WO1999049471A1 - Reacteur pour produire de l'energie et des neutrons par reaction electrolytique dans une solution d'eau legere ou d'eau lourde - Google Patents

Reacteur pour produire de l'energie et des neutrons par reaction electrolytique dans une solution d'eau legere ou d'eau lourde Download PDF

Info

Publication number
WO1999049471A1
WO1999049471A1 PCT/JP1999/001443 JP9901443W WO9949471A1 WO 1999049471 A1 WO1999049471 A1 WO 1999049471A1 JP 9901443 W JP9901443 W JP 9901443W WO 9949471 A1 WO9949471 A1 WO 9949471A1
Authority
WO
WIPO (PCT)
Prior art keywords
reaction
neutrons
energy
generated
electrode
Prior art date
Application number
PCT/JP1999/001443
Other languages
English (en)
Japanese (ja)
Inventor
Tadahiko Mizuno
Original Assignee
Araki, Masao
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 Araki, Masao filed Critical Araki, Masao
Publication of WO1999049471A1 publication Critical patent/WO1999049471A1/fr

Links

Classifications

    • G—PHYSICS
    • G21—NUCLEAR PHYSICS; NUCLEAR ENGINEERING
    • G21B—FUSION REACTORS
    • G21B3/00—Low temperature nuclear fusion reactors, e.g. alleged cold fusion reactors
    • 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
    • Y02E30/00—Energy generation of nuclear origin
    • Y02E30/10—Nuclear fusion reactors

