of them, and have completed the present invention. Disclosure of the invention
- the invention according to claim 1 is a continuous liquid supply type centrifugal separator in which hydrogen and oxygen are taken out in a separated state by continuously taking water into the inside and rotating at a high speed, and a centrifuge taken out from the centrifuge.
- a fuel cell that generates an electromotive force using hydrogen as an anode active material and oxygen as a cathode active material, an electric motor that rotates by the electromotive force generated from the fuel cell, a storage battery, and a stacked capacitor.
- the electric vehicle is characterized in that the vehicle is driven in accordance with the driving of the electric motor and the surplus electric power at the time of driving the vehicle is charged in the storage battery and the multilayer capacitor.
- the invention according to claim 3 is at least one in which the same poles are arranged to face each other.
- a water molecule cluster decomposing device comprising at least 6 OMG s or more magnets is provided, and water passing through the decomposing device is supplied to the centrifugal separator. Since the electric vehicle is described, the efficiency of water splitting by centrifugation can be increased, and a large amount of hydrogen and oxygen can be obtained in a short time.
- high-pressure water injection means for blowing high-pressure water is provided on an inner wall of the rotary tank of the centrifuge. 5. Since the electric vehicle is of the type described above, the rotation of the rotating tank is assisted by high-pressure water, and the dissociation of water molecules by centrifugal force is promoted by the collision energy.
- FIG. 1 is a schematic configuration diagram of an electric vehicle according to the present invention
- FIG. 2 is a cross-sectional view showing an example of a moisture class decomposition apparatus.
- FIG. 1 is a schematic configuration diagram of an electric vehicle according to the present invention.
- the electric vehicle according to the present invention is a continuous liquid supply type in which hydrogen and oxygen are separated and taken out by continuously taking in water and rotating at high speed.
- a centrifuge 1 a fuel cell 2 that uses hydrogen extracted from the centrifuge 1 as an anode active material, and generates an electromotive force using oxygen as a cathode active material, and is rotated by the electromotive force generated from the fuel cell 2.
- the vehicle is driven by rotating the axle 8 with the driving of the electric motor 3, and the storage battery 4 and the multilayer capacitor 16 are charged with surplus power generated when the vehicle is driven.
- Water (H 2 0) is stored in the storage tank 5, and this water passes through the inside of the pipe 18 having the NiH 2 alloy 17 attached to the inner surface thereof, so that the water contacts the Ni H 2 alloy. Taken out of 18.
- the configuration for bringing water into contact with the NiH 2 alloy is not limited to this.For example, a configuration in which water passes through porous pellets of the NiH 2 alloy, or a configuration in which the NiH 2 alloy is embedded in the storage tank 5 The configuration may be set in advance.
- NiH 2 is an interstitial hydride and has the property of reacting with water and ethanol to generate hydrogen.
- hydrogen and oxygen can be extracted from water by bringing the water into contact with the NiH 2 alloy as described above.
- the heating means 7 and the continuous liquid supply centrifuge 1 By sequentially supplying the heating means 7 and the continuous liquid supply centrifuge 1 to the centrifuge 1, the decomposition of water by NiH 2 is promoted, and a large amount of hydrogen and oxygen can be efficiently obtained in a short time.
- the heating means 7 are sequentially supplied to the continuous liquid feed type centrifugal separator 1 In this case, it is possible to obtain hydrogen and oxygen by dissociating the bond between the oxygen atom and the hydrogen atom of the water molecule by high-speed centrifugation.
- FIG. 2 is a cross-sectional view showing an example of the water molecule class evening decomposition device 6.
- the water molecule cluster decomposing device 6 includes a case body 63 having an inlet 61 and a water outlet 62, and one or more sets (four sets in the illustrated example) provided inside the case body 63. Consists of magnets 6 4.
- the inside of the case body 63 is divided into a plurality of sections by water-filling filters 65, each of which has a pair of permanent magnets 64 of the same polarity (in the example shown, the S pole and the S pole). (S pole) facing each other.
- the water taken out of the storage tank 5 is introduced into the inside of the case body 63 from the water inlet 61, and gradually passes through between the S poles of the permanent magnets 64 disposed in each section.
- the molecular clusters become smaller and are finally extracted from the outlet 62.
- water does not exist as a single molecule (H 20 ), but as a group of several molecules. This molecular population is referred to as a class one.
- water decomposition by centrifugation described later can be further promoted.
- the permanent magnet 64 a permanent magnet of 6 OMGs or more, preferably 100 to 15 OMGs, is used. This is because the use of a magnet of less than 6 OMGs cannot sufficiently reduce the water molecule class.
- the heating means 7 is provided for heating the water taken out from the water molecule cluster decomposing device 6. Although a heating wire heater is shown in the illustrated example, the configuration of the heating means 7 in the present invention is not limited to this, and may be a ceramic heater or the like.
- the water heated to a high temperature by the heating means 7 increases the kinetic energy of the molecules, which makes it easier to dissociate the bonds between hydrogen atoms and oxygen atoms, and further promotes water decomposition by centrifugation described later. Can be.
- the continuous liquid supply type centrifugal separator 1 is for extracting hydrogen gas and oxygen gas from water by dissociating bonds between hydrogen atoms and oxygen atoms of water molecules by centrifugal force generated by high-speed rotation.
- the rotation speed of the continuous liquid supply centrifuge 1 is set to a high speed of at least 500 rpm. You.
