JP2008274378A - Method and apparatus for conversion of water into clean combustible gas for use as additive of fuel - Google Patents

Abstract

<P>PROBLEM TO BE SOLVED: To provide production equipment or a system and method for combustible gas formed from water and used in internal combustion engine systems, in other fossil fuel engine systems, in gaseous welding systems and other similar systems. <P>SOLUTION: In an electrolyzer 2 equipped with: an electrolysis chamber 4 for accommodating an electrolyte solution; one or more anode electrodes 14; one or more cathode electrodes; and one or more supplemental electrodes 24-30 or the like, which are at least partially immersed in the electrolyte solution, a clean combustible fuel composed of hydrogen, oxygen and their bonds, called HHO or hydrogen-enriched gas is formed with a high efficiency by electrolyzing the electrolyte solution using distilled water. The formed combustible fuel can be used as an additive to combustion engine fuels or in flame generating equipment such as torches and welders. <P>COPYRIGHT: (C)2009,JPO&INPIT

Description

  The present invention can be used in internal combustion engine systems, fossil fuel engine systems, gas welding systems and other similar systems, and treats water or distilled water into a gas combustion form of combustible HHO gas generated from water, The present invention relates to a system and a method thereof. Moreover, this invention relates to the form of the combustible HHO gas produced | generated with the electrolytic cell or gas generator connected to these systems.

  The field of the invention is a vast number of patent subjects. Among the prior art covered by this patent are U.S. Pat. No. 4,014,777, which was patented to Yul Brown on March 29, 1977 under the name “Welding”, and “Arc assisted hydrogen / oxygen” on March 28, 1978. U.S. Pat. No. 4,081,656 patented to Yul Brown under the name of "welding" and other patents. In this field, as in many literatures described later, “brown gas” is composed of conventional hydrogen gas and oxygen gas having an accurate stoichiometric ratio of 2/3 hydrogen to 1/3 oxygen. Defined as combustible gas. The combustible gas of the present invention clearly and reliably differs from the brown gas.

  Electrolytic equipment and methods for separating water are also subject to numerous patents, including Michael McCambridge under the name “electrolysis of water” on February 23, 1988. U.S. Pat. No. 4,726,888, and Gene B. on the name of “hydrogen / oxygen fuel cell” on August 3, 1995. There are US Pat. No. 5,231,954 patented to Stow and US Pat. No. 5,401,371 patented to Yujiro Oshima on March 29, 1995 under the name of “hydrogen generator”.

  The present invention has novelty that is clearly different from the prior art. These prior art are facilities and methods for the treatment of water into a fuel, which has a conventional gaseous fuel, i.e. a conventional chemical composition or mixture of molecules, called "brown gas". In contrast, the present invention provides a methodology as a related process for producing a new fuel, or HHO combustible gas, comprised of equipment or systems and chemical species beyond conventional molecules, where the fuel has a unique form It is produced from water using an electrolytic cell.

  The present invention relates to the structure, properties and application of a new clean combustible gas, called HHO gas, produced from distilled water using the following electrolytic cell.

  The brown gas or other gas produced in existing electrolyzers and the HHO gas are clearly different despite many similarities. In fact, brown gas or other gas is a combination of conventional hydrogen gas and conventional oxygen gas, that is, a conventional molecular structure having an exact stoichiometric logic ratio of 2/3 hydrogen to 1/3 oxygen. It is gas which has. In contrast, HHO gas does not have an exact stoichiometric ratio, but instead has a “magnecular” property with the presence of clusters at a macroscopic ratio that cannot be explained by ordinary valence bonds. It has the structure which has. As a result, the element clusters of brown gas and HHO gas are clearly different in proportion and chemical composition, as shown below.

  The first feature of the electrolytic cell of the present invention is its efficiency. For example, with as little as 4 kwh, the electrolyser rapidly converts water to 55 standard cubic feet (scf) of HHO gas at a rate of 35 pounds per square inch (psi). By using electricity on an average daily basis at a rate of 0.08 US dollars / kwh, the efficiency of the electrolyzer is a direct cost of 0.07 US dollars / standard cubic foot (scf) of HHO gas. As a result, this HHO gas is superior in price compared to existing fuels.

  In direct inspection, the result is that HHO gas is odorless, colorless and lighter than air. The first feature of the generation of HHO gas is that there is no evaporation of water, and water is directly converted to HHO gas. In any case, the amount of power used in the electrolytic cell is essentially unnecessary for water evaporation.

  This feature alone indicates that the electrolytic cell produces a gas-flammable “new form of water”. The purpose is also to confirm the unknown chemical composition of the generated HHO gas as the first important feature, its relation to the electrolytic cell and some initial applications.

  The second feature of HHO gas is that it shows a “highly varying energy content” in British Thermal Units (BTU), and can accommodate a relatively low temperature combustion outdoors and a large release of thermal energy depending on use. And this 2nd characteristic is a direct confirmation that it has novelity fundamentally in terms of the chemical structure of HHO gas.

  In fact, all known fuels have a “fixed energy content”, ie similar BTU / scf values for all uses. Also, the characteristic that the energy content of the HHO gas is variable is clear evidence that the structure has a molecular characteristic rather than a molecular structure, that is, that the chemical composition includes bonds beyond the valence type.

  A third important feature of HHO gas is that it contains all the oxygen needed inside, so no oxygen is needed for combustion. Other fuels require atmospheric oxygen for combustion and cause a serious environmental problem known as “oxygen deficiency”, which makes combustion without oxygen deficiency an environmental There is the importance of above.

  The fourth important feature of HHO gas is its unique adhesion to gases, liquids and solids, as will become apparent in the following experiments, and this adhesion serves as an additive to improve the desired quality. There are particularly effective uses.

  The fifth feature of HHO gas is that it follows all basic gases, i.e. those having a molecular structure, because the HHO gas begins to deviate from the basic PVT method at about 150 square inches (psi). First, it becomes liquid at a high pressure of 250 square inches (psi) or more. This feature is further investigated for development and commercial development.

  The sixth feature of HHO gas is that it significantly increases the heat content as well as the exhaust environmental standards for gaseous fuels such as natural gas, gas fuel and other fuels and liquid fuels such as diesel, gasoline, mineral oil and other fuels. It can be combined with these gaseous and liquid fuels for improvement.

  The seventh feature of HHO gas is that it dissolves tungsten, bricks and other highly refractive materials almost instantaneously. In particular, this measurement has the remarkable property of almost instantaneously reaching 9000 ° C., that is, the temperature in the solar chromosphere where all the matter on the earth can be sublimated by HHO gas.

  The present invention also includes an electrolytic cell for separating water. In one embodiment, the electrolytic chamber includes water and an electrolyte, and the electrolytic chamber is partially filled so that a gas storage region is formed in the upper portion. An aqueous electrolyte; two main electrodes having an anode electrode and a cathode electrode, at least partly immersed in the aqueous electrolyte; at least partly immersed in the aqueous electrolyte and disposed between the two main electrodes; A plurality of auxiliary electrodes held in a fixed positional relationship are provided between these two main electrodes, and the electrolytic cell is composed of hydrogen atoms and oxygen atoms, and is generated from valence bonds and circular polarization of electron orbits. The flammable gas which is a chemical species caused by the coupling by the attractive force between the opposing magnetic poles is generated. Further, as shown in FIG. 19, these main electrodes and auxiliary electrodes can be easily replaced by a relatively simple design of metal such as a planar rectangular shape or a square shape. The hydrogen oxide combustible gas is recovered in the gas storage area so that it can be sent to the fuel system of the internal combustion engine.

  The present invention can be used to improve the fuel efficiency of an internal combustion engine. The method for improving the fuel efficiency of the internal combustion engine uses any one of the electrolytic cells described in the embodiments together with the internal combustion engine. A potential is supplied to the electrode of the electrolytic cell, and a combustible gas is generated in the electrolytic cell. The combustible gas is then combined with the fuel in the fuel system of the internal combustion engine before the fuel is consumed by the internal combustion engine.

  Another embodiment of the electrolytic cell has an electrolytic chamber for holding an electrolytic solution. The electrolysis chamber is connected to the cover by a flange. A seal is preferably provided between the electrolysis chamber and the cover, and this seal is a neoprene gasket and is disposed between the flange and the cover. The electrolyte may be an electrolyte that produces a mixture of an aqueous electrolyte and a novel gas. However, it is preferable to use distilled water as the electrolytic solution in order to generate a new and unique gas.

  The electrolyte is partially filled into the electrolytic chamber during operation to the amount that the gas storage area is formed on the aqueous electrolyte. The electrolytic cell includes an anode electrode and a cathode electrode, which are two main electrodes at least partially immersed in an aqueous electrolyte. These anode electrode and cathode electrode are inserted into grooves in the rack. This rack is installed in the electrolytic chamber. One or more auxiliary electrodes are also installed in the rack. In addition, at least a part of these auxiliary electrodes is immersed in an aqueous electrolytic solution, and is arranged between the anode electrode and the cathode electrode. Further, the anode electrode, the cathode electrode, and the auxiliary electrode are held at fixed positions by a rack. The anode, cathode, and auxiliary electrode are preferably separated from each other by a distance of about 0.25 inch. The plurality of auxiliary electrodes allow for efficient generation of the gas mixture. It is preferable that 1 or more and 50 or less auxiliary electrodes are arranged between the two main electrodes. Further, it is more preferable that 5 or more and 30 or less auxiliary electrodes are arranged between these two main electrodes, and it is most preferable that about 15 auxiliary electrodes are arranged. Each of these two main electrodes is preferably a metal wire mesh, a metal plate, or a metal plate having one or more holes. Each of these two main electrodes is more preferably a metal plate. Suitable metals for forming these two main electrodes include, but are not limited to nickel, nickel alloys or stainless steel. The preferred metal for these two main electrodes is nickel. The plurality of auxiliary electrodes are preferably a metal wire mesh, a metal plate, a metal plate having one or more holes, or the following foam material. Each of the plurality of auxiliary electrodes is more preferably a metal plate. Suitable metals for forming these auxiliary electrodes include, but are not limited to, nickel, nickel alloys, stainless steel, and the following foam materials.