Definitions

  • the present invention relates to a reactant for generating energy and neutrons by an electrolytic reaction in light water or a heavy aqueous solution, and a method for generating energy and neutrons using the reactants.
  • the present invention provides a reactant capable of generating energy with good controllability and efficiently generating neutrons by an electrolysis reaction in light water or heavy aqueous solution.
  • the purpose is to do.
  • Another object of the present invention is to provide a method for generating energy with good controllability.
  • a further object of the present invention is to provide a method for efficiently generating neutrons.
  • a substrate comprising a high melting point metal and a metal layer formed on the surface thereof and active against hydrogen are included.
  • the reactants for generating energy by the electrolytic reaction there is provided, according to the present invention, by using the reactants or Ranaru force source cathode electrode and ⁇ Roh one cathode electrode of the present invention light water
  • a method for generating energy in which an electrolytic reaction is caused in a heavy aqueous solution to obtain heat energy exceeding electric power supplied between both electrodes.
  • an electrolysis reaction is caused in light water or a heavy aqueous solution using a cathode electrode and an anode electrode comprising the reactant of the present invention, and the reaction is carried out in this reaction.
  • a neutron generation method for efficiently generating neutrons is provided.
  • FIG. 1 is a schematic diagram showing an example of an apparatus for generating energy and neutrons by an electrolytic reaction according to the present invention.
  • FIG. 2 is a graph showing an example of the relationship between the current density and the applied voltage during the electrolytic reaction according to the present invention.
  • FIG. 3 is a schematic diagram showing a heat energy utilization system incorporating the reaction cell of the present invention.
  • FIG. 4 is a schematic diagram showing a neutron utilization system incorporating the reaction cell of the present invention.
  • FIG. 5 is a graph showing an example of a relationship between output energy and input energy during the electrolytic reaction in Examples and Comparative Examples according to the present invention.
  • FIG. 6 is a graph showing the rate of occurrence of the number of neutrons during the electrolytic reaction in the example according to the present invention.
  • the reactant of the present invention is obtained by coating a substrate made of a refractory metal with a metal active against hydrogen.
  • the high melting point metal constituting the substrate of the reactant of the present invention for example, at least one metal selected from titanium, tungsten, zirconium, and nonadium is preferable. Tungsten Most preferred.
  • the hydrogen-active metal that covers the substrate is preferably at least one metal selected from, for example, platinum, nickel, radium, and nickel. Platinum is the most preferred. New
  • the electrolytic reaction can be stably continued, and the movement of hydrogen in the reactant can be controlled. And can be. Therefore, the reactant of the present invention can control the generation of energy by the electrolytic reaction with good controllability, and can efficiently generate neutrons. . Furthermore, the reactants of the present invention are less deteriorated even when used in a high-temperature electrolytic solution for a long time, and therefore can generate stable heat.
  • the high melting point metal used for the reactant of the present invention is preferably a plate having a thickness of about 0.2 to 1 mm. Also, the metal that is active on hydrogen and that covers the surface is usually preferably about 0.01 to 1 mm, but a thickness of about 0.1 mm is sufficient. It is.
  • the reactant of the present invention can be produced by depositing a coating metal on a high melting point metal plate by a vapor deposition method such as a sputtering method.
  • the reactant of the present invention is obtained by arranging a coating metal powder around a plate-shaped mass of a high melting point metal powder, compression-molding the powder, and sintering the obtained compact in a high vacuum. It is also obtained by tying.
  • the type of metal and the shape of the reactant used in the reactant of the present invention are determined by the amount of heat energy to be generated, temperature, current density, It depends on the type of electrolyte. For example, as described later, in order to generate 1 kilobit of thermal energy, at least 1 cm 2 is required as the surface area of the reactant.
  • an aqueous solution of an electrolyte such as metal hydroxide, sulfate, carbonate, and nitrate is used.
  • the water used is light or heavy.
  • the electrolyte concentration of the electrolyte is preferably about 0.1 to 30%.