- the continuous liquid supply type centrifugal separator 1 includes a donut-shaped rotating tank 11 to which water passing through the heating means 7 is supplied, a high-speed rotating motor 12 for rotating the rotating tank 11, One thing is equipped with one to three.
- the high-speed rotating motor 12 is capable of rotating the rotating tank 11 at 500 rpm or more, preferably 150 to 2000 rpm as described above. Is used.
- the water supplied to the centrifugal separator 1 is sprayed on the inner wall inside the rotary tank 11 by high-pressure water injection means 9.
- the high-pressure water injection means 9 includes a pump 91 provided in the middle of the passage 10 connecting the heating means 7 and the centrifugal separator 1, and a tip inserted into the casing 13 and having an inner end inside the rotary tank 11. And a nozzle 92 arranged in the direction of rotation of the rotary tub 11.
- the high-pressure water injection means 9 injects high-pressure water from the tip of the nozzle 9 2 toward the inner wall inside the rotary tank 11 by driving the pump 9 1, thereby assisting the rotation of the rotary tank 11. At the same time, it plays a role in promoting the dissociation of water molecules by centrifugal force by the collision energy.
- the angle of the nozzle 92 is not particularly limited. Hydrogen separated in the centrifuge 1 is taken out from the upper part of the casing 13, and oxygen is taken out from the lower part of the casing 13 and supplied to the fuel cell 2.
- the fuel cell 2 is a known fuel cell that generates an electromotive force using hydrogen as an anode active material and oxygen as a cathode active material, and two porous carbon layers sandwiching an electrolyte solution 21 composed of an aqueous solution of KOH.
- hydrogen is supplied from the outside of one of the carbon plates 22 and oxygen is supplied from the outside of the other carbon plate 23, thereby generating a voltage between the two electrodes (between the carbon plates). This is to generate electric power.
- the electric motor 3 is configured to be rotationally driven by an electromotive force generated between the poles of the fuel cell 2, and the axle 8 is rotated by this drive to drive the vehicle.
- the surplus electric power generated by the generator 15 and the surplus electric power generated by the fuel cell 2 accompanying the driving of the vehicle are charged in the storage battery 4 and the multilayer capacitor 16, and the stored electric power is used when the vehicle starts. It is also used as a power source for the heating means 7, the pump 91, and the high-speed rotating motor 12.
- the reason why the multilayer capacitor 16 is used in combination with the storage battery 4 is that the multilayer capacitor 16 has a large storage capacity and can perform rapid charging and discharging even though it is small.
- a known generator generally used for automobiles may be used, but it is desirable to use a generator with as high an efficiency as possible.
- the electric vehicle according to the present invention can be driven for a long time by extracting a large amount of hydrogen and oxygen from water in a short time and using it as fuel for a fuel cell. Electric vehicle.
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- Electrochemistry (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Organic Chemistry (AREA)
- Combustion & Propulsion (AREA)
- Power Engineering (AREA)
- Transportation (AREA)
- Mechanical Engineering (AREA)
- Inorganic Chemistry (AREA)
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- General Health & Medical Sciences (AREA)
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- Fuel Cell (AREA)
- Electric Propulsion And Braking For Vehicles (AREA)
Abstract
An electric vehicle comprising a continuous liquid supply type centrifugal separator (1) for delivering hydrogen and oxygen separately by rotating at high speed water continuously fed into the separator, a fuel cell (2) for generating an electromotive force using hydrogen from the centrifugal separator as an anode active material and oxygen as a cathode active material, an electric motor (3) rotated by the electromotive force generated by the fuel cell, a storage battery (4) and a multilayer capacitor (16), wherein the vehicle is driven by the electric motor and dump power when the vehicle is driven is charged into the storage battery and the multilayer capacitor, thereby enabling large quantities of hydrogen and oxygen to be produced from water in a short time for use as fuel for the fuel cell and hence providing a practical electric vehicle that can be driven for an extended time.
Description
明 細 Details
技術分野 Technical field
本発明は燃料電池を使用した電気自動車に関するものであり、 その目 的は水から短時間で大量の水素及び酸素を取り出し、 これを燃料電池の 燃料として使用することによって長時間駆動が可能である実用的な電気 自動車を提供することにある。 背景技術 The present invention relates to an electric vehicle using a fuel cell, and its purpose is to extract a large amount of hydrogen and oxygen from water in a short time and use it as fuel for a fuel cell, thereby enabling long-time operation. It is to provide a practical electric vehicle. Background art
従来より使用されている自動車の駆動機関としては、 オット一やディ ーゼル等の内燃機関が主流であるが、 これらの化石燃料を使用する内燃 機関は排ガス中に窒素酸化物や二酸化炭素が含まれており、 その排出規 制は世界的に年々厳しくなっている。 Conventionally used internal combustion engines such as Otto and diesel are the main driving engines for automobiles. And its emission regulations are becoming stricter worldwide.
そこで、 近年では窒素酸化物や二酸化炭素を排出しない無公害自動車 の研究開発が活発に行われており、 その一例として水素吸蔵合金に貯蔵 された水素を燃料として利用する燃料電池自動車が挙げられる。 In recent years, research and development of non-polluting vehicles that do not emit nitrogen oxides or carbon dioxide have been actively conducted. One example is a fuel cell vehicle that uses hydrogen stored in a hydrogen storage alloy as fuel.