  In a more preferred embodiment, the auxiliary electrode is a highly porous foamed material substantially formed of a nickel material, that is, an electrode formed in a composite network using nickel fibers or powder and a foamed material. However, it may be formed of a porous electrode having a high porosity in which 99% or more of nickel is contained in the foamed material. A material for this type of auxiliary electrode is INCO (registered trademark) nickel foam C.A.S No. 7440-02-0 manufactured by Inco Special Products of Wyckoff, NJ. Generally, the nickel content of this nickel foam can be changed from 25% to 85% at a density of 1.0 g / cc to 2.70 g / cc. Here, the nickel content of 99% or more in the nickel foam material and the nickel content of about 14% in the stainless steel plate were excellent when generating a new hydrogen oxide combustible gas as described later. Results are shown. Furthermore, one of the adjacent auxiliary electrodes is formed of a foam material, and the other auxiliary electrode facing the auxiliary electrode is formed of a substantially stainless steel material. These auxiliary electrodes are formed of all the electrodes in the electrolytic cell. It creates a new current or positive (+) and negative (-) ion flow that causes the formation of a single combustible gas across the surface area on both sides. These auxiliary electrodes can be configured in other configurations, but have been found to be very effective when generating the desired hydrogen oxide gas.

  During the operation of the electrolytic cell, a voltage is applied between the anode electrode and the cathode electrode, and a new gas is generated and collected in the gas storage region. The gas mixture stored in the gas storage area passes through the outlet, exits the gas storage area, and is finally supplied to the fuel system of the internal combustion engine. The anode electrode is in electrical contact with the contactor, and the cathode electrode is in electrical contact with other contactors. The contactor is made of metal, and a groove is formed in the path so as to be located on the anode electrode and the cathode electrode. The contactor is attached to a rod inserted through a hole provided in the cover. These holes are threaded and the rod is a threaded rod that is screwed into the holes. Since the anode electrode and the cathode electrode are held at predetermined positions by paths and grooves in the rack, the contactor also holds the rack. Therefore, when the cover is bolted to the electrolysis chamber, the rack is held at the lower part of the electrolysis chamber. The electrolyzer optionally has a pressure relief valve and a level sensor. The pressure relief valve releases the gas mixture in the gas reservoir before the pressure increases excessively. The level sensor sounds an alarm when the electrolyte is too low and reliably stops the flow of gas to the vehicle fuel system. When there is little electrolyte solution, an additional electrolyte solution is added from a water inlet. Moreover, the electrolytic cell may be equipped with the pressure gauge so that the pressure of an electrolysis chamber may be monitored. Further, the electrolytic cell optionally has one or more fins that remove heat from the electrolytic cell.

  In this electrolytic cell variant, the first group of one or more auxiliary electrodes is connected to the anode electrode by a first metal conductor, and the second group of one or more auxiliary electrodes is a second one. It is connected to the cathode electrode by a metal conductor. The anode electrode, the cathode electrode, and the auxiliary electrode are held on the rack by the holder rod, and are inserted into the path in the rack groove. This rack is preferably made of a highly dielectric plastic such as polyvinyl chloride (PVC), polyethylene or polypropylene. Further, the rack holds the anode electrode, the cathode electrode, and the auxiliary electrode in a certain positional relationship. The fixed positional relationship between the two main electrodes and the plurality of auxiliary electrodes is that the electrodes of the two main electrodes and the plurality of auxiliary electrodes are substantially parallel, and each of these electrodes is about 0.15 inches or more and about 0.35. It is preferable that the distance is less than an inch away from the adjacent electrodes. Further, it is more preferable that these electrodes are separated from adjacent electrodes by a distance of about 0.2 inch or more and about 0.3 inch or less, and most preferably about 0.25 inch. This fixed positional relationship is held by a rack that holds these electrodes. Each of these electrodes is mounted in a rack groove that defines the electrodes apart. Furthermore, each of these electrodes or racks can be removed from the rack so that they can be replaced as needed. Further, as described above, the rack, the anode electrode and the cathode electrode are held at predetermined positions, and the auxiliary electrode is also fixed to the rack by the holder rod, so that these auxiliary electrodes are also held at the predetermined position.

  In operation, a new combustible gas is generated by electrolysis of the electrolyte in the electrolytic cell. The electrolytic cell is connected to the recovery tank by a pressure line. The combustible gas is recovered and temporarily stored in the recovery tank. The recovery tank is optionally equipped with a pressure relief valve that can protect against any excessive pressure increase. The recovery tank is connected to the solenoid by a pressure line. The solenoid is sequentially connected to the engine intake manifold by a pressure line. In order to prevent the flame from spreading in the pressure line, a flash protection is optionally attached to the pressure line. Furthermore, the pressure line has a hole that restricts the flow of gas mixture into the engine intake manifold. The size of this hole depends on the size of the engine. For example, a hole diameter of about 0.04 inch is suitable for a 1 liter engine, a hole diameter of about 0.06 inch is suitable for a 2.5 liter engine, and a hole diameter of about 0.075 inch is Suitable for V8 engine. The voltage applied to the electrolytic cell is supplied by the electrolytic cell battery via a solenoid. When the pressure in the recovery tank drops below about 25 psi, the solenoid switches and a voltage of about 12V is applied between the anode and cathode electrodes. The battery insulator allows the vehicle battery and the electrolytic cell battery to be charged by the AC generator, and maintains the electrical insulation of the electrolytic cell battery and the vehicle battery. Furthermore, when the main switch is activated, power is supplied to the solenoid by the vehicle battery. When the vehicle battery supplies power to the gas mixing solenoid and the gas mixture is supplied to the engine intake manifold, the gas mixing solenoid opens. The solenoid receives feedback from a level sensor that stops gas flow when the amount of electrolyte in the electrolytic cell becomes too small. Furthermore, when used in a vehicle, the operation of the vehicle's oxygen sensor needs to be adjusted to account for the additional oxygen added from the electrolytic cell to the fuel system. Typically, if the oxygen sensor senses more oxygen, the vehicle computer determines that the engine is running at an incline and opens the fuel injector so that there is more fuel mixture. This is not appropriate and causes a reduction in fuel efficiency.

  Another embodiment of the invention is a method for improving the fuel efficiency of an internal combustion engine. In this method, the above-described electrolytic cell is used together with the internal combustion engine. In particular, the method includes the steps of preparing the above electrolyzer system, and a new combustible gas is generated and recovered in the gas storage area, so that the electrolyzer delivers the combustible gas to the fuel system of the internal combustion engine. Applying a voltage between the provided electrodes and mixing the fuel in the fuel system of the internal combustion engine with the generated combustible gas. There is also a step of adjusting the operation of the oxygen sensor described above.

  In other embodiments, the electrolyzer or gas generator is incorporated into a weld cut combustion system, other types of systems, or engine systems. These systems include an electrolyte container having an upper portion and a lower portion and having an electrolyte therein. Here, the electrolytic solution is preferably water. The electrolyte container includes a torn or permeable plate that is positioned to seal around the top of the electrolyte container. This plate has a function of releasing the gas pressure in the electrolyte container when a predetermined pressure value is exceeded.

  The self-generated hydrogen oxygen gas generation system includes a pump, preferably an electromagnetic pump, having one end connected to the lower part of the electrolyte container. The other end of the pump is connected to at least one hydrogen and oxygen electrolyzer generator having a conductor therein. One end of this conductor is grounded. Further, the other end on the opposite side of the conductor is electrically connected to one end of the pressure controller. Furthermore, the other end of the conductor is electrically connected to a power source. The pump has a function of circulating the electrolyte solution from the electrolyte container through the gas pipe, through the radiator, through the at least one hydrogen and oxygen electrolytic cell generator and back to the electrolyte container. The radiator has a function of cooling the generated hydrogen and oxygen gas before returning to the electrolyte container.

  The pressure controller is connected to the electrolyte container and monitors the pressure in the electrolyte container. When the gas pressure in the electrolyte container exceeds a predetermined value, the current is processed by the conductor in the hydrogen and oxygen electrolyzer generator to stop the generation of hydrogen oxygen gas. When the gas pressure in the electrolyte container falls below a predetermined value, the current is processed by the electrical conductor in the hydrogen and oxygen electrolyzer generator to initiate the generation of hydrogen oxygen gas. The pre-determined value is less than the value required to cause pressure release through the plate.

  This self-generated on-demand hydrogen oxygen generation system has a check valve connected at one end to the upper end of the electrolyte container below the plate. Further, the other end of the check valve is connected to the drying filter means or the tank.

  In addition, the system includes other dry filter means or tanks in fluid communication with one end of the electrolyte container on the plate, and further to the other check valve via a gas line. The other end is connected. The other end of the gas pipe is connected to other dry filter means or a tank.

  In addition, the system has a pressure reducing valve in which one end of the system is communicated with the upper end of the electrolyte container so that the fluid can move, and the fluid is able to move with respect to the gas pipe. The gas pipe is connected to the radiator.

  The welding system further includes a direct current amperage adjustment device controlled by a microprocessor provided to regulate direct current amperage from the power source to the hydrogen and oxygen electrolyzer generator. The first disconnection switch controlled by the microprocessor is used to stop the supply of power to the welding machine in response to a pump abnormality.

  A second disconnect switch controlled by the microprocessor is used to stop the supply of power to the welder in response to insufficient electrolyte conditions in the electrolyte container. A microprocessor controlled liquid crystal display is used to display operational statistics related to the welding system including operating time, amperage values, indicator lights and pressure gauge readings. The liquid crystal display receives input from a plurality of positions in the system.