  • the reactant of the present invention was used as a force source electrode, immersed in an electrolytic solution together with an anode electrode made of platinum or the like, and an electric current was passed between the two electrodes. Is electrolyzed. When the reactants are electrolyzed, a nuclear reaction occurs, and a large amount of energy and neutrons can be generated.
  • the voltage applied between the force source electrode and the anode electrode is preferably about 10 V to about 500 V, more preferably 50 V to 500 V.
  • the reaction cell 1 for generating the electrolytic reaction is housed in the constant temperature chamber 2.
  • a thermostatic water circulating tank 3 is provided outside the thermostatic chamber 2, and the temperature in the thermostatic chamber 2 is controlled by the thermostatic water circulating in the thermostatic water circulating tank 3.
  • a fan 4 is provided in the constant temperature chamber 2, whereby the atmosphere in the constant temperature chamber 2 is stirred, and the temperature in the constant temperature chamber 2 is kept constant (constant temperature).
  • the reaction cell 1 includes a reaction vessel 5 made of metal (for example, stainless steel SS304).
  • the reaction vessel 5 is hermetically sealed, so that the temperature inside the reaction vessel 5 can be raised to accelerate the electrolytic reaction.
  • the reaction vessel 5 stores an electrolyte 6 therein.
  • the electrolytic solution 6 is stirred by rotating the rotor 8 by the electromagnetic force from the electromagnetic generator 7 attached to the bottom of the constant temperature water circulation tank 3.
  • the temperature of the electrolytic solution 6 is not only controlled by the constant temperature water in the constant temperature water circulation tank 3 but also finely adjusted by a heater wire 9 wound around the reaction vessel 5. That is, by heating the electrolytic solution 6 by energizing the wire 9 by the heater power supply 10, fine adjustment of the temperature of about 0.1 ° C. is possible.
  • the force source electrode 11 and the anode electrodes 12 and 13 are connected to the tips of three platinum rods inserted from the top of the reaction vessel 5. All the electrodes 11 to 13 are immersed in the electrolyte solution 6 and laid.
  • Force electrode 11 is composed of the reactant of the present invention.
  • the area of the force source electrode 11 varies depending on the generated thermal energy. For example, in order to generate one kilowatt of heat, the surface area of the cathode electrode 11 must be at least about 1 cm 2. You. At this time, 0.1 kilowatt is required as the input, and 100 cm 3 is required as the electrolyte 6. Therefore, in order to generate 100 kilowatts of heat, the surface area of the power source 11 must be 0.1 m 2 and the amount of the electrolyte must be 0.1 m 3.
  • the anode electrodes 12 and 13 are preferably formed of platinum.
  • the anode electrode 12 is plate-shaped and is used as an auxiliary electrode.
  • the anode electrode 13 has a mesh shape and is used as a main anode electrode.
  • the total area of the anode electrodes 12 and 13 is preferably about 1 0 times the surface area of the force source 11.
  • the anode electrodes 12 and 13 are arranged at a distance of several cm from the force source electrode 11, and the anode electrode 13 is connected to the force source electrode 11. It is arranged in a semi-cylindrical shape so as to surround it.
  • the auxiliary anode electrode 12 does not need to be particularly provided.
  • the main anode electrode 13 is preferably arranged in a cylindrical shape so as to solidify the power source electrode 11 at a position away from the power source electrode 11. .
  • Anode Such an electrode arrangement is particularly useful for sustaining the electrolytic reaction.
  • a platinum black catalyst 14 is arranged at the upper part of the reaction vessel 5.
  • the platinum black catalyst 14 recombines hydrogen generated from the power source electrode 11 with oxygen generated from the anode electrodes 12 and 13 to form water. It has a function to return.
  • the platinum black catalyst 14 is in a mesh shape and is arranged in a cylindrical shape on the upper inner wall of the reaction vessel 5.
  • thermocouple 15 is inserted from the top of the reaction vessel 5. heat The temperature of the force source electrode 11, ie, the reactant of the present invention, is measured by the thermocouple 15 with an accuracy of 0.03 ° C. The actual measurement is made at the top, middle, and bottom of the reactant, and the average of these values is used as the measured value.
  • thermocouple 15 The temperature output from the thermocouple 15 is monitored by a digital voltmeter 16. Further, c to standard junction 1 7 thermocouple 1 5 is crushed immersed in a constant temperature water of the thermostatic water circulation tank 3
  • thermocouple 15 In order to determine the amount of heat energy generated from the temperature measured by the thermocouple 15, calibrate the temperature measurement value in advance. That is, various powers are input between the force electrode 11 and the anode electrodes 12 and 13, and a thermocouple is applied to each input power.