しかしながら、 水素吸蔵合金を用いた燃料電池においては、 水素吸蔵 合金の水素放出過程は吸熱反応であるため、 水素ガスの放出に伴って水 素吸蔵合金の温度が低下し、 一定温度を下回ると水素ガスの放出が殆ど 起こらなくなって蓄電池への充電が行えなくなるという問題があつた。 このような問題を解決するための方法としては、 水の電気分解装置を 使用し得られた水素と酸素を燃料電池に供給する方法も考えられるが、 自動車に搭載可能な程度の小型の電気分解装置では短時間で大量の水分 解ガスを得ることができなかった。
本発明者は、 かかる実情に鑑みて鋭意研究した結果、 水を高速遠心分 離によって水素と酸素に分離し、 これを燃料電池に供給することによつ て、 上記した充電や分解効率の問題を全て解決することができることを 見いだし、 本発明を完成するに至った。 発明の開示 However, in a fuel cell using a hydrogen storage alloy, the hydrogen release process of the hydrogen storage alloy is an endothermic reaction, so the temperature of the hydrogen storage alloy decreases with the release of hydrogen gas. There was a problem that the gas could hardly be released and the storage battery could not be charged. As a method to solve such a problem, a method of supplying hydrogen and oxygen obtained by using a water electrolysis device to a fuel cell can be considered, but a small electrolysis device that can be mounted on a vehicle is considered. The equipment could not obtain a large amount of decomposed gas in a short time. The present inventor has conducted intensive studies in view of such circumstances, and as a result, has been found that water is separated into hydrogen and oxygen by high-speed centrifugal separation and supplied to a fuel cell, thereby causing the above-described problems of charging and decomposition efficiency. Have been found to be able to solve all of them, and have completed the present invention. Disclosure of the invention
請求の範囲第 1項に係る発明は、 水を連続的に内部に取り入れて高速 回転することにより水素と酸素とを分離状態で取り出す連続液体供給型 遠心分離機と、 該遠心分離機から取り出された水素を陽極活物質とし、 酸素を陰極活物質として起電力を発生する燃料電池と、 該燃料電池から 発生する起電力により回転する電気モ一夕と、 蓄電池と、 積層コンデン ザとを備えてなり、 前記電気モー夕の駆動に伴って車両を駆動させ、 車 両駆動時の余剰電力を前記蓄電池及び積層コンデンサに充電することを 特徴とする電気自動車であるから、 遠心分離機によって水分子の水素原 子と酸素原子の結合を解離させることによって、 水から短時間で大量の 水素及び酸素を取り出すことができるので、 これを燃料電池の燃料とし て使用することによって、 長時間駆動が可能である実用的な電気自動車 となる。 The invention according to claim 1 is a continuous liquid supply type centrifugal separator in which hydrogen and oxygen are taken out in a separated state by continuously taking water into the inside and rotating at a high speed, and a centrifuge taken out from the centrifuge. A fuel cell that generates an electromotive force using hydrogen as an anode active material and oxygen as a cathode active material, an electric motor that rotates by the electromotive force generated from the fuel cell, a storage battery, and a stacked capacitor. The electric vehicle is characterized in that the vehicle is driven in accordance with the driving of the electric motor and the surplus electric power at the time of driving the vehicle is charged in the storage battery and the multilayer capacitor. By dissociating the bond between the hydrogen atom and the oxygen atom, a large amount of hydrogen and oxygen can be extracted from water in a short period of time. Therefore, it is a practical electric vehicle that can be driven for a long time.
請求項 2に係る発明は、 N i H 2 合金に接触させた水を前記連続液体 供給型遠心分離機に供給することを特徴とする請求の範囲第 1項記載の 電気自動車であるから、 N i H 2 の添加による化学反応と、 遠心分離機 による水分子の水素原子と酸素原子の結合の解離の相乗作用によって、 水から短時間で大量の水素及び酸素を取り出すことができ、 これを燃料 電池の燃料として使用することによって、 長時間駆動が可能である実用 的な電気自動車となる。 The invention according to claim 2, since an electric vehicle range first claim of claim, characterized in that to supply water in contact with the N i H 2 alloy into the continuous liquid feed centrifuge, N a chemical reaction by the addition of i H 2, by the synergistic action of the dissociation of binding of water molecules hydrogen atoms and oxygen atoms by centrifuge, can retrieve a large amount of hydrogen and oxygen in a short time from the water, fuel and this By using it as fuel for batteries, it becomes a practical electric vehicle that can be driven for a long time.
請求項 3に係る発明は、 同極同士が対向して配設された少なくとも一
組以上の 6 O M G s以上の磁石からなる水分子クラスター分解装置が備 えられ、 該分解装置を通過した水を前記遠心分離機に供給することを特 徴とする請求の範囲第 1項又は 2記載の電気自動車であるから、 遠心分 離による水分解の効率を高めることができ、 短時間で大量の水素及び酸 素を得ることができる。 The invention according to claim 3 is at least one in which the same poles are arranged to face each other. A water molecule cluster decomposing device comprising at least 6 OMG s or more magnets is provided, and water passing through the decomposing device is supplied to the centrifugal separator. Since the electric vehicle is described, the efficiency of water splitting by centrifugation can be increased, and a large amount of hydrogen and oxygen can be obtained in a short time.