  A microprocessor-controlled polarity change system is used to change the polarity of conductors located in the hydrogen and oxygen electrolyzer generator. A microprocessor controlled cooling system is used to operate the generator fan and pump, and continues fan and pump operation throughout the entire cooling phase following manual shutdown of the system.

  The generated gas or HHO gas is finally sent from the drying means to the gas reservoir tank. The drying means is merely an example. In order to effectively achieve the same purpose, it may be designed as the same unit. The gas is then fed directly to the engine or, in this case, the welding device, via a gas tube, a check valve that is a hydrogen flush suppression check valve and a control valve.

  As described above, the flames from the hydrogen and oxygen species generated in the electrolyzer can instantly dissolve solids without using atmospheric oxygen. Similarly, the generated combustible gas can be used as a fuel without using atmospheric oxygen, and can be combined with other substances by magnetic induction.

  Further, the combustible gas is composed of a combination of hydrogen atoms and oxygen atoms due to the circular polarization of the orbit, and is combined with the fossil fuel. This coupling is due to magnetic polarization caused by at least some of the resulting attractive forces between fossil fuel trajectories and opposite magnetic properties. Furthermore, the combined body of fossil fuel and combustible gas generates less pollutants than the case where only fossil fuel is burned alone, and has a lot of thermal energy.

  An outline of the scientific expression of the main features of HHO or hydrogen oxide gas is given below without using a simple formula that can be easily understood.

Using the special electrolysis process described below, HHO gas is produced from distilled water, which is typically 2/3 (66.66 vol%) hydrogen (H ₂ ), 1/2 ( 33.33% by volume) oxygen (O ₂ ).

The conventional H ₂ gas and O ₂ gas mixture is not certain to exhibit the characteristics of HHO gas, so the generated HHO gas is novel and unique.

In this regard, any possible question can be resolved by comparing the nature of the HHO gas with a mixture of 66.66% H ₂ and 33.33% O ₂ . Under any condition, the mixed gas of 66.66% H ₂ and 33.33% O ₂ cannot cut tungsten or dissolve bricks instantaneously like HHO gas, so that the generated HHO It can be seen that the chemical structure of the gas is novel.

  In order to confirm that the HHO gas is new, special features of the HHO gas, such as instantly dissolving tungsten, bricks, etc., are that HHO is “atomic hydrogen”, ie as shown in FIG. , Not only individual H atoms with no valence bonds to other atoms, but also “magnetically magnetized atomic hydrogen”, ie electrons are magnetized, as shown in FIG. It contains hydrogen atoms that rotate in the annular plane rather than in the spatial direction.

  It has been shown that the presence of “atomic hydrogen” can be assumed in the brown gas. However, it is the following explanation that this feature is insufficient from the calculation to explain all the features of the HHO gas. Therefore, the basic novel point is to use “magnetized atomic hydrogen” as shown in FIG. 1b.

Further, when hydrogen contained in the HHO gas is bonded to other atoms, as shown in part in FIG. 2a, the size of H ₂ molecules generated by thermal rotation is a deeper layer of tungsten or brick. This prevents rapid penetration of hydrogen into the interior and prevents rapid dissolution of these tungsten or bricks. The only known configuration of the hydrogen molecule corresponding to the physicochemical explanation described above is an orbit limited to rotate in the XX-shaped annular surface, as shown in FIG. Is magnetized.

  Indeed, the magnetized hydrogen atoms shown in FIG. 1b and the magnetized hydrogen molecules shown in FIG. 2b are thin enough to rapidly penetrate into deeper layers of material. Furthermore, the magnetic field generated by the rotation of the electrons in the annular surface magnetizes the material trajectory when approaching by magnetic induction. However, the magnetized tracks of tungsten and brick are substantially stationary. Thus, magnetic induction occurs naturally deep within the material by the rapid self-propelling forces of magnetized hydrogen atoms and molecules.

And the H atoms do not have the spherical distribution shown in FIG. Eisenberg and W.W. As shown in Kawsman's "Water Structure and Properties" (Oxford University Press, 1969), the symmetry plane shown in Fig. 3a is shown in Fig. 1b along an annular plane perpendicular to the H-O-H plane. It has the property of a water molecule H ₂ O═H—O—H having a magnetized distribution.

  In addition, the H—O—H molecule has a negative charge density localized in the O atom and a supplementary and dominant localized in the hydrogen atom even if the charge is zero, depending on the temperature and pressure. It is known to have high “electromagnetization” with a high positive charge density, ie a deformation of the charge distribution. This means the repulsive action of the H atom caused by the dominant positive charge, and a singular angle of 105 ° between the HO and OH dimers, as shown in FIG. 3a. To form.

  However, the circular polarization of the H atom orbit in the configuration shown in FIG. 1b is a very strong magnetic field with a magnetic field value about 1415 times larger than the rotation axis perpendicular to the plane of the annular surface and the magnetic moment of the H nucleus (proton). Therefore, it has a value exceeding the repulsive force due to the electric charge.

  Then, in the natural configuration of H—O—H molecules, the strong electromagnetization that occurs in oxygen results in a repulsive action by two H atoms in the H—O—H structure, resulting in H It weakens the magnetic field of the circular polarization of the orbit.

  However, as soon as the strong electromagnetization of HO—H disappears, a very strong attractive force between the opposite polarities of the magnetic field of the magnetized H atom is dominated by the repulsive action of Coulomb by the charge, The new configuration shown in FIG.

  Thus, the electrolytic cell allows the conversion of water molecules from the conventional H-O-H configuration shown in FIG. 3a to the new configuration shown in FIG. 3b, and the new configuration shown in FIG. In the absence of magnetisation, this is possible because the attractive force between magnets opposite the orbital ring distribution is much stronger than the repulsive action of Coulomb by electric charges.

  By representing the valence bond with “-” and the magnetic bond with “x”, the water molecule is represented as H—O—H, as shown in FIG. 3a. Also, the HHO gas is represented as H × HO as shown in FIG. 3b. As a result, R.I. M.M. According to Santilli's “Basics of Hadron Chemistry” (Kulwa Academic Publishing Co., Ltd., 2001), since all bonds are valence type, H—O—H is a “molecule”, while 1 Since H is a magnetic type, H × HO is a special “Magnecule”.

  The effectiveness of the water molecule rearrangement is readily apparent from the fact that when the H—O—H species is a liquid, the new H × HO species can be readily proved to be a gas. The fact that this H × HO species is a gas is due to various reasons such as the atomic mass unit (amu) ratio of hydrogen of 1 to 16 and much lighter than oxygen. As a result, from a thermodynamic point of view, the conversion from liquid to gas implies a well-known increase in entropy, so the new H × HO species is sufficient for conventional thermodynamic laws. And is approximately equal to ordinary oxygen gas. This feature does not require evaporation energy and is explained from the generation from a special gaseous new form of water electrolyser.

  Also, the conversion from the H—O—H configuration shown in FIG. 3 a to the H × H—O configuration shown in FIG. 3 b has another reason to mean the necessary conversion from liquid to gaseous. The technical literature cited above, e.g. Eisenberg and W.W. As described by Kawsman, the fact that water is in a liquid state at atmospheric temperature and atmospheric pressure is caused by the presence of “attraction between hydrogen atoms of different water molecules”, so-called “hydrogen bonding”.

  However, the above description of the liquid state of water remains a conceptual concept because it clearly lacks confirmation of the “attraction” between the different H atoms required to exist in liquid form. Since the only available electrons in the H atom are fully used for bonding in the H—O—H molecule, the attractive force of these electrons cannot be of valence type. Therefore, the bonding force in this H—O—H molecule cannot reliably be a valence type.

  Confirmation of attractive force by hydrogen bonding of liquid water can be confirmed by the second document R.C. M.M. It is done in Santilli, and the repulsive Coulomb force exceeds the repulsive Coulomb force, which is due to the attractive force between the opposite polarities of the annular distribution of the very strong trajectory, which certainly results in a magnetic type.

  Another difference is that two H atoms in which the conversion from the H—O—H configuration to the new H × H—O configuration forms an “internal hydrogen bond” rather than the usual “external bond” with other H atoms. Is substantially caused by. The first point is an accurate confirmation of “physical source of attraction” that is not just a scientific term, as is the case with “numerical value”.

  In view of the above, it is clear that the conversion from the HO—H configuration shown in FIG. 3 a to the H × HO configuration shown in FIG. 3 b means all possible hydrogen bond decays. In some cases, HxHO magnetic is no longer liquid from atmospheric temperature and atmospheric pressure. The fact that this H × H—O magnecle is not liquid at atmospheric temperature and pressure is due to the rotation of the H × H dimer around the O atom, for example, when stable hydrogen bonding does not occur.

  As a result, the conversion from the conventional HO—H configuration shown in FIG. 3a to the new H × HO configuration shown in FIG. 3b means a clear conversion from liquid to gaseous.

  The first and most important confirmation of the present invention is that the removal of the electromagnetization of water molecules is due to the evaporation of water along with the conversion that occurs as a result of the H—O—H configuration to the new H × HO configuration. It does not require the large amount of energy required and can be achieved with the minimum energy available in the electrolytic cell.

  While it is clear that conventional H—O—H species are stable, H × H—O, which has a novel structure, is unstable due to, for example, temperature collisions. And to separate. The latter H × H constitutes a new chemical “species”, referred to below as detectable “clusters” that make up the HHO gas, not the conventional molecular type shown in FIG. 4a, but as shown in FIG. The xH bond arises from the attractive force between the opposite magnetic polarities as described above when the annular track is overlaid.

  H × H, which is a new chemical species, is another novel point because it surely has magnetized atomic hydrogen that requires the above physicochemical explanation. These H × H magnetizations occur naturally in water molecules, and are in a useful form mainly by the new electrolytic cell.

  The individual magnetized atomic hydrogen, as shown in FIG. 1b, causes these hydrogen atoms to instantaneously recover the spherical distribution shown in FIG. 1a by rotation with temperature, so that they are very unstable when separated. It becomes.