  • a pressure measuring terminal 18 is provided at the top of the reaction vessel 5.
  • This terminal 18 has a strain gauge type piezoelectric transducer 1
  • the piezoelectric transducer 19 is connected, and the amount of hydrogen absorbed in the reactant can be obtained directly from the oxygen partial pressure in the reaction vessel 5 by the piezoelectric transducer 19.
  • the output value of the piezoelectric transducer 19 is monitored by a digital voltmeter 20.
  • the electrolytic reaction is performed by supplying power from a power source 21 between the force source electrode 11 and the two anode electrodes 12 and 13. Power is supplied through a white bar connected to each electrode. The voltage applied to each electrode is Monitored by the Talbot Meter 22.
  • the reactor 9 is heated by calorie using the heater 9, but once the reaction starts, the temperature of the reaction cell 1 is maintained by the heat of reaction. After that, the voltage is controlled according to the reaction temperature, the type of reactant, etc., to maintain the reaction.
  • the value of the voltage applied during the electrolytic reaction is as described above, and differs depending on the reaction temperature, the type of the reactant, the type of the electrolytic solution 6, the arrangement of the electrodes in the reaction vessel 5, and the like.
  • the current decreases, heat and light are emitted in the vicinity of the force source electrode 11, generating a large amount of energy and neutrons.
  • Figure 2 is a graph showing an example of the relationship between the current density between the electrodes and the applied voltage when an electrolytic reaction is occurring. For each reaction between points a to d shown in Figure 2, A description is given below.
  • the temperature of electrolyte 6 can be set by raising the temperature of the constant temperature water or passing it through the heater wire 9.
  • the reaction may be performed using an external heat source such as electricity, or may be reaction heat generated by causing electrolysis in the electrolytic solution 6 in advance.
  • a voltage is applied to the force source electrode 11 and the anode electrodes 12 and 13 to generate an electric field in the electrolytic solution 6 to start electrolysis.
  • a current is applied between the force electrode 11 immersed in the electrolyte 6 and the anode electrodes 12 and 13 to increase the voltage
  • hydrogen is applied to the force electrode 11.
  • Oxygen gas is generated in the gas and anode electrodes 12 and 13 and normal electrolysis is performed.
  • the voltage is further increased, the generation of gas gradually increases, and hydrogen gas and steam are periodically released. The current fluctuates violently, and a sound is generated between the cathode electrode 11 and the electrolyte 6.
  • a spark is generated between the power source electrode 11 and the electrolyte 6 and discharge starts.
  • the reaction temperature gradually rises.
  • the current density and voltage that is, the input power
  • the amount of energy generated decreases. Therefore, in order to keep the current density and voltage constant during the reaction, a rectangular wave voltage is applied, and power is intermittently input to keep the reaction temperature constant.
  • the frequency of the square wave, the ratio between the peak (time during which voltage is applied) and the valley (time during which no voltage is applied) of the square wave, and the wave height of the square wave are adjusted to keep the reaction temperature constant. Keep the current density and voltage constant. For example, by reducing the ratio of the peaks and valleys of a square wave, or by reducing the wave height, the actual input power can be reduced, and the reaction temperature is prevented from rising more than necessary. be able to.
  • the pressure in the sealed reaction vessel is also adjusted. As a result, a large amount of energy is generated between the points c and d. As a result, the reaction temperature rises to reach the boiling point of the electrolyte. However, if the pressure in the reaction vessel 5 remains at atmospheric pressure, the electrolyte will boil and the reaction temperature will not rise above the boiling point. Therefore, the pressure in the reaction vessel 5 is adjusted to be higher than the atmospheric pressure so that the electrolyte 6 does not boil and has a temperature higher than the boiling point.
  • the range to be adjusted is 140 to 22 for the applied voltage.
  • 0 V that is, the electric field strength between the electrodes is 120 to 250 Vcm.
  • the frequency of the square wave is 0.01 to 100 kHz.
  • the ratio between the peak and the valley of the rectangular wave is 0.01 to 1
  • the pressure in the reaction vessel is determined at 1 to 100 atm.
  • the adjustment range varies depending on the reaction temperature and the type of the reactants. It depends on the reaction temperature, reactant This is because it differs depending on the type of the device.