請求項 4に係る発明は、 前記遠心分離機の回転槽内壁に対して、 高圧 水を吹き付ける高圧水噴射手段が設けられてなることを特徴とする請求 の範囲第 1項乃至 3いずれかに記載の電気自動車であるから、 回転槽の 回転が高圧水によって補助されるとともに、 衝突エネルギーによって遠 心力による水分子の解離が促進される。 The invention according to claim 4, wherein high-pressure water injection means for blowing high-pressure water is provided on an inner wall of the rotary tank of the centrifuge. 5. Since the electric vehicle is of the type described above, the rotation of the rotating tank is assisted by high-pressure water, and the dissociation of water molecules by centrifugal force is promoted by the collision energy.
請求項 5に係る発明は、 前記遠心分離機に供給される水を高温に加熱 する加熱手段が設けられてなることを特徴とする請求の範囲第 1項乃至 4いずれかに記載の電気自動車であるから、 加熱によって水分子の運動 エネルギーが増大し、 これによつて水素原子と酸素原子の結合が解離し 易くなり、 遠心分離による水分解を一層促進させることができる。 図面の簡単な説明 The invention according to claim 5, wherein the electric vehicle according to any one of claims 1 to 4, further comprising heating means for heating water supplied to the centrifuge to a high temperature. Therefore, heating increases the kinetic energy of water molecules, which makes it easier to dissociate the bonds between hydrogen atoms and oxygen atoms, and further promotes water decomposition by centrifugation. BRIEF DESCRIPTION OF THE FIGURES
第 1図は本発明に係る電気自動車の概略構成図であり、 第 2図は水分 子クラス夕一分解装置の一例を示す断面図である。 発明を実施するための最良の形態 FIG. 1 is a schematic configuration diagram of an electric vehicle according to the present invention, and FIG. 2 is a cross-sectional view showing an example of a moisture class decomposition apparatus. BEST MODE FOR CARRYING OUT THE INVENTION
以下、 本発明に係る電気自動車の好適な実施形態について図面に基づ いて説明する。 Hereinafter, a preferred embodiment of an electric vehicle according to the present invention will be described with reference to the drawings.
第 1図は本発明に係る電気自動車の概略構成図である。 FIG. 1 is a schematic configuration diagram of an electric vehicle according to the present invention.
本発明に係る電気自動車は、 水を連続的に内部に取り入れて高速回転 することにより水素と酸素とを分離した状態で取り出す連続液体供給型
遠心分離機 1と、 この遠心分離機 1から取り出された水素を陽極活物質 とし、 酸素を陰極活物質として起電力を発生する燃料電池 2と、 この燃 料電池 2から発生する起電力により回転する電気モータ 3と、 蓄電池 4 と、 積層コンデンサ 16を備えている。 The electric vehicle according to the present invention is a continuous liquid supply type in which hydrogen and oxygen are separated and taken out by continuously taking in water and rotating at high speed. A centrifuge 1, a fuel cell 2 that uses hydrogen extracted from the centrifuge 1 as an anode active material, and generates an electromotive force using oxygen as a cathode active material, and is rotated by the electromotive force generated from the fuel cell 2. An electric motor 3, a storage battery 4, and a multilayer capacitor 16.
そして、 電気モータ 3の駆動に伴って車軸 8を回転させて車両を駆動 させ、 車両駆動時に発生した余剰電力を蓄電池 4及び積層コンデンサ 1 6に充電するように構成されている。 Then, the vehicle is driven by rotating the axle 8 with the driving of the electric motor 3, and the storage battery 4 and the multilayer capacitor 16 are charged with surplus power generated when the vehicle is driven.
貯槽 5内には水 (H2 0) が貯留されており、 この水は NiH2 合金 17が内面に付着されたパイプ 18の内部を通過することによって、 N i H2 合金と接触した後にパイプ 18から取り出される。 但し、 本発明 において、 水を NiH2 合金と接触させるための構成はこれに限定され ず、 例えば NiH2 合金の多孔質ペレットに水を通過させる構成や、 貯 槽 5内に NiH2 合金を埋設しておく構成としてもよい。 Water (H 2 0) is stored in the storage tank 5, and this water passes through the inside of the pipe 18 having the NiH 2 alloy 17 attached to the inner surface thereof, so that the water contacts the Ni H 2 alloy. Taken out of 18. However, in the present invention, the configuration for bringing water into contact with the NiH 2 alloy is not limited to this.For example, a configuration in which water passes through porous pellets of the NiH 2 alloy, or a configuration in which the NiH 2 alloy is embedded in the storage tank 5 The configuration may be set in advance.
NiH2 は侵入型の水素化物であって、 水及びエタノールと反応して 水素を発生する性質を備えている。 NiH 2 is an interstitial hydride and has the property of reacting with water and ethanol to generate hydrogen.
本発明では、 水を NiH2 合金に接触させることによって、 6H2 0 + 2 N i H2 -»2 N i H2 + 6 H2 + 302 の反応を生じさせ、 水から 水素と酸素を発生させることができる。 In the present invention, by contacting the water to NiH 2 alloy, 6H 2 0 + 2 N i H 2 - cause reactions »2 N i H 2 + 6 H 2 + 30 2, hydrogen and oxygen from water Can be generated.