  However, if two or more magnetized H atoms are bonded as shown in FIG. 4b, this combination is completely stable at ambient temperature because all of the rotation occurs due to the bonded H atoms. Next, since the radius of the former H × H species is the radius of the H atom, the size of the H × H species becomes half the size of a normal H molecule under the rotation by temperature, The radius of the latter H—H species is the diameter of one hydrogen atom. Similarly, this reduction in size is important to explain the characteristics of HHO gas.

  Needless to say, it can be proved by quantum chemistry that H × H species can be 50% to convert into conventional H—H molecules. Thus, the hydrogen content of the HHO gas is expected to be due to a mixture of 50% H × H and 50% H—H under certain conditions.

  HH molecules have a mass of 2 atomic mass units (amu). Bonds in HxH are significantly weaker than H-H valence bonds. Therefore, the H × H species is predicted to be heavier than the conventional one HH because the binding energy is negative. However, since this difference is a slight value of about 1 amu, it exceeds the detection capability of currently available analytical instruments based on single mass detection. The HxH and H-H species then appear identical under conventional mass spectroscopy measurements because both have a mass of 2 amu.

  The H × H species have distinct magnetic properties that are not present in the H—H species, and allow separation and discrimination between the H × H species and the H—H species, so that two H × H species and H The separation and detection of -H molecules requires very accurate analytical equipment with magnetic resonance. The description of the experiment here is based on conventional mass spectrometry.

  It should also be noted that the weak nature of the bond H × H over the conventional valence bond H—H is important for the physicochemical explanation. This only explanation for H × H is possible with “magnetized atomic hydrogen”, ie separated hydrogen atoms without valence bonds with the magnetisation shown in FIG. 1b.

  In view of the strong valence bond HH that must collapse as a necessary state for any chemical reaction, the conventional hydrogen molecule HH cannot be accurately described physicochemically as described above. Is clear. In comparison, the much weaker magnetic bond H × H readily releases individual hydrogen atoms, as required to accurately present experimental data. In fact, the conventional H—H species cannot be explained at all as described above, so this explanation is based on the existence of a novel H × H species that is the only physicochemical basis that can explain the HHO gas. It is a very strong thing that reveals what to do.

  The situation of the oxygen atom following the separation in the H—O—H molecule is almost similar to the situation of hydrogen. When oxygen is part of a H—O—H molecule, the two valence orbitals of this oxygen are distributed in all directions in space, but to an annular plane parallel to the corresponding magnetisation of the H atom. Has magnetism.

  As soon as the valence bond of one H atom collapses, the two H atoms collapse one in the HxHO species, and the orbits of the two valence electrons of the O atom are correspondingly aligned. It is thought that it is done. This means that upon separation of the HxHO species into HxH and O, oxygen has a distinct magnetisation of valence orbitals along parallel annular faces. Furthermore, oxygen is paramagnetic and reacts well to the cyclic polarization of valence electrons by magnetic induction in a magnetic field.

  Next, the oxygen contained in the HHO gas first becomes a novel magnetic OxO species, and there is a possibility that the conventional molecular species OO may be converted by about 50%, and under certain conditions 50% -50% The ratio results in a mixture of OxO and O-O.

  The OO species has a mass of 32 amu. Also, the new OxO species, like HxH, has a mass greater than 32 amu due to a decrease in the absolute value of the binding energy (negative) and a resulting mass increase. However, this mass increase is less than 1 amu and cannot be detected with currently available mass spectrometers.

  It can be easily understood that the HHO gas cannot be constituted solely from the mixture of H × H / H—H gas and O × O / O—O gas confirmed above, and a large number of species can be added. This large number of species can be added because the valence bond is broken when all the valence electrons in the molecule are used, and when this valence bond is broken, no additional atoms can be added. . On the other hand, in the magnetic coupling such as the H × H type shown in FIG. 4B, there is no limit to the number of elements other than the temperature and pressure.

  Therefore, the presence of the following new species in the HHO gas is predicted from the increasing amu value.

  First, the existence of a new 3 amu species consisting of H × H × H is predicted, as is the case with the H—H × H species. Hydrogen has only one valence electron and only a balanced bond occurs in pairs like H-H, so that the triple-valence bond H-H-H is prohibited. Impossible.

  Thus, the 3amu species consisting of 3 H atoms has already been confirmed in mass spectrometry, and the molecule H-H-H is impossible, so that it is Magnecur H × H-H. It becomes confirmation of.

  Next, there is a trace prediction of a 4 amu species that is not helium (because there is no helium in the water), which is Magnecur (HH) × (HH), which has approximately the same atomic mass as helium. Due to the general lack in the HHO gas of magnetized hydrogen molecules H—H required for the generation of (H—H) × (H—H) species (H—H) ) X (H-H) species are expected to exist.

  Additional species with 4 or more hydrogen atoms are possible, but these additional species with 4 or more hydrogen atoms are very unstable under temperature collisions and are present in HHO gas for 1 million minutes. 1 is predicted. Therefore, it is predicted that there are not so many species in the HHO gas between 4 amu and 16 amu. In addition, the part below 16 amu shows oxygen.

  The next species expected in HHO gas is Magnecule HxO, which has 17 amu and has a conversion rate of 50% over conventional radical HO. Since this HxO species occurs in all separations of water, a detectable trace is expected.

  The next species expected for HHO gas is a novel magnetic configuration of water H × HO species shown in FIG. 3b with a mass of 18 amu. The difference in vapor state between this H × HO species and the conventional water molecule HO—H species can be easily confirmed by an infrared detector and other detectors.

  The next species expected for HHO gas has a mass of 19 amu and is a trace amount of Magnecule HxHOOH, or HxHOOH. A further possible species is the H × H—O—H × H species with a mass of 20 amu.

  Heavier species are produced by the main magnetic compounds present in HHO gas, ie, H × H and O × O. Therefore, there is a great possibility that 34 amu seed H × HO—O × O and 35 amu seed H × HO—O—H exist.

  The latter species H.times.HO.times.OH is composed of two conventional dimer HOs of water molecules, as shown in FIG. 5, and the magnetisation of these two dimer HOs. Hydrogen is added by the same magnetic law under the bond that occurs in the opposite polarity of the valence orbital magnetic field.

  Although m and n are expected to be in ppm, the heavier species added is represented by the simple formula m × 1 + n × 16 amu, where m and n are 0 unless both m and n are 0. These are positive integer values.

  In short, the experiment outlined below confirms the newness by direct measurement and relates to the prediction that the HHO gas is composed of:

  i) One of the two major species is a large proportion of less than 66% by weight of 2 amu (representing a mixture of H × H and H—H), and the other is a large proportion of less than 33% by weight of 32 amu (O X represents a mixture of O and O-O).

  ii) 1 amu represents separated atomic hydrogen, 16 amu represents separated atomic oxygen, 18 amu represents H—O—H and H × H—O, 33 amu represents H × Represents a mixture of O × O and H × O—O, 36 amu represents a mixture of H × H—O—O × H × H and similar configurations, 37 amu represents H × H—O—O × H × A mixture of HxH and those representing equivalent composition are included, with a smaller proportion of new species expected to range from 8% to 9%.

  iii) 3 amu represents a mixture of H × H × H and H × H—H, 4 amu represents a mixture of H—H × H—H and equivalent composition, and a mass greater than 17 amu is expressed by the formula n × 1 + m There are many addable species represented by x16, on the order of ppm (where n and m are positive integer values such as 1, 2, 3, etc.), and new species are included in trace amounts. Yes.

Theoretical considerations described above, flammable HHO gas, can be integrated with the prediction that are composed of hydrogen atoms and oxygen atoms bonded to the cluster H _m O _n, where both, m and n Unless n is 0, m and n have positive integer values. Actually, when m = 1 and n = 0, it has atomic hydrogen. When m = 0 and n = 1, atomic oxygen O is contained. In the case of m = 2 and n = 0, it has the usual hydrogen molecule H ₂ = H—H or magnetic H × H. When m = 0 and n = 2, it has normal oxygen molecules O ₂ ═O—O or magnetic O × O. In the case of m = 1 and n = 1, it has a radical H—O or a magnetic H × O. When m = 2 and n = 1, it has a predicted new species of water vapor H—O—H or water H × H—O as shown in FIG. 3b. In the case of m = 3 and n = 2, it has magnetic H × HO—H or H × H × HO. When m = 3 and n = 3, it has magnetic H × H × HO × O or (H—O—H) × O.

As can be seen from the above, the “all” of the magnetic clusters predicted above has been confirmed experimentally, and m and n are positive integer values, except that both m and n are 0. from one symbol _H m _{O n} explain the chemical structure of the flammable HHO gas.

  The above definition of HHO gas clarifies the difference from the final form of brown gas.

  On June 30, 2003, a scientific measurement of the specific mass of HHO gas was at the Adsorption Laboratory in Dublin, Ohio. The result was 12.3 g per mol. This Dublin adsorption laboratory in Ohio repeated measurements with different sample gases and confirmed the results.

The published value of 12.3 g / mol is specific. A common prediction is that the HHO gas consists of a mixture of H ₂ and O ₂ because the HHO gas is generated from water. That the HHO gas is a mixture of H ₂ and O ₂ is a specific weight (2 + 2 + 32) /3=11.1 corresponding to a gas composed of volumes of 66.66% H ₂ and 33.33% O ₂ . It means a mixture of H ₂ and O ₂ at 3 g / mol.

This HHO gas thus has a singular form of 12.3-111.2 = 1 g / mol corresponding to a singular value of 8.8% of the specific mass. Thus, this HHO gas contains only 60.79% of ₂ amu species than the predicted 66.66% H ₂ and only 30.39% of 32 amu species than 33.33% O _2. Contains.

These measurements are a direct experimental confirmation that HHO gas has additional species rather than a single mixture of H ₂ and O ₂ . Furthermore, the HHO gas is generated from distilled water. Therefore, in order to account for the increased mass, there cannot be an excess of O ₂ above H ₂ . Thus, the above measurements indicate the presence in the HHO gas of 5.87% H ₂ and 2.94% O ₂ bound to species heavier than water that can be confirmed by mass spectroscopy.