  • the generation of energy is controlled by controlling the electrolytic reaction according to the present invention.
  • a radioactive substance such as trinitrate (ThNO 3) is mixed in the electrolytic solution 6 and the electrode surface with light emission and heat generation between the points cd in FIG.
  • its radioactivity can be reduced. Therefore, the present invention can be used to reduce the radioactivity of radioactive waste.
  • the type of radioactive substance to be treated varies greatly depending on the type of the reactant used in the electrolytic reaction, the shape of the reaction vessel 5 and the type of the electrolytic solution 6, but an alpha radiator is effective.
  • FIG. 3 is a schematic diagram showing an example of a heat energy utilization system incorporating the reaction cell of the present invention.
  • the system 100 shown in FIG. 3 includes a reaction cell 101 of the present invention.
  • the reaction cell 101 includes a reaction vessel 102 containing an electrolyte solution 105, and the electrolyte solution 105 of the container 102 contains a force comprising the reactant of the present invention.
  • Sword electrode 103 is immersed.
  • a cylindrical anode electrode 104 is provided so as to surround the cathode electrode 103.
  • the anode electrode 104 is preferably formed of platinum.
  • the power source electrode 103 and the anode electrode 104 are connected to the power supply PS via lines L1 and L2, respectively.
  • the reaction cell 101 is contained in a water tank 110 containing water 113.
  • a weight sensor W S is provided at the bottom of the reaction cell 101, and the weight sensor W S is connected to a control device C PU via a line L 6.
  • the water tank 110 has a low temperature water inlet pipe 111 at the bottom and a high temperature water outlet pipe 112 at the top.
  • the aquarium 110 is preferably covered on its entire outer wall with a neutron absorber 120.
  • Thermocouples TC1, TC2, and TC3 for measuring temperature are installed in the water tank 110, the low-temperature water introduction pipe 111, and the high-temperature water discharge pipe 112, respectively.
  • the pairs are connected to the control unit CPU via lines L3, L4 and L5, respectively.
  • a conduit 106 is provided-this conduit 106 is provided with oxygen generated in the reaction vessel 102 by the electrolytic reaction described above. It is used to send hydrogen and oxygen to the oxygen / hydrogen separator 130 via the pressure sensor PRS.
  • the conduit 106 is also used for sending the electrolyte from the replenishing electrolyte container 1331 to the reaction container 102 via the line L9.
  • the oxygen-Z hydrogen separator 130 is, for example, Includes a hydrogen selective permeable membrane made of palladium thin film. The mixture of the introduced oxygen and hydrogen is separated into hydrogen (H 2 ) on the permeate side and oxygen (O 2 ) on the non-permeate side by passing through the hydrogen selective permeable membrane.
  • the pressure sensor PRS is connected to the control device CPU via a line L7. Further, the control device CPU and the replenishing electrolyte container 13 1 are connected by a line 8. In response to the electrolyte weight signal detected by the weight sensor WS, the control unit CPU drives the replenishing electrolyte container 13 1 and connects the conduit 10 via line 9 to the conduit 10. Replenish the electrolyte from step 6 to keep the amount of electrolyte in the reaction vessel 102 constant.
  • the entire system 100 is controlled by controlling the power supply PS by the control unit CPU based on the signals from the thermocouples TC1, TC2 and TC3 and the pressure sensor PRS. It is done by this.
  • the high heat generated by causing the electrolytic reaction in the reaction cell 101 is absorbed by the water 113 in the water tank 110.
  • the high-temperature water that has absorbed the high heat is sent to the heat utilization facility via the high-temperature water discharge pipe 112.
  • Heat utilization equipment includes heat sources for cooling and heating in buildings and areas, and heat sources for home cooling and heating.
  • the turbine can be driven by the high-temperature water to obtain electric energy.
  • this hot water can be used as a backup heat source for electric boilers.
  • the low-temperature water used by such heat utilization equipment is It is introduced into the water tank 110 from the low-temperature water inlet pipe 111, heated again by the heat generated by the electrolytic reaction, and sent again to the heat utilization facility. In this way, the generation, extraction and use of thermal energy can be carried out cyclically.
  • a mixture of oxygen and hydrogen (O 2 + H 2) generated in the reaction cell 101 is introduced into the oxygen / hydrogen separation apparatus 130 via the pressure sensor PRS, and the apparatus 1 At 30 oxygen (O 2) and hydrogen (H 2 ) are separated. This separated hydrogen can be used as hydrogen for fuel cells.
  • FIG. 4 is a schematic diagram showing an example of a neutron utilization system incorporating the reaction cell of the present invention.