本発明においては、 上記したように水を N i H2 合金に接触させるこ とによって水から水素と酸素を取り出すことができるが、 以下に説明す る如く、 この水を水分子クラスター分解装置 6、 加熱手段 7、 連続液体 供給型遠心分離機 1に順次供給することによって、 NiH2 による水分 解を促進させて、 短時間で効率良く大量の水素と酸素を得ることが可能 となる。 In the present invention, hydrogen and oxygen can be extracted from water by bringing the water into contact with the NiH 2 alloy as described above. By sequentially supplying the heating means 7 and the continuous liquid supply centrifuge 1 to the centrifuge 1, the decomposition of water by NiH 2 is promoted, and a large amount of hydrogen and oxygen can be efficiently obtained in a short time.
但し、 本発明では、 水を NiH2 合金に接触させずに水分子クラス夕 一分解装置 6、 加熱手段 7、 連続液体供給型遠心分離機 1に順次供給す
ることによつても、 高速遠心分離によつて水分子の酸素原子と水素原子 の結合を解離させて水素と酸素を得ることが可能である。 However, in the present invention, water molecules class without contacting the water NiH 2 alloy evening one cracker 6, the heating means 7 are sequentially supplied to the continuous liquid feed type centrifugal separator 1 In this case, it is possible to obtain hydrogen and oxygen by dissociating the bond between the oxygen atom and the hydrogen atom of the water molecule by high-speed centrifugation.
第 2図は水分子クラス夕一分解装置 6の一例を示す断面図である。 水分子クラスター分解装置 6は、 入水口 6 1及び出水口 6 2を備えた ケース体 6 3と、 このケース体 6 3の内部に配設された一組以上 (図示 例では 4組) の永久磁石 6 4から構成される。 FIG. 2 is a cross-sectional view showing an example of the water molecule class evening decomposition device 6. The water molecule cluster decomposing device 6 includes a case body 63 having an inlet 61 and a water outlet 62, and one or more sets (four sets in the illustrated example) provided inside the case body 63. Consists of magnets 6 4.
ケース体 6 3の内部は通水可能なフィル夕一 6 5によって複数の区画 に区切られており、 各区画にはそれそれ一組の永久磁石 6 4が同極同士 (図示例では S極と S極) を対向させた状態で配設されている。 The inside of the case body 63 is divided into a plurality of sections by water-filling filters 65, each of which has a pair of permanent magnets 64 of the same polarity (in the example shown, the S pole and the S pole). (S pole) facing each other.
前記貯槽 5から取り出された水は、 入水口 6 1からケース体 6 3内部 へと導入され、 各区画に配設された永久磁石 6 4の S極同士の間を順次 通過することによって次第に水分子クラスターが小さくなり、 最後に出 水口 6 2から取り出される。 The water taken out of the storage tank 5 is introduced into the inside of the case body 63 from the water inlet 61, and gradually passes through between the S poles of the permanent magnets 64 disposed in each section. The molecular clusters become smaller and are finally extracted from the outlet 62.
周知の如く、 水は本来、 単独の分子 (H 2 0 ) で存在するのではなく 幾つかの分子がまとまった状態で存在している。 この分子集団をクラス 夕一というが、 本発明においては磁力によってこのクラスターを小さく することによって、 後述する遠心分離による水分解を一層促進させるこ とができる。 As is well known, water does not exist as a single molecule (H 20 ), but as a group of several molecules. This molecular population is referred to as a class one. In the present invention, by reducing this cluster by magnetic force, water decomposition by centrifugation described later can be further promoted.
尚、 永久磁石 6 4としては 6 O M G s以上、 好ましくは 1 0 0〜 1 5 O M G sのものが使用される。 これは、 6 O M G s未満の磁石を使用し た場合には、 水分子クラス夕一を充分に小さくすることができないため である。 As the permanent magnet 64, a permanent magnet of 6 OMGs or more, preferably 100 to 15 OMGs, is used. This is because the use of a magnet of less than 6 OMGs cannot sufficiently reduce the water molecule class.
加熱手段 7は水分子クラスター分解装置 6から取り出された水を加熱 するために設けられている。 尚、 図示例では電熱線ヒーターが示されて いるが、 本発明において加熱手段 7の構成はこれに限定されず、 セラミ ックヒー夕一等であってもよい。
加熱手段 7によって高温に加熱された水は、 分子の運動エネルギーが 増大し、 これによつて水素原子と酸素原子の結合が解離し易くなり、 後 述する遠心分離による水分解を一層促進させることができる。 The heating means 7 is provided for heating the water taken out from the water molecule cluster decomposing device 6. Although a heating wire heater is shown in the illustrated example, the configuration of the heating means 7 in the present invention is not limited to this, and may be a ceramic heater or the like. The water heated to a high temperature by the heating means 7 increases the kinetic energy of the molecules, which makes it easier to dissociate the bonds between hydrogen atoms and oxygen atoms, and further promotes water decomposition by centrifugation described later. Can be.
連続液体供給型遠心分離機 1は、 高速回転により発生する遠心力によ つて水分子の水素原子と酸素原子の結合を解離させ、 水から水素ガスと 酸素ガスを取り出すためのものである。 The continuous liquid supply type centrifugal separator 1 is for extracting hydrogen gas and oxygen gas from water by dissociating bonds between hydrogen atoms and oxygen atoms of water molecules by centrifugal force generated by high-speed rotation.
但し、 この水素原子と酸素原子の結合解離のためには多大なエネルギ —を必要とするので、 連続液体供給型遠心分離機 1の回転速度は少なく とも 5 0 0 0 0 r p m以上の高速とされる。 However, since a large amount of energy is required for the bond dissociation of the hydrogen atom and the oxygen atom, the rotation speed of the continuous liquid supply centrifuge 1 is set to a high speed of at least 500 rpm. You.