  In addition, the Adsorption Laboratory in Dublin, Ohio, performed a gas chromatography scan of the HHO gas shown in FIG. 6 where most of the expected elements can be confirmed. Actually, in the scan shown in FIG. 6, the presence of the following types of HHO gas was confirmed at a decreasing value.

  1) 2 amu's first major species representing hydrogen in the indistinguishable combination of magnetic H × H species and molecular H—H species shown above.

  2) A second major material species of 32 amu representing the combination indicated above of the molecular OxO species and the molecular OO species.

  3) The only reasonable explanation is a large peak of 18 amu that can be confirmed below by other measurements to be a new form of the HxHO species, which is not water.

  4) An important peak at 33 amu, which is a direct experimental confirmation of a new species in HHO gas shown as H x H-O x H.

  5) A small peak of 16 amu representing atomic oxygen that can be clearly identified.

  6) A peak that can be clearly confirmed although smaller than 17 amu, which confirms the presence of a mixture of magnetic H × O and radical H—O.

  7) A small peak of 34 amu that confirms the presence of a new species (HO) × (HO) but can be clearly confirmed.

  8) A small but clearly identifiable peak of 35 amu confirming the prediction of the new species (HO) × (HO) × H.

  9) Many additional small peaks predicted to be on the order of ppm.

  Normally, infrared (IR) detectors are operating with other gases, whereas the same instrument operation is stopped for a few seconds following the injection of HHO gas. This behavior can only be explained by clogging of the supply tube with HHO gas via specific adhesion to the inner wall of the tube by magnetic induction, so this occurrence is a direct experimental confirmation of the magnetic characteristics of the HHO gas. However, along with the necessary stoppage of the equipment, clogging gradually occurred until the gas was prevented from being blown into the equipment due to the small cross-sectional area of the supply pipe.

The infrared scans shown in FIGS. 7-9 were performed on July 22, 2003 at a PdMA laboratory in Tampa, Florida, using a fixed point / single beam, Perkin Elma infrared scanner model 1600. The reported scans are 1) conventional H ₂ gas shown in FIG. 7, 2) conventional O ₂ gas shown in FIG. 8, and 3) HHO gas shown in FIG.

These scanning inspections show a substantial difference between HHO gas and H ₂ gas and O ₂ gas. H ₂ ═H—H and O ₂ ═O—O are symmetric molecules. Therefore, the infrared peaks of these H ₂ ═H—H and O ₂ ═O—O are very low, as can be seen in the attached scan. The first singular form of HHO shows a much stronger resonance peak. Thus, infrared scanning of HHO initially shows that the HHO gas is asymmetric, which is quite large since the same features are lacking with respect to the estimated mixture of H ₂ and O ₂ gases. It is a feature.

Furthermore, H ₂ gas and O ₂ gas have at most two resonance frequencies in infrared spectroscopy, one for vibration and one for rotation. The spherical distribution and other features of the orbit are confirmed by the scan shown in FIG. 7, while O ₂ has one oscillating infrared frequency and three rotational frequencies, as H ₂ can be confirmed by the scan shown in FIG. To have only one dominant infrared value.

  An infrared scan of the HHO gas shown in FIG. 9 reveals additional novelty. First, a scan of HHO gas reveals the presence of at least nine different infrared frequencies collected at about 3000 wavelengths and a separate infrared frequency at about 1500 wavelengths.

  These measurements show a very important experimental confirmation that the 18 amu species detected in the infrared scan shown in FIG. 6 is not added by water, directly indicating the potential of the new species H × HO. This is the result of the experiment.

  Indeed, the water vapor of the molecule H—O—H has wavelengths 3756, 3657, 1595, or combinations thereof, and infrared frequencies of these wavelengths. The HHO gas scan shown in FIG. 7 confirms the presence of an infrared value in the vicinity of 1595, so that molecular bond H—O can be confirmed in the magnetic structure H × HO, but this scan is performed with 3756 and 3657. Since it does not show the presence of an extra very strong trace of water molecules, it can be confirmed that the peak at 18 amu is not chemically conventional water.

  On July 22, 2003, the flash point was measured at a PdMA laboratory in Tampa, Florida. First, in a commercially available diesel fuel, the flash point of 75 ° C. was measured, and then the flash point of the same fuel following bubbling inside the HHO gas was measured, and the flash point of 79 ° C. was measured.

  In general, the addition of gas to liquid fuel is known to reduce the flash point of this liquid fuel in half, and for a mixture of diesel and HHO gas, the flash point value is expected to be about 37 ° C. These measurements are also specific. Thus, the specific increase in flash point value is about 42 ° C, not 4 ° C.

  Such an increase in flash point value cannot be explained by the assumption that HHO is contained in the diesel in the form of gas and requires the occurrence of a bond between the HHO gas and the liquid fuel. Liquid fuels cannot be of valence type, but are considered magnetic types due to the dielectric polarization of diesel molecules by magnetized HHO gas and the resulting attachment of HHO gas elements to the diesel molecules.

  The main experimental results of this magnetic type coupling were provided by the Southwest Laboratories of Texas on August 1, 2003, and the same “A” as used above for the flash point value of 75 ° C. Figure 10 shows a mass spectrometric measurement of one sample of normal diesel noted, and Figure 11 shows another sample of the same diesel as the internally bubbled HHO gas marked "B".

  These measurements were performed by total ion chromatography (TIC) by gas chromatography mass spectrometry GC-MS (manufactured by Hewlett-Packard) having GC model 5890 series II and MS model 59722. This total ion chromatography (TIC) was obtained with a distillate simulated by gas chromatography (SDGC).

  The column used was HP5MS30 × 0.25 mm. The carrier flow was 50 ° C. and 5 psi helium. The initial temperature of the injection was 50 ° C., the temperature was increased at 15 ° C. per minute and the final temperature was 275 ° C.

  The chromatography shown in FIG. 10 confirmed the typical pattern, extinction time and other characteristics of commercial diesel. However, the same diesel chromatography of the internally bubbled HHO gas shown in FIG. 11 has a large structure, including a very strong reaction in the scan, a larger extinction time, and a peak change for a larger amu value. Showing the difference.

  Thus, the chromatographic measurement shown in FIG. 11 can additionally confirm the presence of a bond between diesel and HHO gas, so that it can be accurately predicted by the unique value of the flash point. Similarly, the bond between a gas and a liquid cannot be of the valence type, but can clearly be of the magnetic type due to the diesel molecules with HHO magnesium and the resulting magnetic polarization in the bond.

  As a result, the presence of magnetically polarized HHO gas can be confirmed by the flash point and the measurement by the scanning experiment shown in FIGS.

Additional chemical analysis on the chemical composition of the HHO gas was performed at Air Toxic LTD, Folsom, California, with the scans shown in FIGS. 12-14, with H ₂ and O ₂ being the key components of the HHO gas. It was confirmed that.

  However, this measurement implies confirmation of the next specific peak.

a) Peak during H ₂ scan with 7.2 min extinction time as shown in FIG.

b) a large peak in the O ₂ scans at 4 minutes of disappearance time shown in FIG. 13.

  c) Many impurities contained in the HHO gas shown in FIG.

  FIG. 15 shows a specific blank of the detector, showing the residual material after gas removal. This blank shows the above scan peak preservation by magnetic induction, the occurrence explained solely by the magnetic polarization of the species, and the resulting adherence inside the instrument via magnetic induction, so after the HHO gas removal Blanks are specific.

  However, the equipment used in the scans shown in FIGS. 12-14 cannot be used to confirm the atomic weight, and thus the unique peak remains unconfirmed in this experiment.

However, it is known that species with larger mass disappear after some time. Thus, the species to disappear after detection of H ₂ and O ₂ is present is an additional direct experimental confirmation of the presence of H ₂ and O ₂ heavier species HHO gas, the additional experiments confirmed .

  The final mass spectrometric measurement with HHO gas is based on the recent GC-MS Claras 500, one of the most sensitive instruments capable of detecting hydrogen by Perkin Elma University of Tampa, Florida. On September 10, 2003.

  Even though the column used during the test was not suitable for the separation of all the species comprising HHO, the measurements were able to fully confirm the above predictions i), ii) and iii) for the structure of HHO gas.

  In fact, the scan shown in FIG. 16 can confirm the existence of 2 amu basic species in HHO representing H—H and H × H, although separation of the basic species is not possible with the GC-MS Claras 500. In addition, this apparatus cannot detect hydrogen atoms separated by insufficient ionization. Since helium is the carrier gas and the peak at 4 amu is removed by the scan shown in FIG. 16, the 4 amu species representing H—H × H—H could not be detected. However, it should be noted that there is a clean species of 5 amu that can only be described as H-HxH-HxH.

  The scan shown in FIG. 17 shows that the species of mass 16 amu confirming the presence of separated atomic oxygen in HHO is apparent, thereby preventing the separated hydrogen atoms from being detected by the instrument. Indicates indirect confirmation of the additional presence of. The scan shown in FIG. 17 shows the presence of 18 amu species in HHO gas by 17 amu species HO, H—O—H and H × HO, which separation is not possible with the above apparatus.

  The scan shown in FIG. 18 clearly shows the presence in HHO of 33 amu representing O—O × H or O—O—H and 34 amu species representing O—H × O—H and similar configurations. Thus, the species of 35 amu detected prior to measurement could be confirmed.

  The test also confirms that the “blank singularity” typical of all gases with a magnetic structure, ie the blank of the device after degassing, continues to detect the basic species and is scanned for simplicity. Thus, it was possible to confirm the unique attachment of O—H × O—H and a similar configuration of 34 amu species to the inner wall of the device, which can be explained only by magnetic polarization.

  As a result, all of the novel features were confirmed by multiple direct experiments.