  • neutron absorbers 120 are provided with neutron passages (through holes) 121, and the rest of the configuration is the same as the system in Fig. 3.
  • An additional neutron absorber 122 is provided around the neutron passage 122 so as to thicken the neutron absorber.
  • a cancer cell is killed by accumulating a boron compound in the cancer cell and irradiating the cancer cell with neutrons from a nuclear reactor.
  • the system shown in Fig. 4 uses neutrons from the system shown in Fig. 4 instead of the neutrons from the conventional reactor by placing the patient near the neutron passage 122. You can do it. More specifically, a patient is placed in the vicinity of the neutron passage 122, electrolysis is started, and the generated neutrons are irradiated to the patient. After that, by controlling the applied voltage, Obtain neutron flux intensity. Thereafter, the electrolytic reaction is continued until the required neutron content is obtained.
  • the system shown in FIG. 4 can also use heat and hydrogen similarly to the system shown in FIG.
  • the reactant used for the force source electrode 11 was made of platinum having a purity of 99.9% and a plate having a thickness of 0.3 mm consisting of tungsten having a purity of 99.5%. A coating with a thickness of 0.1 mm was used. Platinum was used for the anode electrodes 12 and 13.
  • Fig. 5- The measurement results at this time are shown in Fig. 5-The horizontal axis is the input power when the measurement was performed every 10 seconds, and the vertical axis is the generated heat energy value. Fig. 5 As can be clearly seen, the heat energy generated is approximately 10 times as large as the input power, and the two are almost proportionally proportional to each other. You. In addition, red-violet glow emission was sometimes observed at the same time as the generation of thermal energy. Figure 5 also shows the results of measuring the relationship between the thermal energy and the input power when the glow light emission was observed. As is evident from FIG. 5, the same relationship holds when no light emission is observed.
  • the reaction temperature eventually exceeded 100 ° C., and the electrolyte 6 was brought to a boil.
  • the final input power at that time was 110 units.
  • the calculated thermal energy output was estimated to be a maximum of 1.5 kilowatts and a minimum of 0.8 kilowatts.
  • An electrolytic reaction was generated according to the method described above. Then, 150 volts and 0.4 amps Z cm 2 were applied between both electrodes, and a large amount of heat energy was generated for 6 hours in the same manner as in Example 1. Energized. After terminating the electrolytic reaction, the radioactivity of the electrolytic solution was measured. Radioactivity was measured using an ionization chamber and an alpha-ray detector. Comparing the measured value with the measured value before the reaction, it was found that the radioactivity of the stream, which is an alpha emitter, was reduced by about 30% from the value before the reaction. .
  • Neutrons were generated by an electrolytic reaction using the apparatus shown in Fig. 1.-
  • the reactant had a surface area of 1 cm2 and formed a platinum layer on the surface of a tungsten plate.
  • the electrolyte 6 was a 0.1 molar sodium carbonate heavy water solution.
  • the anode electrodes 12 and 13 were made of platinum-a discharge was generated between the electrodes to efficiently generate neutrons according to the method described above. The generated neutrons were measured using He-3 detector.
  • Figure 6 shows an example of the measurement results.
  • the horizontal axis is the time after the start of discharge, and the vertical axis is the neutron This is the number of counts.
  • neutrons are emitted 100 seconds after the start of discharge, and the number of emissions gradually increases while fluctuating. You can see that it goes.
  • the fluctuation range was always between 0 and 500k counts.
  • neutrons were sporadically generated, but gradually became continuous.
  • the number of emitted neutrons gradually increased, and it was recognized that neutrons were generated efficiently.
  • the neutron emission numbers were not stationary, but were irregular, burst-like.
  • the time during which neutrons were hardly counted continued for a while, and once the emission started, it continued to fluctuate continuously.
  • the neutron emission behavior is very similar to the heat generation behavior.
  • the present invention it is possible to generate energy with good controllability and generate neutrons efficiently by an electrolytic reaction in light water or heavy water solution. It is possible to provide a reactant having the following formula. As a result, a large amount of energy can be efficiently and continuously generated, and neutrons can be efficiently generated. Further, according to the present invention, radioactive wastes conventionally produced in large quantities by a nuclear reaction process can be efficiently and continuously treated-