連続液体供給型遠心分離機 1は、 加熱手段 7を通過した水が供給され る平面視ド一ナツ状の回転槽 1 1と、 回転槽 1 1を回転させる高速回転 モー夕 1 2と、 ケ一シング 1 3を備えている。 尚、 この高速回転モー夕 1 2は前述の如く回転槽 1 1を 5 0 0 0 0 r p m以上、 好ましくは 1 5 0 0 0 0〜2 0 0 0 0 0 r p mで回転させることが可能なものが使用さ れる。 The continuous liquid supply type centrifugal separator 1 includes a donut-shaped rotating tank 11 to which water passing through the heating means 7 is supplied, a high-speed rotating motor 12 for rotating the rotating tank 11, One thing is equipped with one to three. The high-speed rotating motor 12 is capable of rotating the rotating tank 11 at 500 rpm or more, preferably 150 to 2000 rpm as described above. Is used.
遠心分離機 1に供給される水は、 高圧水噴射手段 9によって回転槽 1 1の内側の内壁に吹き付けられる。 The water supplied to the centrifugal separator 1 is sprayed on the inner wall inside the rotary tank 11 by high-pressure water injection means 9.
高圧水噴射手段 9は、 加熱手段 7と遠心分離機 1とを繋ぐ通路 1 0の 中途部に設けられたポンプ 9 1と、 ケーシング 1 3内部に挿入され先端 を回転槽 1 1の内側の内壁方向であって且つ回転槽 1 1の回転方向に向 けて配設されたノズル 9 2から構成されている。 The high-pressure water injection means 9 includes a pump 91 provided in the middle of the passage 10 connecting the heating means 7 and the centrifugal separator 1, and a tip inserted into the casing 13 and having an inner end inside the rotary tank 11. And a nozzle 92 arranged in the direction of rotation of the rotary tub 11.
上記高圧水噴射手段 9は、 ポンプ 9 1の駆動によってノズル 9 2先端 から回転槽 1 1の内側の内壁に向けて高圧水を噴射し、 これによつて回 転槽 1 1の回転を補助するとともに、 衝突エネルギーによって遠心力に よる水分子の解離を促進させる役割を果たす。 The high-pressure water injection means 9 injects high-pressure water from the tip of the nozzle 9 2 toward the inner wall inside the rotary tank 11 by driving the pump 9 1, thereby assisting the rotation of the rotary tank 11. At the same time, it plays a role in promoting the dissociation of water molecules by centrifugal force by the collision energy.
但し、 本発明においてノズル 9 2の角度は特に限定されない。
遠心分離機 1において分離された水素はケーシング 1 3の上部から、 酸素はケーシング 1 3の下部から、 それそれ取り出されて燃料電池 2へ と供給される。 However, in the present invention, the angle of the nozzle 92 is not particularly limited. Hydrogen separated in the centrifuge 1 is taken out from the upper part of the casing 13, and oxygen is taken out from the lower part of the casing 13 and supplied to the fuel cell 2.
燃料電池 2は、 水素を陽極活物質とし、 酸素を陰極活物質として起電 力を発生する公知のものであって、 K O Hの水溶液からなる電解液 2 1 を挟んで 2枚の多孔性の炭素板 2 2、 2 3を配設し、 一方の炭素板 2 2 の外側から水素を供給し、 他方の炭素板 2 3の外側から酸素を供給する ことによって、 両極間 (炭素板間) に起電力を発生させるものである。 電気モー夕 3は燃料電池 2の両極間に発生した起電力によって回転駆 動するように構成されており、 この駆動によって車軸 8が回転されて車 両が駆動される。 The fuel cell 2 is a known fuel cell that generates an electromotive force using hydrogen as an anode active material and oxygen as a cathode active material, and two porous carbon layers sandwiching an electrolyte solution 21 composed of an aqueous solution of KOH. By disposing the plates 22 and 23, hydrogen is supplied from the outside of one of the carbon plates 22 and oxygen is supplied from the outside of the other carbon plate 23, thereby generating a voltage between the two electrodes (between the carbon plates). This is to generate electric power. The electric motor 3 is configured to be rotationally driven by an electromotive force generated between the poles of the fuel cell 2, and the axle 8 is rotated by this drive to drive the vehicle.
そして、 車両の駆動に伴って発電機 1 5により発生した余剰電力及び 燃料電池 2にて発生した余剰電力は、 蓄電池 4及び積層コンデンサ 1 6 に充電され、 これら蓄えられた電力は車両の始動時などに使用されるほ か、 加熱手段 7、 ポンプ 9 1、 高速回転モ一夕 1 2の電源としても使用 される。 The surplus electric power generated by the generator 15 and the surplus electric power generated by the fuel cell 2 accompanying the driving of the vehicle are charged in the storage battery 4 and the multilayer capacitor 16, and the stored electric power is used when the vehicle starts. It is also used as a power source for the heating means 7, the pump 91, and the high-speed rotating motor 12.
本発明において、 蓄電池 4と併用して積層コンデンサ 1 6を使用する のは、 積層コンデンサ 1 6は小型でも蓄電容量が大きく急速な充放電を 行うことができるためである。 In the present invention, the reason why the multilayer capacitor 16 is used in combination with the storage battery 4 is that the multilayer capacitor 16 has a large storage capacity and can perform rapid charging and discharging even though it is small.