I) Exceeding a specific mass of 1 g / mol (or 8.8%) can confirm the presence of species heavier than the expected mixture of H ₂ and O ₂ , thereby possibly having no valence bonds The presence of species composed of H and O atoms was confirmed.

  II) The infrared scan shown in FIG. 6 clearly identified all the new species expected for HHO gas. This confirmed the basic direct experiment.

  III) Infrared detectors normally operate on conventional gases, whereas the same infrared detector during the scan shown in FIG. 6 stops after 1 or 2 seconds of HHO gas injection, so This is a direct experimental confirmation of the presence of magnetic polarization in the HHO gas, as is normally detected for all gases having a structure. This is due to the clogging of the supply pipe due to the HHO species adhering to the wall of the supply pipe as a result of magnetic induction, and the subsequent automatic stop of the equipment itself due to the inability to inject HHO gas into the equipment. caused by.

  IV) A significant increase in flash point of diesel fuel following inclusion of HHO gas is the only possible explanation. In other words, it is probably not a valence type, but certainly shows a bond between a gas and a liquid that can be a magnetic type by magnetic induction, which is a direct and obvious experimental result of the magnetic polarization of HHO gas. Yes.

  V) The mass spectrometric measurement of the diesel and HHO mixture shown in FIGS. 10 and 11 is the final experimental confirmation of the bond between HHO and diesel. Similarly, this bond shows the nature of the species in HHO that magnetizes other atoms by magnetic induction, thus confirming the chemical composition of the HHO gas.

  VI) The additional scan shown in FIGS. 12-18 can confirm all of the above results, including the specific blank after HHO gas removal to confirm the magnetic polarization of the HHO gas.

  VII) The nature of HHO gas, which instantaneously dissolves tungsten and bricks, is separated and magnetically magnetized, in addition to the additional penetration by magnetic induction, which is a typical feature of all gases with a magnetic structure. This is the strongest physical confirmation of the presence in the HHO gas of hydrogen and oxygen atoms, i.e. atoms with a very reduced "thickness" that allows increased penetration of other materials in the layer.

Confirmation of experiments, with the exception that each of m and n has a value of 0, can be confirmed thoroughly description of HHO combustible gas with the symbol H _m O _n where m and n can be assumed that the positive integer . In fact, the various analytical measurements described above can confirm the presence of: Atomic hydrogen H (m = 1, n = 0); atomic oxygen O (m = 0, n = 1); hydrogen molecule H—H or magnetic H × H (m = 2, n = 0); Oxygen molecule OO or magnetic OxO (m = 0, n = 2); radical HO or magnetic HxO (m = 1, n = 1); water vapor HO-H or magnetic HxH -O (m = 2, n = 1); magnetic H * H * HO or H * HO * H (m = 3, n = 1); magnetic H * H * HO * O or H * H-O-O * H (m = 3, n = 2), etc.

  In order to easily understand some of the operation functions of the electrolytic cell, the general definition will be described below.

  The term “electrolyzer” means a device that causes a chemical change by passing a current through an electrolyte. Current is passed through the electrolyte by applying a voltage between the cathode and the anode immersed in the electrolyte. The electrolytic cell corresponds to an electrolysis chamber.

  The term “cathode” means the negative terminal or negative electrode of the electrolytic cell. The reduction basically occurs at the cathode.

  The term “anode” means the positive terminal or positive electrode of the electrolytic cell. Oxidation basically occurs at the cathode.

  The term “electrolyte” means a substance that becomes an ionic conductor when dissolved in a suitable solvent or when fused. The electrolyte is used to conduct electricity between the anode and the cathode in the electrolytic cell.

  The term “internal combustion engine” refers to various engines in which a mixture of fuel and air burns within the engine itself so that hot gas combustion products act directly on the surface of the moving parts of the engine. Examples of the movable part include, but are not limited to, a piston or a turbine rotor blade. Internal combustion engines include gasoline engines, diesel engines, gas turbine engines, jet engines, and rocket engines.

  A description will be given with reference to FIG. 19 showing an exploded view of the electrolytic cell. The electrolytic cell 2 has an electrolytic chamber 4 that holds an electrolytic solution. The electrolysis chamber 4 is coupled to the cover 6 by a flange 8. The electrolysis chamber 4 and the cover 6 are preferably sealed with a neoprene gasket 10 installed between the flange 8 and the cover 6. The electrolyte may be an electrolyte that produces a mixture of an aqueous electrolyte of water and a novel gas. However, it is preferable to use distilled water as the electrolytic solution in order to generate a new and specific gas.

  The electrolyte partially fills the electrolysis chamber 4 to level 10 so that during operation a gas storage area 12 is formed on the aqueous electrolyte. The electrolytic cell 2 includes an anode electrode 14 and a cathode electrode 16 which are two main electrodes at least partially immersed in an aqueous electrolyte. These anode electrode 14 and cathode electrode 16 are inserted into a groove 18 in the rack 20. The rack 20 is installed in the electrolysis chamber 4. One or more auxiliary electrodes 24, 26, 28, 30 are also installed in the rack 20. Note that not all auxiliary electrodes are shown in FIG. The auxiliary electrodes 24, 26, 28, and 30 are at least partially immersed in an aqueous electrolyte and are disposed between the anode electrode 14 and the cathode electrode 16. Further, the anode electrode 14, the cathode electrode 16, and the auxiliary electrodes 24, 26, 28, 30 are held at fixed positions by the rack 20. The anode electrode 14, cathode electrode 16, and auxiliary electrodes 24, 26, 28, 30 are preferably separated from each other by a distance of about 0.25 inches. As shown in FIG. 19, the anode electrode 14, the cathode electrode 16, and the auxiliary electrodes 24, 26, 28, and 30 do not have to be flat, but are generally formed of a substantially flat material. One or more auxiliary electrodes allow for an improved and efficient production of the gas mixture. It is preferable that 1 or more and 50 or less auxiliary electrodes are arranged between the two main electrodes. Further, it is more preferable that 5 or more and 30 or less auxiliary electrodes are arranged between these two main electrodes, and about 15 auxiliary electrodes are arranged between the two main electrodes. Most preferably. Each of these two main electrodes is preferably a metal wire mesh, a metal plate, or a metal plate having one or more holes. Each of these two main electrodes is more preferably a metal plate. Suitable metals that form these two main electrodes include, but are not limited to, nickel, nickel alloys, and stainless steel. The preferred metal for these two main electrodes is nickel. The plurality of auxiliary electrodes are preferably a metal wire mesh, a metal plate, or a metal plate having one or more holes. Each of the plurality of auxiliary electrodes is more preferably a metal plate. Suitable metals for forming these auxiliary electrodes include, but are not limited to, nickel, nickel alloys, stainless steel, and the above foam.

  Further, as shown in FIG. 19, during operation of the electrolytic cell 2, a voltage is applied between the anode electrode 14 and the cathode electrode 16, and a new gas is generated and collected in the gas storage region 12. The gas mixture stored in the gas storage region 12 passes through the outlet 31, exits the gas storage region 12, and is finally supplied to the fuel system of the internal combustion engine. The anode electrode 14 is in electrical contact with the contactor 32, and the cathode electrode 16 is in electrical contact with the contactor 33. The contactors 32 and 33 are made of metal, and grooves 34 and 35 are formed so as to be located at the anode electrode 14 and the cathode electrode 16. The contactor 32 is attached to a rod 37 inserted through a hole 36 provided in the cover 6. Similarly, the contactor 33 is attached to a rod 38 inserted through a hole 40 provided in the cover 6. Preferably, the holes 36, 40 are threaded and the rods 37, 38 are threaded rods that are screwed into the holes 36, 40. Since the anode electrode 14 and the cathode electrode 16 are held at predetermined positions by the paths 34 and 35 and the groove 18 of the rack 20, the contactors 32 and 33 also hold the rack 20. Therefore, all of these contactors 32 and 33, rack 20, groove 18 and paths 34 and 35 function as holding means for holding each anode electrode 14 and cathode electrode 16 in parallel with each other at a predetermined position. Therefore, when the cover 6 is fastened to the electrolysis chamber 4 with bolts, the rack 20 is held at the lower portion of the electrolysis chamber 4. The electrolytic cell 2 optionally has a pressure safety valve 42 and a level sensor 44. The pressure relief valve 42 releases the gas mixture in the gas storage area before the pressure increases excessively. The level sensor 44 sounds an alarm when the electrolyte is too low and reliably stops the gas flow to the vehicle fuel system. When there is little electrolyte solution, an additional electrolyte solution is added from a water inlet. Moreover, the electrolytic cell 2 may be equipped with the pressure gauge 48 so that the pressure of the electrolysis chamber 4 may be monitored. Further, the electrolytic cell 2 functions as an external heat treatment cell and optionally has one or a plurality of fins 50 for removing heat from the electrolytic cell 2. As can be seen from FIG. 19 and the above, this electrode tank can be used as a closed system or a pressurized system by appropriately operating the pressure of components and piping connected to the electrode tank.

  A modification of the electrolytic cell will be described with reference to FIG. As shown in FIG. 19, the auxiliary electrodes are not electrically connected to each other. Output is provided only for each of the anode and cathode electrodes. In the embodiment shown in FIG. 20, a first group of one or more auxiliary electrodes 52, 54, 56, 58 is connected to the anode electrode 14 by a first metal conductor 70, and one or more auxiliary electrodes. The second group of electrodes 62, 64, 66, 68 is connected to the cathode electrode 16 by a second metal conductor 60. Similarly to FIG. 19, these auxiliary electrodes may be made of the above-mentioned foam material, and these auxiliary electrodes are made of stainless steel or similar to the electrode foam material of the electrode tank shown in FIG. It may be. A mechanism for fixing the electrode plate will be described with reference to FIG. 21 which is a perspective view. The anode electrode 14, the cathode electrode 16, and the auxiliary electrodes 24, 26, 28, 30 are held and fixed by holder rods 72 inserted into the path 74 of the rack 20, and the path 74 is within the groove 18 of the rack 20. Has been inserted. Note that not all of the auxiliary electrodes are shown in FIG.