Landscapes

  • Physics & Mathematics (AREA)
  • Engineering & Computer Science (AREA)
  • Plasma & Fusion (AREA)
  • General Engineering & Computer Science (AREA)
  • High Energy & Nuclear Physics (AREA)
  • Electrolytic Production Of Non-Metals, Compounds, Apparatuses Therefor (AREA)

Abstract

L'invention concerne un réacteur destiné à produire de l'énergie et des neutrons par réaction électrolytique dans une solution d'eau légère ou d'eau lourde. Ce réacteur comporte une base en métal réfractaire et, formée sur cette base, une couche métallique active contre l'hydrogène. Ce réacteur servant de cathode est immergé dans un électrolyte avec une anode. On fait passer un courant entre la cathode et l'anode afin d'entraîner une réaction électrolytique, et ainsi de produire de l'énergie thermique et des neutrons.
PCT/JP1999/001443 1998-03-20 1999-03-23 Reacteur pour produire de l'energie et des neutrons par reaction electrolytique dans une solution d'eau legere ou d'eau lourde WO1999049471A1 (fr)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
JP10/71681 1998-03-20
JP10071681A JPH11271484A (ja) 1998-03-20 1998-03-20 軽水または重水溶液中での電解反応によってエネルギーおよび中性子を発生させるための反応体およびこの反応体を用いたエネルギーおよび中性子の発生方法

Publications (1)

Publication Number Publication Date
WO1999049471A1 true WO1999049471A1 (fr) 1999-09-30

Family

ID=13467562

Family Applications (1)

Application Number Title Priority Date Filing Date
PCT/JP1999/001443 WO1999049471A1 (fr) 1998-03-20 1999-03-23 Reacteur pour produire de l'energie et des neutrons par reaction electrolytique dans une solution d'eau legere ou d'eau lourde

Country Status (2)

Country Link
JP (1) JPH11271484A (fr)
WO (1) WO1999049471A1 (fr)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US20200156182A1 (en) * 2017-07-20 2020-05-21 Ih Ip Holdings Limited Apparatus for excess heat generation

Families Citing this family (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2014037996A (ja) * 2012-08-13 2014-02-27 Tadahiko Mizuno 核融合反応方法
JP2015090312A (ja) * 2013-11-06 2015-05-11 有限会社イデアリサーチ 常温核融合反応方法及び装置
JP2017062243A (ja) * 2016-11-01 2017-03-30 水野　忠彦 核融合反応方法
JP2018036275A (ja) * 2017-10-30 2018-03-08 水野　忠彦 核融合反応方法及び核融合反応装置
JP7020255B2 (ja) * 2018-04-04 2022-02-16 日本製鉄株式会社 水素充填方法および水素脆化特性評価方法

Citations (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH02281184A (ja) * 1989-04-22 1990-11-16 Akira Fujishima 電気化学的手法による低温核融合装置用陰極およびその陰極を用いた核融合方法
WO1991018396A1 (fr) * 1990-05-17 1991-11-28 Jerome Drexler Accumulateur au deuterium pour la conversion d'energie
JPH03274487A (ja) * 1990-03-24 1991-12-05 Seiko Epson Corp 低温核融合炉
JPH0424595A (ja) * 1990-05-21 1992-01-28 Nippon Telegr & Teleph Corp <Ntt> 核融合反応方法およびその装置
JPH04157395A (ja) * 1990-10-19 1992-05-29 Matsushita Electric Ind Co Ltd 低温核融合用電極
JPH04186060A (ja) * 1990-11-20 1992-07-02 Nippon Telegr & Teleph Corp <Ntt> 発熱方法
JPH07104080A (ja) * 1993-10-05 1995-04-21 Tadahiko Mizuno 常温核融合を起こさせるための反応体及びその製造方法、並びに常温核融合を起こさせる方法及びその装置
JPH07146387A (ja) * 1993-11-25 1995-06-06 Technova:Kk 交流電流重水電解による過剰熱発生方法