発電機 1 5としては、 一般的に自動車に使用される公知のものを使用 すればよいが、 できるだけ高効率のものを使用することが望ましい。 産業上の利用可能性 As the generator 15, a known generator generally used for automobiles may be used, but it is desirable to use a generator with as high an efficiency as possible. Industrial applicability
以上説明したように、 本発明に係る電気自動車は、 水から短時間で大 量の水素及び酸素を取り出し、 これを燃料電池の燃料として使用するこ とにより、 長時間駆動が可能である実用的な電気自動車となる。
As described above, the electric vehicle according to the present invention can be driven for a long time by extracting a large amount of hydrogen and oxygen from water in a short time and using it as fuel for a fuel cell. Electric vehicle.
Claims
1. 水を連続的に内部に取り入れて高速回転することにより水素と酸素 とを分離状態で取り出す連続液体供給型遠心分離機 (1) と、 該遠心分 離機から取り出された水素を陽極活物質とし、 酸素を陰極活物質として 起電力を発生する燃料電池 (2) と、 該燃料電池から発生する起電力に よって回転する電気モー夕 (3) と、 蓄電池 (4) と、 積層コンデンサ ( 16) とを備えてなり、 前記電気モー夕の駆動に伴って車両を駆動さ せ、 車両駆動時の余剰電力を前記蓄電池及び積層コンデンサに充電する ことを特徴とする電気自動車。 1. A continuous liquid supply centrifuge (1) that separates hydrogen and oxygen by separating water by continuously taking in water and rotating at high speed, and using the hydrogen extracted from the centrifugal separator as an anode. A fuel cell (2) that generates an electromotive force using oxygen as a cathode active material, an electric motor (3) that is rotated by the electromotive force generated from the fuel cell, a storage battery (4), and a multilayer capacitor ( 16) An electric vehicle, comprising: driving a vehicle in accordance with driving of the electric motor, and charging the storage battery and the multilayer capacitor with surplus power when the vehicle is driven.
2. N i H2 合金 ( 17 ) に接触させた水を前記連続液体供給型遠心分 離機に供給することを特徴とする請求の範囲第 1項記載の電気自動車。2. N i H 2 electric vehicle range first claim of claim alloy the contacted water (17) and supplying the continuous liquid supply type centrifugal away machine.
3. 同極同士が対向して配設された少なくとも一組以上の 6 OMGs以 上の磁石からなる水分子クラスター分解装置 (6) が備えられ、 該分解 装置を通過した水を前記遠心分離機に供給することを特徴とする請求の 範囲第 1項又は第 2項記載の電気自動車。 3. A water molecule cluster decomposing device (6) comprising at least one set of 6 or more OMGs or more magnets arranged with the same poles facing each other is provided. 3. The electric vehicle according to claim 1, wherein the electric vehicle is supplied to a vehicle.
4. 前記遠心分離機の回転槽内壁に対して、 高圧水を吹き付ける高圧水 噴射手段が設けられてなることを特徴とする請求の範囲第 1項乃至第 3 項いずれかに記載の電気自動車。 4. The electric vehicle according to any one of claims 1 to 3, wherein high-pressure water injection means for spraying high-pressure water is provided on an inner wall of the rotary tank of the centrifugal separator.
5. 前記遠心分離機に供給される水を高温に加熱する加熱手段 (7) が 設けられてなることを特徴とする請求の範囲第 1項乃至第 4項いずれか に記載の電気自動車。
補正書の請求の範囲 5. The electric vehicle according to any one of claims 1 to 4, further comprising heating means (7) for heating water supplied to the centrifuge to a high temperature. Claims of amendment
[2000年 8月 18日 (18. 08. 00) 国際事務局受理:出願当初の請求の範囲 3は 取り下げられた;出願当初の請求の範囲 1, 2, 4及び 5は補正された。 (1頁)] [August 18, 2000 (18.08.00) Accepted by the International Bureau: Claim 3 at the time of filing was withdrawn; claims 1, 2, 4 and 5 at the time of filing were amended. (1 page)]
1. (補正後) 水を連続的に内部に取り入れて高速回転することによつ て水素と酸素とを分離状態で取り出す連続液体供給型遠心分離機 ( 1 ) と、 該遠心分離機から取り出された水素を陽極活物質とし、 酸素を陰極 活物質として起電力を発生する燃料電池 (2) と、 該燃料電池から発生 する起電力によって回転する電気モ一夕 (3) と、 蓄電池 (4) と、 積 層コンデンサ ( 1 6) と、 同極同士が対向して配設された複数組の 60 1. (After correction) A continuous liquid supply centrifuge (1) that takes out hydrogen and oxygen in a separated state by continuously taking in water and rotating at high speed, and taking out the centrifuge. A fuel cell (2) that generates an electromotive force using the extracted hydrogen as an anode active material and oxygen as a cathode active material; an electric motor (3) that rotates by the electromotive force generated from the fuel cell; ), A multilayer capacitor (16), and multiple sets of 60s with the same poles facing each other.