  The rack 20 is preferably made of a highly dielectric plastic such as PVC (polyvinyl chloride), polyethylene, or polypropylene. Further, the rack 20 holds the anode electrode 14, the cathode electrode 16, and the auxiliary electrodes 24, 26, 28, and 30 in a fixed positional relationship. The fixed positional relationship between the two main electrodes and the plurality of auxiliary electrodes is such that the two main electrodes and the plurality of auxiliary electrodes are substantially parallel, and each of the main electrodes and the plurality of auxiliary electrodes is approximately 0.38 cm (0.15 inch), respectively. It is preferable that the distance is about 0.89 cm (0.35 inches) or less from the adjacent electrodes. Further, it is more preferable that each of these main electrodes and auxiliary electrodes are separated from the adjacent electrodes by a distance of about 0.2 inch or more and about 0.3 inch or less, and most preferably about 0.25 inch. This fixed positional relationship is held by a rack that holds the two main electrodes and the plurality of auxiliary electrodes in a fixed positional relationship. The two main electrodes and the plurality of auxiliary electrodes are attached to a groove in a rack that holds the electrodes apart. In addition, the two main electrodes and the plurality of auxiliary electrodes can be removed from the rack so that the two main electrodes and the plurality of auxiliary electrodes or racks can be replaced as needed. Further, as described above, the rack 20, the anode electrode 14, and the cathode electrode 16 are held at predetermined positions, and the auxiliary electrodes are also fixed to the rack 20 by the holder rod 72, so these auxiliary electrodes are also held at the predetermined positions. Has been.

  In a further preferred modification of the electrode configuration shown in FIGS. 19 and 20, FIG. 25 shows that the auxiliary electrodes 24, 26, 28, 30... Are unclear, and a plurality of anode electrodes 14 and cathode electrodes 16 are connected to a power source. It shows a configuration that is connected to the output in a state where it is not. The auxiliary electrode is located between the flat anode electrodes 14, between the flat cathode electrodes 16, or between a predetermined flat cathode electrode 16 and the flat anode electrode 14, and the output is enclosed. It is given to a certain electrolysis chamber 4. With this configuration, a uniform voltage can be applied across the plate-like electrode.

  FIG. 22 and FIG. 23 show a configuration that includes an internal combustion engine and represents an electrolytic cell piping system and electrical operation. During operation, a new combustible gas is generated by electrolysis of the electrolyte in the electrolytic cell 2. The electrolytic cell 2 is connected to the recovery tank 80 by a pressure line 82. The combustible gas is recovered and temporarily stored in the recovery tank 80. The recovery tank 80 optionally includes a pressure relief valve 84 that can protect against any excessive pressure increase. The recovery tank 80 is connected to a solenoid 86 by a pressure line 88. The solenoid 86 is sequentially connected to the engine intake manifold 92 of the engine 94 by a pressure line 90. An anti-flame 96 is optionally attached to the pressure line 90 to prevent the flame from spreading in the pressure line 88. Furthermore, the pressure line 90 has a hole 97 that restricts the gas mixture from flowing into the engine intake manifold 92. The size of this hole depends on the size of the engine. For example, a hole diameter of about 0.04 inch is suitable for a 1 liter engine, a hole diameter of about 0.06 inch is suitable for a 2.5 liter engine, and a hole diameter of about 0.075 inch is Suitable for V8 engine. The voltage applied to the electrolytic cell 2 is supplied by the electrolytic cell battery 100 via the solenoid 98. When the pressure in the recovery tank 80 drops below about 25 psi, the solenoid 98 is switched and a voltage of about 12V is applied between the anode and cathode electrodes of the electrolytic cell 2. The battery insulator 102 allows the vehicle battery 104 and the electrolytic cell battery 100 to be charged by the AC generator 106, and maintains electrical insulation between the electrolytic cell battery 100 and the vehicle battery 104. Further, when the main switch 108 is operated, power is supplied to the solenoid 98 by the vehicle battery 104. When power is supplied to the gas mixing solenoid 86 by the vehicle battery 104 and the gas mixture is supplied to the engine intake manifold 92, the gas mixing solenoid 86 is opened. The solenoid 86 receives feedback from the level sensor 44 that stops the flow of gas to the solenoid 86 when the amount of the electrolytic solution in the electrolytic cell 2 becomes too small. Furthermore, when used in a vehicle, the operation of the vehicle's oxygen sensor needs to be adjusted to account for the additional oxygen added from the electrolytic cell to the fuel system. Typically, if the oxygen sensor senses more oxygen, the vehicle computer determines that the engine is running at an incline and opens the fuel injector so that there is more fuel mixture. This is not appropriate and causes a deterioration in fuel efficiency. The electric wires 110 and 112 of the oxygen sensor 114 are preferably provided with an RC circuit 116. The RC circuit 116 has a resistor 118 and a capacitor 120. The resistor 118 is preferably about 1 mΩ and the capacitor 120 is preferably about 1 mF. The electric wire 110 is a check engine light signal, and the electric wire 112 transmits a control signal related to the amount of oxygen in the vehicle exhaust. The resistor 118 is in series with the electrical wire 110 and ensures that the vehicle control system reads the oxygen sensor to operate correctly. Similarly, the capacitor 120 signals the vehicle computer to prevent accidental opening of the vehicle fuel injector when gas from the electrolyzer 2 is supplied to the fuel system. Further, the main switch 108 activates the RC circuit when gas is supplied, for example, when the electrolytic cell is used, and stops the RC circuit when gas is not supplied.

  Another embodiment of the invention is a method for improving the fuel efficiency of an internal combustion engine. In this method, the above-described electrolytic cell is used together with the internal combustion engine. In particular, the method further comprises the steps of providing an electrolyzer system as described below in the above or other novel embodiments, and a new combustible gas is generated and recovered in the gas storage area, Applying a potential between electrodes provided to deliver a combustible gas to the internal combustion engine fuel system, and mixing the fuel in the internal combustion engine fuel system and the generated combustible gas. is doing. There is also a step of adjusting the operation of the oxygen sensor described above.

  FIG. 24, which is a flow diagram of another embodiment of a hydrogen and oxygen gas electrolyzer generator system 300, shows a configuration formed for use with a welded cut combustion type system. This system can also be incorporated and used in other types of systems where heat or combustion is desired. The system 300 includes an electrolyte container 318 having an upper part and a lower part and having an electrolytic solution 319 therein. Here, the electrolytic solution is preferably water. The electrolyte container 318 includes a torn or permeable plate 320 positioned so that the periphery of the upper part of the electrolyte container 318 can be sealed. The plate 320 has a function of releasing the gas pressure in the electrolyte container 318 when a predetermined pressure value is exceeded.

  Further, the self-generated hydrogen oxygen gas generation system 300 includes a pump 316, preferably an electromagnetic pump, having one end connected to the lower part of the electrolyte container 318. The other end of the pump 316 is connected to at least one hydrogen and oxygen electrolyzer generator 312 having a conductor 352 therein. One end of the conductor 352 is grounded. The other end of the conductor 352 on the opposite side is electrically connected to one end of the pressure controller 328. Further, the other end of the conductor 352 is electrically connected to a power source. The pump 316 functions to circulate the electrolyte 319 from the electrolyte container 318 through the gas pipe 350, through the radiator 314, through the at least one hydrogen and oxygen electrolyzer generator 312 and back to the electrolyte container 318. Have. The radiator 314 has a function of cooling the generated hydrogen and oxygen gas before returning to the electrolyte container 318.

  The pressure controller 328 is connected to the electrolyte container 318 and monitors the pressure in the electrolyte container 318. When the gas pressure in the electrolyte container 318 exceeds a predetermined value, the current is processed by the conductor 352 in the hydrogen and oxygen electrolyzer generator 312 to stop the generation of hydrogen oxygen gas. When the gas pressure in the electrolyte container 318 falls below a predetermined value, the current is processed by the electrical conductor 352 in the hydrogen and oxygen generator 312 to initiate the generation of hydrogen oxygen gas. The predetermined value is less than that required to cause pressure relief through the plate 320.

  This self-generated on-demand hydrogen oxygen generation system 300 includes a check valve 322 having one end connected to the upper end of an electrolyte container 318 below the plate 320. Further, the other end of the check valve 322 is connected to the drying filter means or the tank 332.

  In addition, the system 300 includes other drying filter means or tank 330 that is in fluid communication with one end of the electrolyte container 318 on the plate 320 and is further connected via a gas line 342 to another check. The other end on the opposite side is connected to the valve 344. The other end of the gas pipe 342 is connected to other dry filter means or a tank 332.

  Further, the system 300 includes a pressure reducing valve 326 that is communicated with one end of the system 300 to the upper end of the electrolyte container 318 so that fluid can be activated and communicated with the gas pipe 350 so that the fluid can move. Yes. The gas pipe 350 is connected to the radiator 314.

  The welding system 300 further includes a direct current amperage adjustment device 305 controlled by a microprocessor provided to regulate direct current amperes from the power source to the hydrogen and oxygen electrolyzer generator 312. A first disconnecting switch 306 controlled by the microprocessor is used to stop supplying power to the welding machine in response to an abnormality of the pump 316.

  A second disconnect switch 307 controlled by the microprocessor is used to stop supplying power to the welder in response to insufficient electrolyte conditions in the electrolyte vessel 318. A microprocessor controlled liquid crystal display 308 is used to display operational statistics relating to the welding system 300 including operating time, amperage values, indicator lights and pressure gauge readings. The liquid crystal display receives input from a plurality of locations within the system 300.

  A microprocessor controlled polarity change system 309 is used to change the polarity of the conductors located in the hydrogen and oxygen electrolyzer generator 312. A microprocessor controlled cooling system 313 is used to operate the generator fan 311 and pump 316 and continues fan and pump operation throughout the entire cooling phase following manual shut down of the system 300.