Patent Citations (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH02281184A (ja) * 1989-04-22 1990-11-16 Akira Fujishima 電気化学的手法による低温核融合装置用陰極およびその陰極を用いた核融合方法
JPH03274487A (ja) * 1990-03-24 1991-12-05 Seiko Epson Corp 低温核融合炉
WO1991018396A1 (fr) * 1990-05-17 1991-11-28 Jerome Drexler Accumulateur au deuterium pour la conversion d'energie
JPH0424595A (ja) * 1990-05-21 1992-01-28 Nippon Telegr & Teleph Corp <Ntt> 核融合反応方法およびその装置
JPH04157395A (ja) * 1990-10-19 1992-05-29 Matsushita Electric Ind Co Ltd 低温核融合用電極
JPH04186060A (ja) * 1990-11-20 1992-07-02 Nippon Telegr & Teleph Corp <Ntt> 発熱方法
JPH07104080A (ja) * 1993-10-05 1995-04-21 Tadahiko Mizuno 常温核融合を起こさせるための反応体及びその製造方法、並びに常温核融合を起こさせる方法及びその装置
JPH07146387A (ja) * 1993-11-25 1995-06-06 Technova:Kk 交流電流重水電解による過剰熱発生方法

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US20200156182A1 (en) * 2017-07-20 2020-05-21 Ih Ip Holdings Limited Apparatus for excess heat generation

Also Published As

Publication number Publication date
JPH11271484A (ja) 1999-10-08

Similar Documents

Publication Publication Date Title
Mizuno et al. Production of heat during plasma electrolysis in liquid
KR20190021195A (ko) 열에너지 발생 방법, 상기 방법의 구현 장치, 및 열 발생 시스템
WO1999049471A1 (fr) Reacteur pour produire de l&#39;energie et des neutrons par reaction electrolytique dans une solution d&#39;eau legere ou d&#39;eau lourde
WO2001026117A1 (fr) Extracteur d&#39;energie thermique, fourniture d&#39;eau chaude et generateur electrique
DuFour Cold fusion by sparking in hydrogen isotopes
EP1656678B1 (fr) Generateurs pulses d&#39;electricite par reactions nucleaires de faible energie
JP3637039B2 (ja) 水素ガスの発生方法および水素ガス発生装置
JP2004003973A (ja) エネルギー／物質変換方法と構造
Kim et al. Investigation of the characteristics of a stacked direct borohydride fuel cell for portable applications
Takahashi et al. Excess heat and nuclear products by D2O/Pd electrolysis and multibody fusion
JP2004337843A (ja) 水素同位体水の濃縮方法及び装置
JP3443237B2 (ja) 固体高分子型燃料電池発電システム
US8071248B2 (en) Structure and method for optimizing system efficiency when operating an SOFC system with alcohol fuels
Dufour et al. Interaction of palladium/hydrogen and palladium/deuterium to measure the excess energy per atom for each isotope
JPS63236269A (ja) 燃料電池制御方法
AU2015296800B2 (en) Fluid heater
JP2007026927A (ja) 燃料改質器および燃料電池発電装置
Will et al. Studies of electrolytic and gas phase loading of palladium with deuterium
JP2006058204A (ja) 水素製造装置
WO2017061903A1 (fr) Recombineur et procédé de recombinaison d&#39;hydrogène ou de méthane et oxygène dans un mélange gazeux
JPH05196201A (ja) Ｐ／ｆ効果を利用した蒸気原動機
Todorovski et al. Design and testing of a water-methanol evaporator for integration in a methanol steam reforming-high temperature proton exchange membrane fuel cell system
JPH0527062A (ja) 異常熱の発生方法
KR20220087224A (ko) 발전 잠열을 이용한 수증기 전기분해 수소 생성 장치 및 이를 이용하여 생산되는 수소의 생산량 예측 방법
JPH07120574A (ja) 発熱装置

Legal Events

Date Code Title Description
AK Designated states

Kind code of ref document: A1

Designated state(s): US

AL Designated countries for regional patents

Kind code of ref document: A1

Designated state(s): DE FR GB

DFPE Request for preliminary examination filed prior to expiration of 19th month from priority date (pct application filed before 20040101)
121 Ep: the epo has been informed by wipo that ep was designated in this application
122 Ep: pct application non-entry in european phase