MG s以上の磁石からなる水分子クラスター分解装置 (6) とを備えて なり、 該分解装置を通過した水を前記遠心分離機に供給するとともに、 前記電気モータの駆動に伴って車両を駆動させ、 車両駆動時の余剰電力 を前記蓄電池及び積層コンデンサに充電することを特徴とする電気自動 車。 A water molecule cluster decomposing device (6) comprising a magnet of MGs or more, and supplying water passing through the decomposing device to the centrifugal separator, and driving a vehicle in accordance with driving of the electric motor. An electric vehicle, wherein surplus electric power when the vehicle is driven is charged in the storage battery and the multilayer capacitor.
2. NiH2 合金 ( 1 7) に接触させた水を前記連続液体供給型遠心分 離機に供給することを特徴とする請求の範囲第 1項記載の電気自動車。 2. The electric vehicle according to claim 1, wherein water brought into contact with the NiH 2 alloy (17) is supplied to the continuous liquid supply type centrifugal separator.
3. (削除) 3. (Delete)
4. (補正後) 前記遠心分離機の回転槽内壁に対して、 高圧水を吹き付 ける高圧水噴射手段が設けられてなることを特徴とする請求の範囲第 1 項又は第 2項いずれかに記載の電気自動車。 4. (After correction) A high-pressure water injection means for spraying high-pressure water on the inner wall of the rotary tank of the centrifuge is provided, either of the claims 1 or 2. An electric vehicle according to claim 1.
5. (補正後) 前記遠心分離機に供給される水を高温に加熱する加熱手 段 (7) が設けられてなることを特徴とする請求の範囲第 1項、 第 2項 、 第 4項のいずれかに記載の電気自動車。
条約 1 9条に基づく説明書 請求の範囲第 1項は、 遠心分離機に供給される水が、 同極同士が対向 して配設された複数組の 6 0 M G s以上の磁石からなる水分子クラス夕 一分解装置を通過した水であることを明確にしたものである。 5. (After correction) A heating means (7) for heating water supplied to the centrifuge to a high temperature is provided, wherein the heating means (7) is provided. The electric vehicle according to any one of the above. Statement based on Article 19 of the Convention Claim 1 states that the water supplied to the centrifuge is water consisting of multiple sets of 60 MGs or more magnets with the same poles facing each other. The molecular class clarifies that the water has passed through the decomposer.
本発明は、 同極同士が対向して配設された複数組の 6 O M G s以上の 磁石からなる水分子クラス夕一分解装置を水が通過することによって、 水はクラスターを破壊するのに充分に強い磁力を多段階にわたって受け ることとなり、 このようにして子め分子クラスタ一が充分に小さくされ た水を遠心分離機に供給することによって、 水から酸素と水素とを短時 間で効率良く取り出すことが可能となり、 長時間の運転が可能な実用的 な電気自動車を得ることができる。 According to the present invention, water passes through a water molecule class decomposer composed of a plurality of sets of magnets of 6 OMGs or more in which the same poles are opposed to each other, so that water is sufficient to destroy clusters. By supplying the centrifugal separator with water whose molecular clusters have been sufficiently reduced in this way, oxygen and hydrogen can be efficiently converted from water in a short time. It is possible to obtain a practical electric vehicle that can be taken out well and can be operated for a long time.
これに対し、 国際調査報告書において引用された引用文献のうちの 1 つには、 磁石の回転磁界によるイオン水生成電解促進槽が開示されてい るが、 6 O M G s以上の磁力をもつ磁石を使用する構成や同極同士が対 向して配設された複数組の磁石を使用する構成については記載されてお らず、 またクラス夕一を破壊した水を遠心分離機に供給して酸素と水素 とに分離するという構成を導くための記載や示唆も存在しない。
On the other hand, one of the references cited in the International Search Report discloses an electrolysis promotion tank for the generation of ionized water by the rotating magnetic field of a magnet.However, a magnet with a magnetic force of 6 OMGs or more is required. It does not describe the configuration to use or the configuration using multiple sets of magnets with the same poles facing each other, and also supplies water that destroyed class I to the centrifuge to supply oxygen. There is no description or suggestion for deriving the configuration of separation into hydrogen and hydrogen.
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PCT/JP1999/002235 WO2000065679A1 (en) | 1999-04-26 | 1999-04-26 | Electric vehicle |
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PCT/JP1999/002235 WO2000065679A1 (en) | 1999-04-26 | 1999-04-26 | Electric vehicle |
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WO2003064318A1 (en) * | 2002-01-29 | 2003-08-07 | Honda Giken Kogyo Kabushiki Kaisha | Hydrogen generating apparatus, hydrogen generating system and use thereof |
FR2843898A1 (en) * | 2002-08-30 | 2004-03-05 | Renault Sa | DEVICE FOR RECOVERING LIQUID FROM A DIPHASIC FLUID AND FUEL CELL COMPRISING SUCH A DEVICE |
JP2006021961A (en) * | 2004-07-08 | 2006-01-26 | Aqua Energy Kk | Method and system for producing hydrogen |
US7138198B2 (en) | 2002-02-15 | 2006-11-21 | Honda Giken Kogyo Kabushiki Kaisha | Ventilation apparatus for fuel cell system |
WO2007023514A1 (en) * | 2005-08-22 | 2007-03-01 | Kousaku Mabuchi | System for producing hydrogen from seawater and method for producing hydrogen |
WO2023026226A1 (en) * | 2021-08-25 | 2023-03-02 | TI-Holdings B.V. | Thermal inverter box |
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WO2023026226A1 (en) * | 2021-08-25 | 2023-03-02 | TI-Holdings B.V. | Thermal inverter box |
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