  The produced gas or HHO gas is finally sent from the drying means 332 to the gas reservoir 336. The drying means 330 and 332 are merely examples. In order to effectively achieve the same purpose, it may be designed as the same unit. The gas is then supplied directly to the engine or, in this case, the welding apparatus, via gas pipe 348, check valve 338, which is a hydrogen flush suppression check valve, and control valve 340.

  In any of the embodiments described above, a safety device of at least one of a hydrogen flash suppressor and a check valve may be added to any device or system where appropriate.

  Moreover, although each said embodiment was described exemplarily, these embodiment is only what described all the forms of this invention exemplarily. Precisely, the terms in the specification are limited description terms and various changes may be made without departing from the spirit and scope of the invention.

a is a figure which shows the conventional hydrogen atom which forms a sphere with distribution of the electron orbit to the whole space direction. b is a diagram showing similar hydrogen atoms whose orbits are magnetized in an annular surface where electrons generate a magnetic field along the rotation axis of the annular surface. a is a diagram showing a conventional hydrogen molecule with some of the rotations caused by temperature. b is a diagram showing a conventional molecule in which two magnetic fields are generated in opposite directions because the orbits are magnetized into an annular surface and hydrogen molecules are diamagnetic. a is a conventional water molecule H— in which the dimers HO and OH form an angle of 105 ° and the orbits of two H atoms are magnetized into an annular plane perpendicular to the HO—H plane. It is a figure which shows OH. b is a diagram showing a central species of the present invention composed of water molecules in which one valence bond is broken and the other one hydrogen atom collapses. a is a figure which shows the conventional hydrogen molecule magnetized. b is a diagram showing the bond between two hydrogen atoms, which is the main species of the present invention and is generated by the attractive force between opposite magnetic poles starting from the circular polarization of the orbit. Two dimers HO of water molecules in magnetized form, such as occurs in water molecules with magnetically bound hydrogen atoms that are separated and magnetized bonded to the resulting magnetic bond. It is a figure which shows the novel chemical species confirmed for the first time by this invention comprised by. It is a figure which shows the mass spectroscopic scanning of the HHO gas of this invention. It is a figure which shows the infrared scanning of the conventional hydrogen gas. It is a figure which shows the infrared scanning of the conventional oxygen gas. It is a figure which shows the infrared scanning of the HHO gas of this invention. It is a figure which shows the mass spectrometry of a commercially available diesel fuel. It is a figure which shows the mass spectrometry of the same diesel fuel as FIG. 10 in the state by which the HHO gas of this invention was absorbed inside through foaming. It is a figure which shows the analytical detection of the hydrogen content of the HHO gas of this invention. It is a figure which shows the analytical detection of the oxygen content of the HHO gas of this invention. It is a figure which shows the analysis detection of the impurity contained in the HHO gas of this invention. FIG. 6 shows a detector specific blank showing residual material after gas removal. It is a figure which shows the scanning which confirms presence in HHO gas of 2amu basic species which represents H-H and HxH, and presence of 5amu clean species which can be explained only by H-HxH-HxH. . The presence of the separated atomic oxygen in the HHO gas was confirmed in order, and the 17 amu species and the 18 amu species in the HHO gas composed of H—O, H—O—H, and H × HO— It is a figure which shows the scan for confirming the clear description of the seed of mass 16amu which confirms existence. It is a figure which shows the scan for confirming presence in the HHO gas of 33amu showing O-OxH or O-O-H, and the species of 34amu showing O-HxOH or the same structure. . It is an exploded view showing an electrolytic cell. It is a top view which shows the modification of the electrolytic cell with which the 1st group of the auxiliary electrode was connected to the anode electrode, and the 2nd group of the auxiliary electrode was connected to the cathode electrode. It is a perspective view which shows the mechanism which fixes the electrode plate of the electrolytic cell shown in FIG. It is the schematic of piping which shows integration of the electrolytic cell when using for a vehicle. It is the electrical schematic which shows integration of the electrolytic cell when using it for a vehicle. It is the schematic which shows an electrolytic cell when using it for a welding system. It is a figure which shows the modification by which the output was connected to the some anode electrode and cathode electrode in the state in which the auxiliary electrode was connected to the electrolysis chamber without connecting to a power supply.

Claims (13)

An electrolytic cell that separates water into a high hydrogen content flammable gas,
A pressurizable electrolysis chamber;
An aqueous electrolyte that contains water and is partially filled into the electrolysis chamber such that a gas storage region is formed thereon;
Means for adding the aqueous electrolyte to the electrolysis chamber during operation of the electrolyzer;
Two or more main electrodes each having one or more anode electrodes and one or more cathode electrodes, at least partially immersed in the aqueous electrolyte;
A plurality of auxiliary electrodes that are at least partially immersed in the aqueous electrolyte solution and maintained in a fixed positional relationship between the main electrodes;
One of the adjacent auxiliary electrodes is formed of a highly porous mesh-like foam material made of a substantially nickel material, and the other opposite electrode is formed of a substantially stainless steel material. These auxiliary electrodes are formed in the electrolytic cell. An electrolyzer that produces a current that causes the production of a single combustible gas across the entire surface area on both sides of all electrodes, or a flow of positive (+) and negative (-) ions. Two or more main electrodes are connected to a power source, and an auxiliary electrode is not connected to the power source and is arranged between the two or more main electrodes, or the first group of the auxiliary electrodes is a first metal conductor Connected to one or more anode electrodes, the second group of auxiliary electrodes connected to one or more cathode electrodes by a second metal conductor, or two or more main electrodes connected to a power source, Electrodes are not connected to the power source but are arranged between adjacent anode electrodes, between adjacent cathode electrodes, and between adjacent anode electrodes and cathode electrodes, and the power source is grounded to the electrolytic chamber. The electrolytic cell according to claim 1.   The electrolytic cell of claim 1, wherein adjacent electrodes are spaced apart by a distance of from about 0.15 inches to about 0.35 inches.   The electrolytic cell further includes a rack that holds two or more main electrodes and a plurality of auxiliary electrodes in a fixed positional relationship, and the two or more main electrodes and the plurality of auxiliary electrodes are movably attached to the rack. The electrolytic cell according to claim 1.   The electrolytic cell according to claim 1, wherein the rack is made of a highly dielectric plastic including any of polyvinyl chloride, polyethylene, and polypropylene. When used in an on-demand self-generated flammable gas electrolyzer system that separates water into flammable gas for use in any of the welding equipment, cutting equipment, melting equipment, and combustion equipment including internal combustion engines,
This electrolytic cell system
An electrolyte container;
A pump provided between a lower portion of the electrolytic solution container and the electrolytic cell, and taking out an aqueous electrolytic solution from the electrolytic solution container and supplying the aqueous electrolytic solution to the electrolytic cell;
A radiator that is provided between the electrolytic cell and the electrolytic solution container and cools the generated combustible gas before returning it to the upper part of the electrolytic solution container;
A space for accumulating the generated combustible gas on the aqueous electrolyte that is an upper part in the electrolyte container;
2. An electrolyzer according to claim 1 comprising at least one drying and filtering means through which the generated combustible gas passes before it is removed as required. A method for improving any of fuel efficiency of an internal combustion engine, cutting efficiency of a welding system, and welding efficiency,
A pressurizable electrolysis chamber, an aqueous electrolyte containing water and partially filled in the electrolysis chamber so that a gas storage region is formed on the top, and the aqueous electrolyte is added to the electrolysis chamber during operation Means, two or more main electrodes having one or more anode electrodes and one or more cathode electrodes, at least partially immersed in the aqueous electrolyte, and at least partially immersed in the aqueous electrolyte A plurality of auxiliary electrodes held in a fixed positional relationship between the main electrodes, and one of the adjacent auxiliary electrodes is a mesh-like foam having high porosity, one of which is made of a substantially nickel material. And the other opposite is made of a generally stainless steel material, and these auxiliary electrodes have a current that causes the production of a single flammable gas over the entire surface area on both sides of all electrodes in the electrolytic cell, or plus (+) And minor (-) providing an electrolytic cell to generate a flow of ions,
Applying a potential between the electrodes where the combustible gas is generated;
Providing a means for delivering the combustible gas to an end use. Two or more main electrodes are connected to a power source, and an auxiliary electrode is not connected to the power source and is arranged between the two or more main electrodes, or the first group of the auxiliary electrodes is a first metal conductor. Or connected to a plurality of anode electrodes, the second group of auxiliary electrodes is connected to one or more cathode electrodes by a second metal conductor, or two or more main electrodes are connected to a power source, and the auxiliary electrodes Are not connected to the power source and are arranged between adjacent anode electrodes, between adjacent cathode electrodes, and between adjacent anode electrodes and cathode electrodes, and the power source is grounded to the electrolytic chamber. The method of claim 7.   The method of claim 7, wherein adjacent electrodes are spaced apart by a distance between about 0.15 inches and about 0.35 inches.   The electrolytic cell further includes a rack that holds two or more main electrodes and a plurality of auxiliary electrodes in a fixed positional relationship, and the two or more main electrodes and the plurality of auxiliary electrodes are movably attached to the rack. The method of claim 7.   8. The method of claim 7, wherein the rack is constructed of a highly dielectric plastic including polyvinyl chloride, polyethylene or polypropylene.   8. The method of claim 7, further comprising adjusting the operation of the oxygen sensor so as not to cause combustion conditions that are high in oxygen. The operation of the oxygen sensor is adjusted by the RC circuit,
This RC circuit
A register arranged in series with the check engine photoelectric line of the oxygen sensor;
A capacitor disposed between a control line of the oxygen sensor for monitoring the amount of oxygen and the check engine photoelectric line;
The method of claim 12, wherein the capacitor is attached to the check engine photoelectric line opposite the resistor at a location where the resistor is in electrical contact with the oxygen sensor.

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